1. Section 219.605 Compliance Plan (Repealed)
      2. interim dates as required in 35 Ill. Adm. Code 201.242.
    1. Section 219.608 Operating Practices for Petroleum Solvent Dry
    2. Cleaners
    3. In order to minimize fugitive solvent emissions, the owner or
    4. a) General Housekeeping Requirements
    5. covered except when in use.
    6. load transfer.
      1. 25322-01-4 Nitropropane
      2. 1321-12-6 Nitrotoluene
      3. 156-43-4 p—phenetidine108—95—2 Phenol98-67-9, Phénolsulfonic acids585—38—6,
      4. 609—46—1,133_39_7c91-40-7 Phenyl anthranilic acid
      5. Phenylenediamine75-44-S Phosgene
      6. 2.2 Captured Emissions Volumetric Flow Rate.
      7. emissions at point i, ppm propane--j
      8. emissions at point j, ppm propane--~j
      9. concentration gas, ppm propane-ri
      10. calibration gas, ppm propane-.-~
      11. measured at point i, ppm propane-~
      12. point j, ppm propane-~
    7. emissions for conducting the drift checks. Introduce the zero
    8. and calibration gas at the calibration valve assembly and verify
    9. that the appropriate gas flow rate and pressure are present at
    10. calibration gas, ppm propan*rj.
      1. 7. CALCULATIONS
      2. 3.2 Determination of Flow Rates.
      3. 2. APPARATUS AND REAGENTS

ILLINOIS POLLUTION CONTROL
BOARD
September
9,
1993
IN THE MATTER OF:
)
OMNIBUS
CLEANUP
OF THE VOLATILE
ORGANIC MATERIAL RACT RULES
)
R93-9
APPLICABLE TO OZONE NONATTAINMENT
)
(Rulemaking)
AREAS:
AMENDMENTS TO 35 ILL. ADM.
)
CODE PARTS
203,
211,
218
AND
219.
)
Adopted Rule.
Final
Order.
ORDER OF THE
BOARD
(by B. Forcade):
On March 16,
1993,
the Illinois Environmental Protection
Agency
(Agency)
filed this proposal for rule making.
This
proposal was filed pursuant to section 28.5
of the Environmental
Protection Act.
(415 ILCS 5/28.5
(1992).)
The proposal
represents one part of Illinois’ submittal of a complete state
implementation plan
(SIP).
Pursuant to section 182(a)
of the
Clean Air Act
(CAA), as amended in 1990,
Illinois was to adopt
and submit its plan by November 15,
1992.
The Board adopted the
First Notice Opinion and Order
in this proceeding without comment
on the substance of the rule on March 25,
1993.
The proposed
amendments were published in the Illinois Register on April
9,
1993 at 17
Ill. Reg.
4782
(Part 211),
17
Ill.
Reg.
4898
(Part
203),
17 Ill.
Reg.
4905
(Part 218)
and
17 Ill. Reg.
5169
(Part
219).
A correction to the proposed rules,
adding some pages of
the proposed rule that were omitted from the initial publication,
was published in the Illinois Register on April
23,
1993 at 17
Ill.
Reg.
6520
(Part 218)
and 17 Ill.
Reg.
6539
(Part 219)
On July 22,
1993,
the Board adopted the second notice opinion and
order and submitted the second notice to the Joint Committee on
Administrative Review (JCAR).
A certification of no objection
from JCAR was received on August 30,
1993.
Today the Board acts to adop~this proposal.
This order is
supported by
a separate opinion adopted on the same day.
The
Board directs the Clerk of the Board to cause the filing of the
following adopted amendments with the Code Division of the
Secretary of State’s Office.
The complete text of the proposed
rules follows.
IT IS SO ORDERED.
I,
Dorothy M. Gunn,
Clerk of the Illinois Pollution Control
Board, do hereby~~tifythat the
ove order was adopted by the
Board on the
7~i~
day of
________________,
1993,~.by a vote
of
___________
.
~
7~
/~-/~
~
Dorothy M. ,~inn, Clerk
Illinois PbLlution Control Board

2
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE B:
AIR POLLUTION
CHAPTER I:
POLLUTION CONTROL BOARD
SUBCHAPTER a:
PERMITS
AND
GENERAL PROVISIONS
PART 203
MAJOR STATIONARY SOURCES CONSTRUCTION
AND
MODIFICATION
SUBPART A:
GENERAL PROVISIONS
Definitions
Actual Construction
Actual Emissions
Allowable Emissions
Available Growth Margin
Building,
Structure and Facility
Commence
Construction
Dispersion Enhancement Techniques
Emission Baseline
Emission Offset
Emissions Unit
Federally Enforceable
Fugitive Emissions
Installation
Lowest Achievable Emission Rate
Nonattainment Area
Potential to
Emit
Reasonable Further Progress
Secondary Emissions
Stationary Source
Volatile Organic Material (Repealed)
Public Participation
Severability
(Repealed)
SUBPART
B:
MAJOR STATIONARY SOURCES IN NONATTAINNENT AREAS
Section
203.201
Prohibition
203.202
Coordination
with
Permit
Requirement
and
Application
Pursuant to 35 Ill.
Adm. Code 201
Construction Permit Requirement and Application
Duration of Construction Permit
(Repealed)
Effect of Permits
Major Stationary Source
Major Modification of a Source
Net Emission Determination
Significant Emissions Determination
Relaxation of a Source-Specific Limitation
Permit Exemption Based on Fugitive Emissions
Section
203. 101
203.103
203.104
203.107
203.110
203.112
203.113
203.116
203.117
203.119
203.121
203.122
203.123
203.124
203.125
203.126
203.127
203.128
203.131
203.134
203. 136
203.145
203.150
203.155
203.203
203.204
203.205
203.206
203.207
203.208
203
.
209
203.210
203.211

3
SUBPART C:
REQUIREMENTS FOR MAJOR STATIONARY SOURCES IN
NONATTAINMENT AREAS
203.301
Lowest Achievable Emission Rate
203.302
Maintenance of Reasonable Further Progress and Emission
Offsets
203.303
Baseline and Emission Offsets Determination
203.304
Exceptions from Emissions Offset Requirement
(Repealed)
203.305
Compliance by Existing Sources
203.306
Analysis of Alternatives
SUBPART
F:
OPERATION OF A MAJOR STATIONARY SOURCE OR MAJOR
MODIFICATION
Section
203.601
Lowest Achievable Emission Rate Compliance Requirement
203.602
Emission Offset Maintenance Requirement
203.603
Ambient Monitoring Requirement
(Repealed)
SUBPART G:
GENERAL MAINTENANCE OF EMISSION OFFSETS
Section
203.701
General Maintenance of Emission Offsets
SUBPART H:
OFFSETS FOR EMISSION INCREASES FROM ROCKET ENGINES
AND MOTOR FIRING
Section
203.801
Offsets for Emission Increases from Rocket Engines and
Motor Firing
AUTHORITY:
Implementing Section 9.1 and 10 and authorized by.
Section 27 and 28.5 of the Environmental Protection Act
(Ill.
Rev.
Stat.
1991,
ch.
111½, pars.
1009.1,
1010 and 1027)
(P.A.
87—
1213,
effective September 26,
1992)
415
ILCS 5/9.1,
10,
27, and
28.5.
SOURCE:
Adopted and codified at 7
Ill.
Reg.
9344, effective July
22,
1983; codified at
7 Ill.
Reg.
13588; amended in R85—20 at 12
Ill.
Reg.
6118,
effective March 22,
1988;
amended in R9l-24 at 16
Ill.
Reg.
13551, effective August 24,
1992; amended in R92-21 at
17
Ill.
Reg.
6973, effective April 30,
1993; amended in R93—
_____
at 17
Ill. Reg.
_________,
effective
____________________

4
Section 203.145
Volatile Organic Material
(Repealed)
“Volatile organic material”
(VON)
means any compound of carbon,
excluding carbon monoxide,
carbon dioxide,
carbonic acid,
1-n111r~
rnrhiti~~
nr
ci-hriic~t~~
~
ammonium arbonate,
~..rhirth
participa
a)
This includes any such organic compound other than the
following,
which have been determined to have
negligible photochemical reactivity:
Methane;
ethane;
methylene chloride (dichlormethanc),
1,1,1
trichlorethanc
(methyl chloroform),
1,1,1 trichioro
2,2,2 trifluoroethanc
(CFC 113); trichlorofluoromethane
(CFC 11); dichlorodifluoromethane
(CFC 12);
chiorodifluoromethane
(CFC 22); trifluoromethane
(FC
23); 1,2 dichloro 1,1,2,2 tetrafluoroethane
(CFC 114);
e
~
CFC 115)
,
1, 1,
1
trif1........~.
.~
dich1oro~thnn~
(HCFC
123);
1,1,12
tetrafluoroethane
A
S
.!
~
‘I
~fl
‘I
.A_ 1_
I
VT
*fl
A
I_
S
t.~
‘~~
1,1
aicnioro
i.
~iuoroetnunc
~UL~L
i4iD);
chioro
1,1
difluoroethane
(HCFC
142b);
2
chioro
~
(HCF(~
1~4~
f1~i~hny,,-
1,1,1,2
(HFC!
i~j;
1,1,2,~.tctrar.Luoroctru:lne
(HFC 134);
1,1,1
trifluoroethane
(HFC 143a);
1,1 difluroethane
(HFC
152a); and perfluorocarbon compounds which fall into
th~~i~
c~1
~
1
~
-..
1)
Cyclic,
branched,
or linear,
completely
fluorinated alkanes;
~)
r~1ir~
r~,-
completely
I
fluorinated
-
c,
branched,
or
mated
tertiary
•1
completely
4)
Sulfur containing perfluorocarbons with no
unsaturations and with sulfur bonds only to carbon
b)
For purposes of determining VOM emissions and
eempl
-~‘~
~
~
will
be
I
I
r~
i
~
T.J
I
U~fl
~Ffl
1
~4
:-~
I
(~I
ri
:-~
I
I
m
I
1...
~,
~
-
~
ii
r
~y
LflC
tCSt
mctnoas
in the approved ilupiementucion
plan
or 40 CFR Part 60, Appendix A,
incorporated by
reference at Sections 215.105,
210.112,
and 210.112,
as
applicable or by source specific test methods which
have been established pursuant to a permit issued
ri~1~1r,i1~
4~t~s
n~rrt-1
nr promulgated under
•‘,‘-~-~-&fl
(5PP
Prtr+
ci
Title
of
the
Clea..
Air
Act
Subpart
I
or Appendix
0,
incorporated by reference at
Sections 210.112 and 219.112
or under 40 CFR Part

5
52.21,
incorporated by reference at Sections 218. 112
and 219.112.
as ~pplicab1e.
Where such a method also
measures compounas with negligib~.cpnotocnemi~..~.
reactivity,
these negligibly reactive compounds may be
excluded as VON
if
the amount of such compounds
is
accurately quantified, and such exclusions
is approved
by thc Agency.
1
——
c)
As a precondition to axcluding these negligibly
reactive compounds as VON or at any time thereafter,
the Agency may require an owner or operator to provide
monitoring or testing methods and results
mi~ifh,r,
1-,-~ +~h~
satisfnr-f~ir~n
rtf
1-hp
-‘~-~r
amount of negligibly reactive compounds in the
sources’s emissions.
1.~-.~I1
~
~.1
ate determination
to appropriate methods for test~L.,
monitorlziy
negligibly reactive compounds
if such determination is
not reflected in any of the provisions
of paragraph
(Source:
Repealed at
Ill.
Reg.
effective

6
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE B:
AIR POLLUTION
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
C:
EMISSION STANDARDS
AND
LIMITATIONS
FOR STATIONARY SOURCES
PART 211
DEFINITIONS
AND
GENERAL PROVISIONS
SUBPART A:
GENERAL PROVISIONS
Acid Gases
Actual
Heat
Tnr~+-
Adhesive
Aeration
Afterburner
Air
Contaminant
Air
Dried
Coatings
~ir Oxidation Process
~,
ir
Pollutant
~,
ir
Pollution
Air
Pollution Control Eaui~ment
Air Suspension Coater/Dryer
Airless SPray
Air Assisted Airless Spray
Annual Grain Through-Put
Application Area
As Applied
Asphalt
Asphalt Prime Coat
Automobile
Automobile or Light-Duty Truck Assembly Source or
Automobile or Light-Duty Truck Manufacturing Plant
Automobile or Light-Duty Truck Refinishing
Baked Coati~g~
Batch Loading
Bead-Dipping
Binders
British Thermal Unit
Incorporations by Reference
Abbreviations and Units
SUBPART B:
DEFINITIONS
Other Definitions
Definitions
(Repealed)
Accelacota
Accumulator
Section
211.101
211.102
Section
211.121
211.122
211.130
2 11. 150
211.170
211.210
211.230
211. 250
211.
290
211.310
211.
330
211.350
211.370
211.390
211. 410
211.430
211.450
2 11. 470
211.490
211.510
211.530
211.550
211.570
2 11. 590
211.610
211.630
211.650
211.670
211.690
211. 710
211.730
211.750
211.770
Architectural Coating
Brush or Wipe Coating

7
211.790
211.810
211.
830
211.850
211.
870
2 11. 890
211.910
211.930
211.950
211.970
211.990
211.
1010
211. 1050
211.
1090
211. 1110
211. 1130
211.1150
211.
1170
211.
1190
211.
1210
211.
1230
211.1250
211.
1270
211.
1290
211.1310
211.
1330
211.1350
211.1370
211.1390
211.
1410
211.
1430
211.
1470
211. 1490
211.
1510
211.1530
211. 1550
211. 1570
211.1590
211.1610
211.1630
211.
1650
211.
1670
211.
1690
211.1710
211. 1730
211. 1750
211.1770
211.
1790
211.1810
211.1830
211. 1850
211.1870
Bulk Gasoline Plant
Bulk Gasoline Terminal
Can
Can
Coating
Can
Coating
Line
Capture
Capture
Device
Capture Efficiency
Capture System
Certified Investigation
Choke Loading
Clean Air Act
Cleaning and Separating Operation
Clear Coating
Clear Topcoat
Closed Purge System
Closed Vent System
Coal Refuse
Coating
Coating Applicator
Coating Line
Coating Plant
Coil Coating
Coil Coating Line
Cold Cleaning
Complete Combustion
Component
Concrete Curing Compounds
Concentrated Nitric Acid Manufacturing Process
Condensate
Condensible PM—b
Continuous Process
Control Device
Control Device Efficiency
Conventional Soybean Crushing Source
Conveyorized Degreasing
Crude Oil
Crude Oil Gathering
Crushing
Custody Transfer
Cutback Asphalt
Daily-Weighted Average VON Content
Q~y
Degreaser
Delivery Vessel
Dip Coating
Distillate Fuel Oil
Drum
Dry Cleaning Operation or Dry Cleaning Facility
Dump-Pit Area
Effective Grate Area
Effluent Water Separator

8
211.1890
211. 1910
211.1930
211.1950
211.1970
211.1990
211.2010
211.2050
211.2070
211.2090
211.2110
211.2130
211.2150
211.2170
211.2190
211.2210
211.2230
211.2250
211.2270
211. 2310
211.2330
211.2350
211.2370
211.2390
211.2410
211.2430
211.2450
211.2470
211.2490
211.2510
211.2530
211.2550
211.2570
211.2590
211.2650
211.2670
211.2690
211.2710
211.2730
211.2750
211.2770
211.2790
211.2810
211.2830
211.2850
211.2870
211.2890
211.2910
211.2930
211.2950
E1~ctrogtatic
B~11
or
flisc Sorav
spray
Emission Rate
Emission Unit
Enamel
Enclose
End Sealing Compound Coat
Ethanol Blend Gasoline
Excess Air
Excessive Release
Existing Grain-Drying Operation
Existing Grain-Handling Operation
Exterior Base Coat
Exterior End Coat
External Floating Roof
Extreme Performance Coating
Fabric Coating
Fabric Coating Line
Federally Enforceable Limitations and Conditions
Final Repair Coat
Firebox
Fixed-Roof
Tank
Flexographic Printing
Flexographic Printing Line
Floating
Roof
Fountain Solution
Freeboard Height
Fuel Combustion Emission Unit or Fuel Combustion
Emission Source
Fugitive Particulate Matter
Full Operating Flowrate
Gas
Service
Gas/Gas Method
Gasoline
Gasoline Dispensing Operation or Gasoline Dispensing
Facility
Grain
Grain-Drying Operation
Grain-Handling and Conditioning Operation
Grain-Handling Operation
Green-Tire Spraying
Green Tires
Gross Heating Value
Gross Vehicle Weight Rating
Heated Airless Spray
Heatset
Heatset-Web-Offset Lithographic Printing Line
Heavy Liguid
Heavy Metals
Heavy Off-Highway Vehicle Products
Heavy Off-Highway Vehicle Products Coating
Heavy Off-Highway Vehicle Products Coating Line

9
211.2970
211.2990
211.3010
211.3030
211.3050
211.3070
211.3090
211.3110
211.3130
211.3150
211. 3170
211. 3190
211.3210
211.3230
211.3250
211.3270
211.3290
211.3310
211.3330
211.3350
211.3370
211.3390
211.3410
211.3430
211.3450
211.3470
211.3490
211.3510
211.3530
211.3550
211.3570
211.3590
211.3610
211.3630
211.3650
211.3670
211.3690
211.3710
211.3730
211.3750
211.3770
211.3790
211.3810
211.3830
211.3850
211.3870
211.3890
211.3910
211.3930
211 .3970
211.3990
211.4010
High Temperature Aluminum Coating
High Volume Low Pressure
(HVLP) Spray
Hood
Hot
Well
Housekeeping Practices
Incinerator
Indirect Heat Transfer
Ink
In—Process Tank
In-Situ Sampling Systems
Interior Body Spray Coat
Internal-Floating Roof
Internal Transferring Area
Lacquers
Large Appliance
Large Appliance Coating
Large Appliance Coating Line
Light
Liquid
Light-Duty Truck
Light Oil
Liauid/Gas Method
Liquid-Mounted Seal
Liquid
Service
Liquids
Dripping
Lithographic Printing Line
Load-Out
Area
Low Solvent Coating
Magnet Wire
Magnet Wire Coating
Magnet Wire Coating Line
Ma-br Dump Pit
Naior Metropolitan Area
(MMA)
Malor Population Area
(MPA)
Manufacturing Process
Marine Terminal
Material Recovery Section
Maximum Theoretical Emissions
Metal
Furniture
Metal Furniture Coating
Metal Furniture Coating Line
Metallic Shoe-Type Seal
Miscellaneous Fabricated Product Manufacturing Process
Niscel~ri~iicFor~,mi~tion
M
ii
r’+llrina
Process
Miscellaneous Metal Parts and Products
Miscellaneous Metal Parts and Products Coating
Misce
~aneous
Metal Parts or Products Coating Line
Miscellaneous Organic Chemical Manufacturing Process
Mixing Operation
Monitor
Multiple Package Coating
New Grain-Drying Operation
New Grain-Handling Operation

10
211.4030
211.4050
211.4070
211.4090
211.4110
211.4130
211.4150
211.4170
211.4190
211.4210
211.4230
211.4250
211.4270
211.4290
211.4310
211.4330
211.4350
211.4370
211.4390
211.4410
211.4430
211.4450
211.4470
211.4490
211.4510
211.4530
211.4550
211.4590
211.4610
211.4630
211.4650
211.4670
211.4690
211.4710
211.4730
211.4750
211.4770
211.4790
211.4810
211.4870
211.4890
211.4910
211.4930
211.4950
211.4990
211.5030
211.5050
211.5070
No
Detectable
Volatile
Organic
Material Emissions
Non—contact
Process
Water
Cooling
Tower
Offset
One Hundred Percent Acid
One—Turn Storage Space
O~acity
Opaque
Stains
Open
To~ Vapor
Degreasing
Open-Ended
Valve
Operator of a Gasoline Dispensing Operation or Operator
of a Gasoline Dispensing Facility
Organic Compound
Organic Material and Organic Materials
Organic Vapor
Oven
Overall Control
Overvarnish
Owner of a Gasoline Dispensing Operation or Owner of a
Gasoline Dispensing Facility
Owner or Operator
Packaging Rotogravure Printing
Packaging Roto~ravurePrinting Line
Pail
Paint Manufacturing Source or Paint Manufacturing Plant
Paper Coating
Paper Coating Line
Particulate Matter
Parts Per Million
(Volume)
or PPM (Vol)
Person
Petroleum
Petroleum Liquid
Petroleum Refinery
Pharmaceutical
Pharmaceutical Coating Operation
Photochemically Reactive Material
Pigmented Coatings
Plant
Plasticizers
PM- 10
Pneumatic Rubber Tire Manufacture
Polybasic Organic Acid Partial Oxidation Manufacturing
Process
Polystyrene Plant
Polystyrene Resin
Portable Grain-Handling Equipment
Portland Cement Manufacturing Process Emission Source
Portland Cement Process or Portland Cement
Manufacturing Plant
Power Driven Fastener Coating
Pressure Release
Pressure Tank
Prime Coat

11
211.5090
Primer Surfacer Coat
211.5110
Primer Surfacer Operation
211.5130
Primers
211.5150
Printing
211.5170
Printing Li~
211.5185
Process Emission
Source
211.5190
Process Emission Unit
211.5210
Process Unit,
211.5230
Process
Unit Shutdown
211.5250
Process Weight Rate
211.5270
Production Equipment Exhaust System
211.5310
Publication Rotogravure Printing Line
211.5330
Purged Process Fluid
211.5350
Reactor
211.5370
Reasonably Available Control Technology
(RACT)
211.5410
Refiner
211.5430
Refinery Fuel Gas
211.5450
Refinery Fuel Gas System
211.5470
Refinery Unit or Refinery Process Unit
211.5490
Refrigerated Condenser
211.5510
Reid Vapor Pressure
211.5550
Repair Coat
211.5570
Repaired
211.5590
Residual Fuel Oil
211.5610
Restricted Area
211.5630
Retail Outlet
211.5650
Rinqelmann Chart
211.5670
Roadway
211.5690
Roll Coater
211.5710
Roll Coating
211.5730
Roll Printer
211.5750
Roll Printing
211.5770
Rotogravure Printin,g
211.5790
Rotogravure Printing Line
211.5810
Safety Relief Valve
211.5830
Sandblasting
211.5850
Sanding Sealers
211.5870
Screening
211.5890
Sealer
211.5910
Semi—Transparent Stains
211.5930
Sensor
211.5950
Set
of
Safety
Relief Valves
211.5970
Sheet
Basecoat
211.5990
Shotblasting
211.6010
Side—Seam Spray Coat
211.6030
Smoke
211.6050
Smokeless Flare
211.6070
Solvent
211.6090
Solvent Cleaning
211.6130
Source
211.6150
Specialty High Gloss Catalyzed Coating
211.6190
Specialty Soybean Crushing Source

12
211.6210
211.6230
211.6270
211.6290
211.
6310
211.6330
211.6350
211.6370
211.6390
211.
6410
211.6430
211.
6450
211.6470
211.6490
211.6510
211.6530
211.6550
211.6570
211.6590
211.6610
211.6670
211.6690
211.6730
211.6750
211.6770
211.6790
211.6810
211.6850
211.6870
211.6890
211. 6910
211.6930
211. 6950
211.6970
211.6990
211.7010
211.7030
211.7070
211.7090
211.7110
211.7130
211.7150
211.7170
211.7190
211.7210
211.7230
211.7250
211.7270
211.7290
211.7310
Splash Loading
Stack
Standard
Conditions
Standard
Cubic
Foot
(scf)
Start-Up
Stationary Emission Source
Stationary
Emission
Unit
Stationary
Source
Stationary
Storage
Tank
Storage
Tank
or
Storage
Vessel
Styrene
Devolatilizer
Unit
Styrene
Recovery
Unit
Submerged
Loading
Pipe
Substrate
Sulfuric Acid Mist
Surface Condenser
Synthetic Organic Chemical or Polymer Manufacturing
Plant
Tablet Coating Operation
Thirty-Day Rolling Average
Three—Piece Can
Topcoat
Topcoat
Operation
Transfer
Efficiency
Tread End Cementing
True
Vapor
Pressure
Turnaround
Two—Piece Can
Undertread
Cementing
Unregulated Safety Relief Valve
Vacuum Producing System
Vacuum Service
Valves Not Externally Regulated
Vapor Balance System
Vapor Collection System
Vapor Control System
Vapor-Mounted Primary Seal
Vapor Recovery System
Vinyl Coating
Vinyl Coating Line
Volatile Organic Liquid
(VOL)
Volatile Organic Material Content
(VOMC)
Volatile Organic Material
(VON)
or Volatile Organic
Compound
(VOC)
Volatile Petroleum Liquid
Wash Coat
Wastewater
(Oil/Water) Separator
Weak Nitric Acid Manufacturing Process
Web
Wholesale Purchase
Consumer
Wood Furniture
Wood Furniture Coating

13
211.7330
Wood Furniture Coating Line
211.7350
Woodworking
21l.Appendix A
Rule into Section Table
211.Appendix B
Section into Rule Table
AUTHORITY:
Implementing Sections
9,
9.1 and
10 and authorized by
Section 27 and 28.5 of the Environmental Protection Act
(Ill.
Rev.
Stat.
1991,
ch.
111½,
pars.
1009,
1009.1,
1010 and 1027),
(P.A.
87—1213,
effective September 26,
1992)
415
ILCS
5/9,
9.1,
10,
27
and
28.5.
SOURCE:
Adopted
as
Chapter
2:
Air Pollution, Rule 201:
Definitions, R71—23,
4
PCB
191,
filed
and
effective April
14,
1972; amended
in R74-2 and R75-5,
32 PCB 295,
at
3
Ill. Reg.
5,
p.
777, effective February
3,
1979; amended
in R78-3 and 4,
35
PCB
75
and
243,
at
3
Ill.
Reg.
30,
p.
124, effective July 28,
1979;
amended
in
R80-5,
at
7
Ill.
Reg.
1244,
effective January
21,
1983;
codified
at
7
Ill.
Reg.
13590; amended in R82—1
(Docket
A)
at 10 Ill.
Reg.
12624, effective July 7,
1986; amended in
R85—21(A)
at
11 Ill.
Reg.
11747, effective June ?9,
1987;
amended
in R86-34 at
11 Ill.
Reg.
12267, effective July
10,
1987; amended
in R86—39 at
11 Ill.
Reg.
20804, effective December 14,
1987;
amended
in R82—l4 and R86-37 at 12
Ill. Reg.
787,
effective
December 24,
1987; amended in R86-18 at
12
Ill.
Reg. 7284,
effective April
8,
1988; amended in R86—1O at 12
Ill. Reg.
7621,
effective April 11,
1988; amended in R88-23 at
13
Ill. Reg.
10862, effective June 27,
1989; amended in R89—8
at 13
Ill.
Reg.
17457, effective January
1,
1990; amended in R89—16(A)
at 14
Ill.
Reg.
9141,
effective
Nay
23,
1990;
amended
in
R88-30(B)
at
15
Ill.
Reg.
5223,
effective March 28,
1991;
amended in R88—14 at 15
Ill. Reg.
7901,
effective May 14,
1991; amended in R9l—b0 at 15
Ill.
Reg.
15564, effective October 11,
1991; amended in R9l-6 at
15
Ill. Reg.
15673, effective October 14;
1991; amended
in R91—22
at
16 Ill.
Reg.
7656,
effective May
1,
1992; amended
in R9l-24 at
16
Ill.
Reg.
13526, effective August 24,
1992;
amended in R93—
at
17
Ill.
Reg.
______,
effective ___________________________
Section
211.102
Abbreviations and Units
a)
Abbreviations
used
in
this
Part
include the following:
ASTM
American Society for Testing and
Materials
barrels
(42 gallons)
btu
British thermal units
(60°F)
degrees Celsius or centigrade
cm
centimeters
cu in
cubic inches
°F
degrees Fahrenheit
FIP
Federal Implementation Plan

14
ft
feet
ft2
square
feet
g
grams
gallons per minute
g/mole
grams
per
mole
gallons
hours
in
inch
degrees
Kelvin
kcal
kibocabories
kg
kilograms
kg/hr
kilograms per hour
kPa
kilopascals;
one
thousand newtons per
square meter
liters
1/sec
liters per second
lbs
pounds
lbs/hr
pounds
per
hour
lbs/gal
pounds per gallon
lower explosive limit
in
meters
m2
square
meters
m3
cubic meters
milligrams
Meqagrams, metric tons or tonnes
milliliters
minutes
MJ
megaloules
mmHg
millimeters
of
mercury
natural
draft
opening
ppm
(vol)
parts per million
ppmv
parts per million by volume
psi
pounds
per
square
inch
psia
pounds
per
square
inch
absolute
psig
pounds per square inch gauge
RACT
reasonably available control technology
scf
standard cubic feet
standard cubic meters
sec
seconds
SIP
State Implementation Plan
TTE
temporary total enclosure
sq
cm
square centimeters
sq
in
square
inches
T
short
ton
(2.000
lbs)
short ton
(2,000
bbs)
USEPA
United States Environmental Protection
Agency
VOC
volatile organic compounds
volatile organic liquids
VON
volatile organic materials

15
b)
The
following
conversion
factors are used in this Part.
English
1
gal
1,000
gal
1
psia
2.205
lbs
320
1
bbl
1
cu
in
1 lb/gal
1
ton
iT
Metric
3.785
1
3,785
1
or
3.785
m3
6.897
kPa
(51.71
mmHg)
1
kg
0°C
(273.15°
K)
159.0
1
16.39
ml
119,800
m~/l
0.907
Mg
0.907
Mg
(Source:
Amended
at
Ill.
Reg.
______,
effective
SUBPART
B:
DEFINITIONS
Section 211.121
Other Definitions
All terms defined in 35
Ill. Adm.
Code 201 which appear in 35
Ill.
Adm. Code 211
-
217 through 219 have the definitions
specified by 35
Ill. Adm.
Code
201.102.
Otherwise
the
definitions in Section 211.122 this Part shall apply.
(Source:
Amended at
Ill.
Reg.
______,
effective
________
Section 211.122
Definitions
(Repealed)
“Accelacota”:
consists of a
a pharmaceutical coating
horizontally rotating per
operation which
forated drum in
which tablets arc placed,
a coating
..s applicd by
spraying and the coating is dried by the flow of air
ro~
thc~ cirum
through th~
nerforntion~
of a condensing unit
receiving the condensate from a surface condenser.
“Acid Cases”:
For the purposes of Section 9.4 of the
Environmental Protection Act (the Act)
(Ill.
Rev.
Stat.
1987,
oh.
111½,
par.
1009.4), hydrogen chloride,
hydrogen fluoride and hydrogen bromide, which exist as
gases,
liquid
mist,
or any combination thereof.
“Actual Heat Input”:
The quantity of heat produced by
the combustion of fuel using the gross heating value of
the fuel.
The reservoir

16
“Aeration”:
The practice of forcing air through bulk
stored grain to maintain the condition of the grain.
“Afterburner”:
A device in which materials in gaseous
effluents arc combustcd.
“Air Dried Coating”:
Coatings that dry by the use of
air or forced air at
temperatures
up to 363.15° 1
(194°
~)-~
“Air suspension coater/dryor”:
a pharmaceutical
coating operation which consists of vertical chambers
in which tablets or particles are placed, and a coating
is applied and then dried while the tablets or
particles
arc
kept
in
a fluidizcd state by the passage
of
air
upward
through
the
chambers.
“Annual
Grain Through-Put”:
Unless otherwise shown by
the owner or operator, annual grain through-put for
grain-handling
operations,
which
have
been
in
operation
for
three
consecutive
years
prior
to
June
30,
1975,
shall
be
determined
by
adding
grain
receipts
and
shipmcnts
for
the
three
previous
fiscal
years
and
dividing
the
total
by
6.
The
annual
grain
through-put
for
grain
handling
operations
in
operation
for
less
than
three
consecutive
years
prior
to
June
30,
1975,
shall
be
determined
by
a
reasonable
three-year
estimate;
the
owner
or
operator
shall
document
the
rcasonablencss of his three—year estimate.
“Architectural Coating”:
Any coating used for
residential or commercial buildings or their
appurtenances,
or for industrial buildings which
is
site applied.
“Asphalt”:
The dark-brown to black ccmcntitious
material
(solid,
semisolid or liquid in consistency)
of
which the main constituents arc bitumcns which occur
naturally or as a residue of petroleum refining.
“Asphalt Prime Coat”:
A low-viscosity liquid asphalt
applied to an absorbent surface as the first of more
than one asphalt coat.
“Automobile”:
Any first division motor vehicle as
that
term is defined in the Illinois Vehicle Code
(Ill.
Re-v.
Stat.
1987,
ch.
95½, pars
1-100
et seq.).
“Automobile
or
Light-Duty Truck Manufacturing Plant”:
A facility where parts
are
manufactured or finished
fe-r
eventual
inclusion
into
a
finished
automobile
or
light-duty truck ready for sale to vehicle dealers,
but

17
ot including
~e~aintcr~
_1,a—..4.~__,..
In
I
—J
“Automobile or Light Duty Truck Refinishing”:
The
repainting
of
used
automobiles
or
light
duty
trucks.
“Batch
Loading”:
The
process
of
loading
a
number
of
individual
parts
at
the
same time for dcgrcasing.
“Bead-Dipping”:
The
dipping
of
an
assembled
tire
head
into a solvent-based cement.
“British
Thermal
Unit”:
The
quantity
of
heat
required
to
r~i~r on~ nound
of
~at~r
from
60°
F
to
61°
F
(abbrcviatcd
btu).
“Bulk Gasoline Plant”:
Any gasoline storage and
distribution facility that receives gasoline from bulk
gasoline terminals by delivery vessels and distributes
gasoline to gasoline dispensing facilities.
“Bulk Casolinc Terminal”:
Any gasoline storage and
distribution facility that receives gasoline by
pipeline,
ship or barge, and distributes gasoline to
bulk gastdine plants or gasoline dispensing facilities.
“Can Coating”:
The application of a coating material
to a single walled container that is manufactured from
metal sheets thinner than 29 gauge
(0.0141
in).
11-Certified Investigation”:
A report signed by Illinois
Environmental Protection Agency
(Agency) personnel
certifying whether
a grain-handling operation
(or
portion
thereof)
or grain-drying operation is causing
or
tending
to
cause
air
pollution.
Such report must
describe the signatory’s investigation,
including a
summary
of
those
facts
on
which
he
relics
to
certify
whether the grain-handling or grain-drying operation is
causing
or
threatening or allowing the discharge or
emission
of
any contaminant
into
the
environment
so
as
to
cause
or
tend
to
cause
air
pollution
in
Illinois,
either alone or in combination with contaminants from
other sources,
or so as to violate regulations or
standards adopted by the Pollution Control Board
-(Board) under the Environmental Protection Act
(Act).
The certified investigation shall be open to a
reasonable public inspection and may be copied upon
payment of the actual cost of reproducing the original.
“Choke
Loading”:
That method of transferring grain
from
thr
rcr-, i n—hr,r,rll
inn
r~nr’r-iti
on
to
~1
~
for
....~pmentor dclivcry which precludes a free fall

18
~
a aiscnarn~
~*rIirnit
into
the
receiving container.
“Cleaning and Separating Operation”:
That operation
where
foreign
and
undesired
substances
are
removed
from
the grain.
“Clear
Coating”:
Coatings
that
lack
color
and
opacity
or
arc
transparent
using
the
undercoat
as
a
ref lectant
base
or
undertone
color.
“Closed
Purge
System”:
A
system
that
is
not
open
to
the atmosphere and that is composed of piping,
connections,
and,
if
necessary,
flow
inducing
devices
that
transport
liquid
or
vapor
from
a
piece
or
pieces
of equipment to a control device,
or return the liquid
or
vapor
to
the
process
line.
“Closed Vent System”:
A system
that
is
not
open
to
the
atmosphere
and
that
is
composed
of
piping,
connections,
and,
if necessary,
flow inducing devices that transport
gas or vapor from a piece or pieces of equipment to a
control device,
or return the gas or vapor to the
process line.
“Coal Refuse”:
Waste products of coal mining, cleaning
and coal preparation operations containing coal, matrix
material, clay and other organic and inorganic
material.
“Coating”:
For purposes of this Part,
a coating
includes a material applied to a substrate for
decorative,
protective or other functional purposes.
Such material shall include, but
are
not
limited
to
paints, varnishes,
scalers,
adhesives, diluents and
thinners.
“Coating Applicator”:
Equipment used to apply a
surface coating.
“Coating Line”:
An operation where a surface coating
is applied to a material and subsequently the coating
is dried and/or cured.
“Coating Plant”:
Any building, structure or
installation that contains a coating line and which
is
located on one or more contiguous or adjacent
properties and which is owned or operated by the same
person
(or by persons under common control).

19
container.
“Coil Coating”:
The application of a coating material
to any flat metal sheet or
strip
that comes
in rolls or
coils.
“Cold
Cleaning”:
The
process
of
cleaning
and
removing
soils
from
surfaces
by
spraying,
brushing, flushing or
immersion while maintaining the organic solvent below
its
boiling
point.
Wipe
cleaning
is
not
included
in
this definition.
“Complete
Combustion”:
A
process
in
which
all
carbon
contained in a fuel or gas stream
is converted to
carbon
dioxide.
“Component”:
Any piece of equipment
which
has
the
potential to leak volatile organic material including,
but not limited to, pump seals,
compressor seals, seal
oil
degassing
vents,
pipeline
valves,
pressure
relief
devices,
process
drains
and
open
ended
valves.
This
definition
excludes
valves
which
arc
not
externally
regulated,
flanges,
and
equipment
in
heavy
liquid
service.
For
purposes
of
35
Ill.
Adm.
Code
215.
Subpart
Q,
this definition also excludes bleed ports of
gear
pumps
in
polymer
service.
“Concentrated
Nitric
Acid
Manufacturing
Process”:
Any
acid
producing
facility
manufacturing
nitric
acid
with
a
concentration
equal
to
or
greater
than
70
percent
by
weight.
“Condensate”:
Hydrocarbon liquid separated from its
n~ociatcd
gasses which condcns~
tcmocr~”--’
due
tc
~
~n
the
~
~..8
~~ins
liquid
at
standard
cnanci-’
eUIlui
L1Ufl~J
“Condensibic PM-b”:
PM-b
formed immediately or
shortly after discharge to the atmosphere,
as
measured
by the applicable test method specified in
35
Ill. Adm.
Code 212.110.
Condensible particulate matter exists
in
gaseous
and/or
vapor
form
prior
to
release to the
atmosphere,
e.g.,
in
the
stack,
and
forms
particulate
matter
upon
condensation
when
subject
to
conditions
of
cooling and dilution in the atmosphere.
“Control Device”:
Equipment,
such as an afterburner,
adsorber, scrubber, condenser,
cyclone or baghouse used
to
remove
or
prevent
the
emission
of
air pollutants
from
a
contaminated
exhaust
stream.
For
purposes
of
35
Ill.
Adin.
Code
215,
Subpart
Q,
an enclosed combustion
vanor
recovery
system,
flare,
or
closed

20
“Conveyoriccd
Degrcasina”!
Thr’
rr~ntinuous
~roocss
of
1_~_~•_4
--
C
~
~ftd
a.
s...aus., .
a_a,’~
5ø”ia...s
4.L.
5.~~tt
a.~4...s...a
utilizin~
either
cold
or
vaporized
solvents.
-
~
.-...-....c—-.
tura
lly
consists
of
hydrocarbons
and
sulfur,
nitrogen
or
oxygen
derivatives
of
hydrocarbons
and
which
is
a
liquid
at
standard conditions.
“Crude
Oil
Cathering”:
The transportation of crude oil
or condensate after custody transfer between a
production facility and
a reception point.
“Crushing”:
The fragmentation of non—metallic mineral-s
by a machine such as a jaw,
gyratory,
cone,
roll,
rod,
mill, hammermill,
and impactor.
“Custody Transfer”:
The transfer of produced petroleum
and/or condensate after processing and/or treating
in
the producing operations,
from storage tanks or
automatic
transfer
facilities
to
pipelines
or
any
other
forms of transportation.
“Cutback Asphalt”:
Any asphalt which has been
liquified by blending with petroleum solvents other
than
residual
fuel
oil
and
has
not
been emulsified with
water.
“Dcgreaser”:
Any
equipment
or
system
used
in
solvent
cleaning.
“Delivery
~1L~
-A..2 tank truck
trail._a. ~
with
a
storage
tank
that
is
used
for
the
transport
of
gasoline
to
a stationary storage tank at a
gasoline
dispensing facility, bulk gasoline plant or bulk
gasoline terminal.
“Distillate Fuel Oil”:
Fuel oils of grade No.
1 or
2
as specified in detailed requirements for fuel oil
A.C.T.N.
D—369—69
(1971).
“Dry Cleaning Facility”:
A facility engaged in the
cleaning
of
fabrics
using
an
essentially
nonaqueous
solvent
by
means
of
one
or
more
solvent
washes,
extraction
of
excess
solvent
by
spinning
and
drying
by
tumbling
in
an
airstream.
The facility includes,
but
4-s
not
limited
to,
washers,
dryers,
filter
and
purification
systems,
waste
disposal
systems,
holding
tanks,
pumps
and
attendant
piping
and
valves.
“Dump-Pit Area”:
Any area where grain is received at a
grain-handling or grain-drying operation.

21
“Effective Crate Area”:
That
through which air passes,
or
aspirated.
area of a dump—pit
would pass, when
grate
“Effluent Water Ceparator”t
Any
tank,
box,
ciump or
other apparatus in which any organic material floating
entra.a.ned or containca
...u
water
cnterluy
L.uuh
sumn or othor rinnnratur i~
rh:~ior~11v
parui~u
and
removed
from
3uch
water
prior
to
outfall,
drainage or recovery of such water.
“Emission
Rate”:
Total
quantity of any air contaminant
discharge
into
the
atmosphere
in
any
one—hour period.
“Enclose”:
With
respect
to
35 Ill.
Adm.
Code 215
Subpart
T,
to
cover
any
volatile
organic
liquid
surface
that is
exposed to the atmosphere.
“End
Scaling
Compound Coat”:
A compound applied to can
ends which functions as a gasket when the
end is
assembled on the can.
“Excess Air”~ Air supplied in addition to the
theoretical quantity necessary for complete combustion
~f r~~1
1
fu~~1 r~nri’r,r
t-~r,mh11~-It-ih1r-~
-i’-*tr~ m~tr~ri~I1
~~~~1
“Excessive
flcleasc”i
A
discharge
of
more
than
295g
(0.65
pounds)
of
mercaptans
or
hydrogen
sulfide
into
the atmosphere
in any five minute period.
“Existing Cram-Drying Opcration”z
Any grain-drying
operation the construction or modification of which was
commenced prior to June 30,
1975.
“Existing Grain-Handling Operation”:
Any
grain-handling operation the construction or
modification of which was commenced prior to June 30,
1975.
“Exterior
Base
Coat”:
An
initial
coating
applied
the exterior of a can
after
the
can
body
has
been
to
formed.
“Exterior End Coat”:
A coating applied by rollers or
spraying to the exterior end of a can.
0
rl_
L
.1
Floating
single
deck
which
is
supported
by the pctrol~um liquid
hr~ina
c~nnt~iinr~d
-,rd
ir~
rn
ir~nrd~~ith ~ ci1o~ure~eri~1
-:1
—~-
~:-
4-~~-~l,-~
1

22
“Extreme
Performance
Coating”:
Coatings designed for
exposure
to
any
of
the
following:
the
ambient
weather
conditions,
temperatures
above
368.15°
K
(203°
F),
detergents,
abrasive
and
scouring
agents,
solvents,
corrosive atmospheres, or other similar extreme
environmental conditions.
“Fabric
Coating”:
The coating of a textile substrate,
including operations where the coating impregnates the
substrat-e-.
“Final
Repair
Coat”:
The
repainting
of
any
coating
which
is
damaged
during
vehicle
assembly.
“Firebox”:
The chamber or compartment of a boiler or
furnace in which materials arc burned,
but not the
combustion chamber or afterburner of an incinerator.
“Flexographic Printing”:
The application of words,
designs and pictures to a substrate by means of a roll
printing technique in which the pattern to be applied
is raised above tho printing roll and the image carrier
is made of elastomeric materials.
“Floating Roof”:
A roof on a stationary tank,
reservoir or other container which moves vertically
u-p~on
change in volume of the stored material.
“Freeboard Height”:
For open top vapor degreascro,
the
distance from the top of the vapor zone to the top of
the degreaser tank.
For cold cleaning degreaciers, the
distance from the solvent to the top of the degreaser
tank.
“Fur-i
Combuciti~
~imi1~a. ~~ipmcnt
used for th~primary ~
nroduri
nn
hr~t
or
nntrrr
by
I
nd
I rrot
hr~t
tr~n~frr
-
--
~—~“:
Any furnace, boil~
-
212 othcrwi~ ~~licable
~~ly
becau~
of
a
stack.
“Fuel
Gas
System”:
A
system
for collection of refinc~-y
fuel
gas including,
but not limited to, piping for
collecting tail gas from various process units,
mixing
drums and controls and distribution piping.
“Fugitive Particulate Matter”:
Any particulate matter
emitted into the atmosphere other than through a stack,
provided that nothing in this definition or in 35
Ill.
Adin.
Code 212.Cubpart K
shall
exempt any source from
compliance
trith
M-hr--~-
r~ir,n~
of
~
Ti1
~dm
C~r~dr-
r’-F
fhr-
absence

Means
that
the
component
cont~..ii~
process
fluid
that
is
in
the
gaseous
state
at
operating
conditions.
“Gasoline”:
Any petroleum distillate having a Reid
vapor pressure of
4 pounds or greater.
“Gasoline
Dispensing
Facility”:
Any
site
where
g-asoline
is
transferred
from
a
stationary
storage
tank
to a motor vehicle gasoline tank used to provide fuel
to the engine of that motor vehicle.
“Grain”:
The whole kernel or seed of corn, wheat,
oats,
soybeans and any other cereal or oil seed plant;
and the normal fines, dust and foreign matter which
results from harvesting, handling or conditioning.
The
grain shall be unaltered by grinding or processing.
“Cram-Drying Operation”:
Any
operation,
excluding
aeration, by which moisture
is
removed from grain and
which typically uses forced ventilation with the
addition of heat.
r~-
“Cram-Handling
Operation”:
Any
operation
where
one
or
more of the following grain-related processes (other
than grain-drying operation, portable grain-handling
equipment, one-turn storage space,
and
excluding
flour
mills
and
feed
mills)
are performed:
receiving,
shipping,
transferring, storing, mixing or treating of
or
other
processes
pursuant
to
normal
grain
operations.
“Green Tire Spraying”:
The spraying of
green
tires,
both
inside
and
outside,
with release compounds which
help
remove
air
from
the
tire
during molding and
prevent
the
tire
from
sticking
to
the
mold
after
curing.
“Green
Tires”:
Assembled
tires
before
molding
and
curing have occurred.
“Cross Heating Value”:
Amount of heat produced when a
unit quantity of fuel
is burned to carbon dioxide -and
water
vapor,
and
the
water
vapor
condensed
as
described
in
A.S.T.M.
D—2015—66,
D—900-55, D—1826—64 and
D—240—64.
-
c._~-_-..-~
~
23
“Crain-Handli, and Condition.~.~.~a..~..on”:
A
..,~d-..
storage facility and its associate grain transfer,
cleaning, drying, grinding and mixing operations

24
“Heavy Liquid”:
Liquid with a true vapor pressure of
less than 0.3
kPa (0.04 psi)
at
294.30
K (70°F)
or 0.1
Reid Vapor Pressure as determined by A.C.T.M. method
D-323; or which when distilled requires a temperature
of
3000
F or greater to recover 10
of the liquid as
determined by A.S.T.M. method D-86.
“Heavy Metals”:
For the purposes of Section 9.4 of the
Act, elemental,
ionic,
or combined forms of arsenic,
cadmium, mercury,
chromium, nickel and lead.
“Heavy, Off-Highway Vehicle Products”:
For the
purposes of Section 215.204(k), heavy off-highway
vehicle products shall include:
heavy construction,
mining,
farming or material handling equipment; heavy
industrial engines; diesel-electric locomotives and
associated power generation equipment; and the
components of such equipment or engines.
“Hot Well”:
The reservoir
of a condensing unit
receiving the
condensate from a barometric condenser.
“Housekeeping Practices”:
Those activities
specifically defined in the list of housekeeping
practices developed by the Joint EPA
-
Industry Task
Force and included herein under 35 Ill.
Adm.
Code
212.461.
“Incinerator”:
Combustion apparatus in which refuse is
burned.
“Indirect Heat Transfer”:
Transfer of heat in such a
way that the source of heat does not come into direct
contact with process materials.
“In-Process Tank”:
A container used for mixing,
blending,
heating, reacting,
holding, crystallizing,
evaporating,
or cleaning operations in the manufacture
of pharmaceuticals.
“In-situ Sampling Systems”:
Nonextractive samplers or
in—line samplers.
“Interior Body Spray Coat”:
A coating applied by spray
to the interior of a can after the can body has been
formed.
“Internal Transferring Area”:
Areas and associated
equipment used for conveying grain among the various
ar~in
onrr~tionr~_

25
“Large Appliance Coating”:
The application of a
coating material to
(including but not
the component metal parts
limited to doors,
cases,
lids,
pancis ana interior support parts~ ot rcciuentiai and
commercial washers, dryers, ranges, refrigerators,
freezers, water heaters, dishwashers, trash compactors,
air conditioners and other similar products.
“Light-Duty Truck”:
Any
second division motor vehicle,
as that term is defined in the Illinois Vehicle Code,
(Ill.
Rev. Stat.
1989,
oh.
95½, pars.
1-100 et seq.)
weighing loss than 3854 kilograms
(8500 pounds)
gross.
“Liquid—Mounted Seal”:
A primary seal mounted in
continuous contact with the liquid between the tank
wall and the floating roof edge around the
circumference of the roof.
“Liquid Service”:
Means that the equipment or component
contains process fluid that is in a liquid state at
operating conditions.
“Liquids Dripping”:
Any visible leaking from a seal
-
including spraying, misting, clouding and icc
formation.
H~pp~_p~~
Aa.
a~.
~AfI~’
......
....~-a.
ja.
a.
from the grain-handling operation
or delivery.
to any vehicle for
shipment
“Low Solvent Coating”:
A ceating which contains less
ULyuIliu
uulvent than the convent.w~iuicoatings used by
the industry.
Low solvent coatings include
water-borne, higher solids, electro-deposition and
powder coat
ing-9-o-
“Magnet Wire Coating”:
The application of a coating of
electrically insulating varnish or enamel to conducting
wire to be used in electrical machinery.
“Major Dump Pit”:
Any dump pit with an annual grain
through-put of more than 300,000 bushels,
or which
receives more than 40
of
the annual grain through-put
of the grain-handling operation.
“Major Metropolitan Area
(MMA)”:
Any county or group
of counties which is defined by the following Table:
MAJOR METROPOLITAN
AREAS
IN ILLINOIS (~1A’s)
MMA
COUNTIES INCLUDED IN ~A

26
Champaign-Urbana
~uuu
Cook,
Lake,
Will,
DuPagc,
McHenry, Kane,
Grundy,
Kcndzill, Kankakee
Peoria
Peoria, Tazcwcll
Rockford
Winnebago
Rock Island
--
Nolinc
Rock Island
Springfield
Cangamon
St. Louis
(Illinois)
Ct. Clair, Madison
Bloomington
--
Normal
McLean
“Major Population Area
(NPA)”:
Areas of major population
concentration in Illinois,
as descria.~.~......ow:
The area within the counties of Cook; Lake; Durage;
Will;
the townships of Burton,
Richmond, McHenry,
Crccnwood,
Nunda,
Door, Algonquin,
Grafton and the municipality
of.
Woodstook, plus
a zone
extending two miles beyond the
boundary of said municipality located in McHenry County;
the townships of Dundee, Rutland,
Elgin, Plato,
St.
Charles,
Campton, Ccncva, Blackberry, Batavia,
Sugar
Creek and Aurora located in Kane County; and the
municipalities of Kankakec, Bradley and Bourbonnais, plus
a zone extending two miles beyond the boundaries of said
municipalities in Kankakec County.
The area within the municipalities of Rookford and Loves
Park, plus a zone extending two miles beyond the
boundaries of said municipalities.
The area within the municipalities of Rock Island,
Molinc, East Moline, Carbon Cliff, Milan,
Oak Grove,
Cilvis,
Hampton, Greenwood and Coal Valley, plus a zone
extending two miles beyond the boundaries
of said
municipalities.
The area within the municipalities of Galesburg and East
Calcsburg, plus a zone extending two miles beyond the
boundaries of said municipalities.
The area within the municipalities of Bartonville, Peoria
and Peoria Heights, plus a cone oxtending two miles
beyond the boundaries of said municipalities.
Thr
iirr-~
uithin
1-hr
mI1r~i
cipalitics of Pekin,
North
PrkIn~
Marquette Heights,
Creve
~
reoria,
pluc3a
cone extending two miles beyond the boundaries of said
municipalities.

27
iithin the municipalities of Bloomington and
~
L_us
n
~nnr
r-~ctrndini
two miles beyond the
boundaries ot saia
mllnlr-lrln,lties.
The area within the municipalities of Champaign,
Urbana
and Cavoy, plus a zone extending two miles beyond the
boundaries of said municipalities.
The area within the municipalities of Decatur, Mt.
Zion,
Harristown and Forsyth, plus a zone extending two miles
beyond the boundaries of said municipalities.
The area within the municipalities of Springfield,
Lelarid
Crove, Jerome, Southern View, Crandview,
Sherman and
Chatham, plus a zone extending two miles beyond the
boundaries of said municipalities.
The area within the townships of Godfrey,
Foster, Wood
River, Fort Russell,
Choutcau, Edwardoville, Venice,
Nanieoki, Alton, Granite City and Collinsville located in
Madison County; and the townships of Ctites,
Canteen,
Centreville, Caseyville,
St. Clair,
Sugar Loaf and
Stookey located in St. Clair County.
“Manufacturing Process”:
A process emission source or
series of process emission sources used to convert raw
materials,
feed stocks, subasoemblies or other components
into a product,
either for sale or for use as a component in
a subsequent manufacturing process.
“Marine Terminal”:
A facility primarily engaged in loading
and unloading watercraft.
“Metal Furniture Coating”:
The application of a coating
material to any furniture piece made of metal or any metal
part which is or will be assembled with other metal, wood,
fabric, plastic or glass parts to form a furniture piece
including, but not limited to, tables,
chairs, wastebaskets,
beds, desks,
lockers, benches, shelving,
file cabinets,
lamps and room dividers.
This definition shall not apply to
any coating line coating metal parts or products that is
identified under the Standard Industrial Classification Code
for Major Groups 33,
34,
35,
36,
37,
38,
39,
40 or 41.
“Miscellaneous Fabricated Product Manufacturing Process”:
A manufacturing process involving one or more of the
following applications,
including any drying and curing
of formulations,
and capable of emitting volatile organic
material:

28
Adhesives to fabricate or a
components or products
Asphalt solutions to paper
Asphalt to paper or felt
Coatings or dye to leather
Coatings to plastic
Coatings to rubber or glass
Curing of furniture adhi
in excess of 10 tons of
y..~rif
...~
air pollutioi.
Diciinfcc~”~~
nragc
pr~~
rIr-r-1!~
dccicr
E~
UL~L
ft~
___
hand1....~,
_________
-
and handli
cci for do
described above.
“Mi~uei~uiieuu~
Formulation Manufacturing Process”;
A manufacturing process which compounds one or more ef
the following and
is capable of emitting
volatile
organic material:
Adhesives
Asphalt solutions
inn
r,f
formu1~-~tion~-*
associated
~.jith
.~.
..bovc.
liquids and other
rig of
organic
an—up
operatinn~
.~1n
I~itr-d
yith
1-hi-’
1
-
contrc
.~
in an oven which would emit
latilc organic material per
~
cquipmei.
.~-—
—.-.—-——--—
-~
.—
——
i—iaocio
ioaln
~crup
or
“fluff” from the manufacture
of
foam containers and
pellets
packaging material to form
recii-n
Resin solutions to fiber substances
Rubber solutions to molds
Viscose solutions for food casings
The
-ø~
t~ -p~
ciubsta
proce-~
t.auix~, ~caianc~ or waterproofing agents
Coatings,
other than paint and ink
Concrete curing compounds

Dyes
Fricti
iais and
29
Resin solutions
Rubber solutions
Viscose solutions
The
cit
~-
I..
age and handling
The use and handling of organic liquids and other
substances for clean-up operations associated with the
“Miscellaneous Metal Parts and Products”:
For the purpose
of 35 Ill. Adm. Code 215.204, miscellaneous metal parts and
products shall include farm machinery,
garden machinery,
small appliances,
commercial machinery,
industrial
machinery,
fabricated metal products and any other
industrial category which coats metal parts
or products
under the Standard Industrial Classification Code for Major
Croups
33,
34,
35,
36,
37,
38 or 39 with the exception of
the following:
coating lines subject to 35 Iii. Adm. Code
~‘i5.2O4(a)-(i)and
(k)
~utomohiir
or
light-duty trur*
refinishing, the exterior of marine vessels and the
customized top coating of automobiles and trucks
if
production is less than thirty-five vehicles per day.
“Miscellaneous Organic Chemical Manufa
i~
manuiacturing process
‘Wnu’.u
yLUUU
reaction, one or more of the following organic compounds
or mixtures of organic compounds and which
is capable of
Chemicals listed
in
35 Ill. Adm.
Code 215. Appendix D.
Chlorinated and
detergent,
soap
surfactant intermedi
Disinfcctants
F~ru-9 ~r1ditiyr~i
additi
,
2
~.a
2
emittL.~
2
~L.
_
——
- -
-
2
I
organi~
~
Oil and petroleum pr

30
Plasticizers
flesins or polymers
Rubber aau
Sweeteners
Varnishes
The storage and handling
4
t-~
l-.-.~
The use and handling
of organic liquids and other
oubotances for clean-up operations associated with the
“Mixing Operation”:
The operation of combining two or more
ingredients, of which at least one
is a grain.
“New Grain-Drying Operation”z
Any grain-drying operation
the construction or modification of which is
op
mmenced on or
June 30,
1975.
n_~.
2
tt_
.~
I
2
-
--
1
——
.s_t.
s____s.1_
handliny
I
“No Detectable Volatile Organic Material
Emissions”:
A
discharge
UL
vuiuciie
uryanju
macor
im_u
atmosphere
as indicated by
above background
an
as
instrument
determined
reading of less than
in accordance with
500 ppm
40 CFR
60.485(c).
4-I-.
-.
-‘
a.
~~a~cns,
the
~
and Ringelmann shall be employed:
Opacity
“One Hundred Percent Acid”:
Acid with a specific gravity of
1.3205 at 30°C in the case of sulfuric acid and 1.4952 at
30°C in the case of nitric acid.
“One-Turn Storage Space”:
That space used to store grain
with a total annual through-put not in excess of the total
bushel storage of that spacb.
“Opacity”:
A condition which renders material partially or
wholly impervious to transmittance of light and causes
obstruction of an observer’s view.
For the purposes of
41~...-....
hr’1-tyr-,-n
opacity
0.5
Ringclmann
—It’
1.
SU
1c

A(I
1
t¼~
‘..
60
3.
80
4.
31
“Open Top Vapor Degreasirig”:
The batch process of cleaning
and
removing
soils
from
surfaces
by
condensing
hot
solvent
vapor on the colder metal parts.
“Operator of Gasoline Dispensing Facility”:
Any person who
is the lessee of or operates, controls or supervises a
gasoline dispensing facility.
“Organic Compound”:
Any compound of carbon,
excluding
carbon monoxide, carbon dioxide, carbonic acid,
metal
carbides or carbonates,
and aminonium carbonate.
“Organic Material”:
Any chemical compound of carbon
including diluents and thinners which are liquids at
standard conditions and which are used as dissolvers,
viscosity reducers or cleaning agents, but excluding
methane, carbon monoxide, carbon dioxide, carbonic acid,
metallic carbonic acid, metallic carbide, metallic
carbonates and ammonium carbonate.
“Organic Materials”:
For the purposes of Section 9.4 of the
Act, any chemical compound of carbon,
including diluents and
thinners which are liquids at standard conditions and which
are used as dissolvers, viscosity reducers or cleaning
agents, and polychiorinatod dibcnzo-p-dioxins,
polyohlorinated dibencofurans and polynucloar aromatic
hydrocarbons are organic materials, while methane,
carbon
monoxide, carbon dioxide, carbonic acid, metallic carbonic
acid, metallic carbide, metallic carbonates and amxnoniun
carbonate are not organic materials.
“Organic Vapor”:
Gaseous phase of an organic material or a
mixture of organic materials present
in the atmosphere.
“Ovcrvarnish”:
A coating applied directly over ink or
printing.
L~
-11Owner
of
Gasoli.....
~
Facility”.
-~egalorequitable title toa
~
tank at a
ya~uJ.ine ui~penuiny
iuuiiit.y.
“Packaging Rotogravure Printing”:
Rotogravure printing upon
paper, paper board, metal
foil,. plastic film and other
substrates,
which are,
in subsequent operations,
formed into
packaging products or labels for articles to be
sold.
who has

32
“Paint Manufacturing Plant”:
A plant that mixes,
blends,
or
compounds enamels,
lacquers, scalers,
shellacs,
stains,
varnishes or pigmented surface coatings.
“Paper Coating”:
The application of a coating material to
paper or pressure sensitive tapes,
regardless of substrate,
including web coating on plastic fibers and decorative
coatings on metal foil.
“Particulate Matter”:
Any solid or liquid material,
other
than water, which exists in finely divided form.
“Petroleum Liquid”:
Crude oil, condensate or any finished
or intermediate product manufactured at a petroleum
refinery, but not including Number
2 through Number
6 fuel
oils
as specified in A.C.T.M. D-396-69,gas turbine fuel oils
Numbers 2-CT through 4 CT as specified in A.S.T.N. D-2880-71
or diesel fuel oils Numbers 2-D and 4-D,
as specified in
A.S.T.M.
D—975-68.
“Petroleum Refinery”:
Any facility engaged in producing
gasoline, kerosene, distillate fuel oils, residual fuel
oils,
lubricants, or other products through distillation,
cracking, extraction or reforming of unfinished petroleum
derivatives.
“Pharmaceutical”:
Any compound or mixture,
other than food,
used in the prevention, diagnosis,
alleviation, treatment or
cure of disease in man and animal.
“Pharmaceutical Coating Operation”:
A device in which a
coating is applied to a pharmaceutical,
including any drying
or curing of the coating.
“Photochemically Reactive Material”:
Any
organic material
with an aggregate of more than 20 percent of its total
volume composed of the chemical compounds classified below
or the composition of which exceeds any of the following
individual percentage composition limitations.
Whenever any
photochemically reactive material or any constituent of any
organic material may be classified from its chemical
structure into more than one of the above groups of organic
materials it shall be considered as a mcm~eror tnc most
reactive group,
that is,
the group having the least
allowable percent of the total organic materials.
A combination of hydrocarbons, alcohols,
aldehydes,
esters,
ethers
or ketones
having an olofinic or
cyclo-olefinic
types
of
unsaturation:
5
percent.
This
definition does not apply to perchlorcthylene or
1-TI
rthi
nrpet~~i
r-nr’
-
-L

33
A combination of aromati
——
1_
_
——
A_t
tEl-Il
.t4-tI
l~1
1
~
compounds with eight
belong to the came inductrial grouping, are located on one
or more contiguous or adjacent properties,
and are under the
control of the same person
(or persons under common
control), except the activities of any marine vessel.
Pollutant-emitting activities shall be considered as part of
the same industrial grouping if they belong to the same
major group
(i.e., which have the same two-digit code)
-as
described
in
the “Standard Industrial Classification
Manual”,
1987.
“PH—b”:
particulate matter with an aerodynamic diameter
less than or equal to a nominal 10 micrometers,
as measured
by the applicable test methods specified by rule.
Ambient
air concentrations for PM-b
are usu~1ivn~mressedin
cubic meter
(ug/m?-)-
“Pneumatic Rubber Tire Manufacture”:
The production of
pneumatic rubber tires with a bead diameter
irn
to
but
not
including 20.0 inches and cross section dimension up to 12.8
inches, but not including specialty tires for antique or
other vehicles when produced on equipment separate from
normal production lines for passenger or truck type tires.
“Polybasic Organic
Acid Partial Oxidation Manufacturing
Process”:
Any process involving partial oxidation of
hydrocarbons with air to manufacture polybasic acids or
their anhydrides,
such as maleic anhydride, phthalic
anhydride,
terephthalic acid,
isophthalic acid, trimcllctic
anhydridc.
“Portable Grain-Handling Equipment”:
Any equipment
(excluding portable grain dryers) that is designed and
maintained to be movable primarily for use in a
-
non-continuous operation for loading and unloading one—turn
storage space, and is not physically connected to the grain
elevator, provided that the manufacturer’s rated capacity of
the equipment does
not exceed 10,000 bushels per hour.
“Portland Cement Manufacturing Process Emission Source”:
any items of process equipment or manufacturing processes
used in or associated with the production of portland
cement,
including,
but not limited to,
a kiln,
clinker
cooler, raw mill system,
finish mill system, raw material
percent.
A combination of ethylbcnzene, ketones having branched
hydrocarbon structures or toluene:
20 percent.

dryer, material storage bin or system, material conveyor
belt or other transfer system, material conveyor belt
transfer point, bagging operation, bulk unloading station,
or bulk loading station.
“Portland Cement Process” or “Portland Cement Manufacturing
Plant”:
Any facility or plant manufacturing portland
cement
by either the wet or dry process.
“Power Driven Fastener Coating”:
The coating of nail,
staple, brad and finish nail fasteners where such fasteners
arc fabricated from wire or rod of 0.0254 inch diameter or
greater, where such fasteners are bonded into coils or
strips,
such coils and strips containing a number of such
fasteners, which fasteners arc manufactured for use in power
.-__-l.-.-.-_
-
~cuz.a~iu~
LOS
Lu
u~c~ u~~
and national organizations including FedeL-u~
~peuiiiuuciun
FF-N-105b of the General Services Administration dated
August 23,
1977
(does not include any later amendments or
editions; U.S. Army Armament Research and Development
Command, Attn:
DRDAR-TST, Rock Island,
IL 61201), Bulletin
UH-25d of the U.S. Department of Housing and Urban
Development
-
Federal Housing Administration dated
-
P~m1-rmhrr
F~
1rJ7’~
(does not include any later amendmrnt-i
or
-,
ucoartment of HUD, 547 W. Jackson Blvd.. Room
jo,
IL 60606), and the
4
1
Buildi.~,
-
American Building Officials,
and similuL
Code of the
~cunuurui~.
For
the
purposes
01.
~.i1L~
UOLi1LLLiUfl~
the
terms
“brad” and “finish nail” refer to single leg fasteners
fabricated
in the came manner as staples.
The application
of coatings to staple,
brad,
and finish nail fasteners may
be associated with the incremental forming of such fasteners
in a cyclic or repetitious manner
(incremental fabrication)
or with the forming of strips of such fasteners as a unit
from a band of wires
(unit fabrication).
“PPM
(Vol)
-
(Parts per Million)
(Volume)”:
A volume/volume
ratio which expresses the volumetric concentration of
gaseous air contaminant in a million unit volumes of gas.
“Pressure Release”:
The emission of materials resulting
from system pressure being greater than set pressure of the
pressure relief device.
“Pressure Tank”:
A tank in which fluids are stored at a
n-ressure greater than atmospheric pre~ure.
“Prime Coat”:
The first film of coating material applied in
~-u
multiple eo~toneratign.
OOE
-Me e~
34
and which
~
.~a....
I
~-...I
~2
editions,
1005, Chi
ii of
coupe
-
-5-

35
t”:
A film of
rrl,ti
touches up areas on the surface not adequately covered by
the prime coat before application
of the top coat.
“Process”:
Any stationary emission source other than a fuel
combustion emission source or an incinerator.
“Process Unit”:
Components assembled to produce, as
intermediate or final products,
one or more of the chemicals
listed in 35 Ill.
Adm. Code 215.Appcndix D.
A process unit
can operate independently if supplied with sufficient feed
or raw materials and sufficient storage facilities for the
product.
“Process
Unit
Shutdown”:
A work practice or operational
procedure that stops production from a process unit or part
of a process unit.
An unscheduled work practice or
operational procedure that stops production from a process
unit or part of a process unit for less than 24
hours
is not
a process unit shutdown.
The use of sparc components and
technically feasible bypassing of components without
stopping production is not a process unit shutdown.
“Process Weight Rate”:
The actual weight or engineering
approximation’ thereof of all materials except liquid and
gaseous fuels and combustion air,
introduced into any
process per hour.
For a cyclical or batch operation,
the
process weight rate shall be determined by dividing ouch
actual weight or engineering approximation thereof by the
number of hours of operation excluding any time during which
the equipment is
idle.
For continuous processes,
the
process weight rate shall be determined by dividing such
actual weight or engineering approximation thereof by the
number of hours
in one complete operation,
excluding any
time during which the equipment is idle.
“Production Equipment Exhaust System”:
A system for
collecting and directing into the atmosphere emissions of
volatile organic material from reactors, centrifuges and
other process emission sources.
4-I
~f
1-
-~
1_’
~IuL
1.—’-e—...’,—.--.—---.-..11-p—.-’
r-~
r!nv:1
,
rluIllr’n
-
-
ii
1
~
11r
,
ri~
u1u’~T
“Publicati~.,-~t,~....~
Printing”.
printi..~
i-p
paper
~-~4e~
“~sequently formed into books,
m&~izinc~,
~‘
‘----
-.-
-~
_a.~2
supplements or other types of non—pacicaging printed
materials.
testing
“Purged Process Fluid”:
Liquid or vapor from a process unit
that contains volatile organic material and that results
from flushing or cleaning the sample line(s)
of a process
unit so that an uncontaminated sample may then be taken for
4

36
“Reactor”:
A vat, vessel or other device in which chemical
reactions take place.
“Reasonably Available Control Technology
(1IACT)”:
The
lowest omission limitation that an omission source is
capable of meeting by the application of control technology
that is reasonably available considering technological and
economic feasibility.
-
“Refincry Fuel Cac”:
Any gas which is generated by a
petroleum refinery process unit and which is combusted at
the refinery,
including any gaseous mixture of natural gas
and fuel gas.
“Refinery Unit,
Process Unit or Unit”:
A set of components
which are a part of
a basic process operation such as
distillation, hydrotreating, cracking or reforming of
hydrocarbons.
“Refrigerated Condenser”:
A surface condenser in which the
coolant supplied to the condenser has been cooled by a
mechanical device, other than by a cooling tower or
evaporative spray cooling, such as a refrigeration unit or
steam chiller unit.
“Residual Fuel Oil”:
Fuel oil-s of grade No.
4,
5 and
6 as
specified in detailed requirements for fuel oils A.C.T.H.
D—396—69
(1971).
-
“Restricted Area”:
The area within the boundaries of any
“municipality” as defined in the Illinois Municipal Code,
plus a zone extending one mile
beyond the boundaries of any
suon municipality having a ~
of 1000 or more
according to the latest federal census.
1
“Ringelmann Chart”:
The chart published and described in
the Bureau of Mines,
U.S. Department of Interior,
Information Circular 8333 (Revision
of 1C7718) May
1,
1967,
or any adaptation thereof which has been approved by the
Agency.
“Roadway”:
Any street,
highway, road,
alloy,
sidewalk,
parking lot,
airport, rail bed or terminal, bikeway,
pedestrian mall or other structure used for transportation
purposes.
“Roll Printing”:
The application of words,
designs and
ni
etnre~
to
n
~ub~trnt~
u~u~
1 lv by menn~ of
~
~eri o~ of hnrd
5__
-
“Rotogravure Printing”
The application of words, designs
-
~Il
printing
~~1

37
technique in which the pattern to be applied is recessed
relative to the non-image area.
“Safety Rclic~Thlvr’
—-
I
— -
_t.
I_C~~
I
wnion
iu
uc~ignca
to open in oraer to relieve excessive
pressures within a vessel or pipe.
“Candblaoting”:
The use of
a mixture of sand and air at
high pressures for cleaning and/or polishing any type of
surface.
“Screening”:
Separating material according to size by
pressing undersized material through one or more mesh
surfaces (screens)
in series,
and retaining oversized
material on the mesh surfaces
(screens).
“Censor”:
A device that measures a physical quantity or the
change in a physical quantity ouch as temperature, pressure,
flow rate,
pH, or liquid level.
“Set of Safety Relief Valves”:
One or more safety relief
valves designed to open
in order to relieve excessive
pressures in the came vessel or pipe.
“Sheet Basecoat”:
A coating applied to metal when the metal
is in sheet fOrm to serve as either the exterior or interior
of a can for either two-piece or three—piece cans.
“Chotbiasting”:
The usc of a mixture of any metallic or
non-metallic substance and air at high pressures for
cleaning and/or polishing any type of surface.
“Side-Scam Spray Coat”:
A coating applied to the seam of
a
three—piece can.
“Smoke”:
Small gas-borne particles resulting from
incomplete combustion,
consisting predominately but not
exclusively of carbon, ash and other combustible material,
that form a visible plume in the air.
“Smokeless Flare”:
A combustion unit and the stack to which
it is affixed in which organic material achieves combustion
by burning in the atmosphere such that the smoke or other
particulate matter emitted to the atmosphere from such
combustion does not have an appearance density or shade
darker that
No.
1 of the Ringlcmann Chart.
~
r~
1
~rr~n
T
-
sun
.-
-
process
~-~f
r~1f’111iI1r!
~r,il~z frr~m
-~è~
.~
by-
ld clcanL.~-~—~..
top vapor de~a.
~
conveyorized degreasing.

38
tiLJE~1U.JLSL
L
51I
“Specialty High Gloss Catalyzed Coating”:
Commercial
~iishing
of
__5~2
macor iai.
prepaL-eu
jUL
pL-.Lnters and
lithographers where the finishing process uses
a
solvent—borne coating, formulated with a catalyst,
in a
quantity of no more than 12,000 gallons/year as supplied,
where the coating machines arc sheet fed and the coated
sheets are brought to a minimum surface temperature of 190°
F, and where the coated sheets are to achieve the minimum
specular reflectance index of
65 measured at a 60 degree
angle with a gloss meter.
“Splash Loading”:
A method of loading a tank, railroad tank
car, tank truck or trailer by use of other than a submerged
loading pipe.
“Stack’1:
A flue or conduit, free standing or with exhaust
port above the roof of the building on which it is mounted,
by which air contaminants are emitted into the atmosphere.
“Standard Conditions”:
A temperature of 70°F and a
pressure of 14.7 pounds per square inch absolute
(psia).
“Standard Cubic Foot
(sof)”:
The volume of one cubic foot
of gas at standard conditions.
“Startup”:
The setting in operation of an emission source
for any purpose.
“Stationary Emission Source”:
An emission source which is
not self-propelled.
“Stationary Storage Tank”:
Any container of liquid or gas
which
is designed and constructed to remain at one site.
“Submerged Loading Pipe”:
Any loading pipe the discharge
opening of which
is entirely submerged when the liquid level
is
6 inches above the bottom of the tank.
When applied
to—a
tank which is loaded from the side,
any loading pipe the
submerrir’rl when the liquid
discharge
.--c
~
~
“c~ly
level
i-c
18 inches or two times the loading pipe diameter,
whichever is greater, above the bottom of the tank.
The
definition shall also apply to any loading pipe which is
continuously submerged during loading operations.
.--
Jfl
“Sulfuric Acid Mist”:
Sulfuric acid mist as measured
according to the method specified in 35
Ill.
Adm. Code
~14
101 (h~
-
‘—I
r’~A
4
device
from a gas stream by reducing the temperature of the stream-i-
without direct contact between the coolant and the stream.

39
“Synthetic Organic Chemical or Polymer Manufacturing Plant”:
A plant that produces,
as intermediates or final products,
one or more of the chemicals or polymers listed in 35 Ill.
Adm. Code 215.Appcndix D.
“Tablet Coating Operation”:
A pharmaceutical coating
operation in which tablets are coated.
“Top Coat”:
A film of coating material applied
in a
multiple coat operation other than the prime coat,
final
repair coat or prime surfacer coat.
“Transfer Efficiency”:
Ratio of the amount of coating
deposited onto a part or product to the total amount of
coating solids used.
“Tread End Cementing”:
The application of a solvent-based
cement to the tire tread ends.
“True Vapor Pressure”:
The equilibrium partial pressure
exerted by a petroleum liquid as determined in accordance
with methods described in American Petroleum Institute
Bulletin 2517,
“Evaporation Loss From Floating Roof Tanks”
(l962-)--
-
“Turnaround”:
The procedure of shutting down an operating
refinery unit,
emptying gaseous and liquid contents to do
inspection, maintenance and repair
work,
and putting the
unit back into production.
“Undcrtread Cementing”:
The application of a solvent—based
cement to the underside of a tire tread.
“Unregulated Safety Relief Valve”:
A safety relief valve
which cannot be actuated by a means other than high pressure
in the pipe or vessel which it protects.
“Vacuum Producing System”:
Any reciprocating, rotary or
centrifugal blower or compressor,
or any jet ejector or
device that creates suction from a pressure below
atmospheric and discharges against a greater pressure.
“Valves
Not
Externally Regulated”:
Valves that have no
external controls, such as in line check valves.
unloading tank and a receiving
tank
such that vapors
displaced from the receiving tank are transferred to the
tank being unloaded.
Balance System”:
Any combination of pipes or ho~cu
r’~lrvlrrl
syctr—m
hr-tcirr-n thr~ u-nrlnr-
~flr1r~r—t
r-,-f
r-,.

item”:
All piping,
cc:
vents
-~
“Vapor Control System”:
Any system that prevents release to
the atinoophore of organic material in the vapors displaced
from a tank during the transfer of gasoline.
“Vapor Mounted Primary Seal”:
A primary seal mounted with
—~
—~
h~n~r-t~
by
-t-hr— h~fPr~m
of the
~r
iTh1-r-L’
~~-i
1
,
the
tank wall,
the liquid
and the floating roof
this definition.
For ~
-of-
“ith emission limits, volatile
For purposes of this definition,
the following organic
compounds have been determined to have negligible
flhotOehCmicl)l reactivity and are not volatile organic
5--.-
materials:
Chlorodifluorocthane
(HCFC-142b)
Ch1orodif’uorometh~une (CFC-2’~’
-~
_,—,i-~
1_
—~.
1
— —
Dichlorodifluoromethanc(CFC-i2)
Dichlorofluoroethane
(HCFC-14lb)
Dichloromethane
(Hethylenc chloride)
Diohlorotetrafluoroethano
(CFC-114)
Dichlorotrifluoroethane
(HCFC-l23)
1, 1-Difluorocthane
(HFC-152a)
Ethane
Methane
Pentafluoroethane
(HFC-l2 5)
Tetrafluoroethane
(HFC-134a)
1,1,2,2-Tetrafluoroethane
(HFC 134)
Trichlorocthane (Methyl chloroform)
“Vapor Collccti
connections
40
~~1
.
r-
~
,
sources between
processing unit
-the gasoline delivery vessel
and/or the storage tanks and
and the vapor
vapor holder.
.ls,
hoses,
“Vinyl Coating”:
The application of a topcoat or printing
to vinyl coated fabric or vinyl sheets; provided, however,
that the application of an organisol or plastisol is not
vinyl coating.
“Volatile Organic Liquid”:
Any liquid which contains
volatile organic material.
“Volatile Organic Material”:
Any organic compound which
in atmo2phoric
~
-
LipcuLL...~Liy
exexnptect
determining complianoc
organic material shall be measured i~y
cii~
LCLULCnUO
methods incorporated by reference in 35 Ill.
Adm. Code
215.105.
Where such a method also inadvertently measures
compounds with negligible photoohemical reactivity,
an owner
or operator may exclude these negligibly reactive compounds.

41
1,1,l-Trichloroethane
(Methyl chloroform)
Trichlorofluoromethane (CFC 11)
Trichlorotrifluoroethane (CFC
Trifluoromcthane
(FC-23)
113)
and the following classes of compounds:
Cyclic,
branched,
or linear, completely fluorinated
alkanco.
Cyclic, branched,
or linear, completely fluorinated
ethero with no unoaturations.
Cyclic, branched,
or linear, completely
-I-c~rtiirv
~Th1fl~~!1
uith no
fluorinated
-L
Sulphur-containing perfluorocarbons with no unsaturations
and with sulfur bonds only to carbon and fluorine.
BOARD NOTE:
USEPA or the Agency may require
monitoring to demonstrate the amount of an exempted
compound in a source’s emissio-nc on a case-by-ease basis
as a pre-condition to exemption of that compound under
certain circumstances,
such as where VOMs and exempted
compounds are mixed together, there are a large number of
exempted compounds, or the chemical composition of the
excmo’—-~coir-’~oundo
215.108;
56 Fed flog.
11419—20.
~-‘-iown.Sec 35 Ill.
Adm.
CocL
In.
-I
S.
1
1
Ut
t~~t#
U
S~
t
_ld result
from the exposure of a coating, printing ink, fountain
solution, tire spray, dry cleaning waste or other similar
material to the air,
including any drying or curing,
in the
absence of any control equipment.
VOMC is typically
expressed as kilogram
(kg) VOM/liter
(lb VON/gallon)
of
coating or coating solids,
or kg VON/kg
(lb VOM/lb)
of
coating soliri~~~
of coal—inn material or material.
“Volatile Petroleum Liquid”:
Any petroleum liquid with a
true vapor pressure that is greater than 1.5 psia
(78
millimeters of mercury)
at standard conditions.
“Wastewater
(Oil/Water)
Separator”:
Any device or piece of
equipment which utilizes the difference in density between
oil and water to remove oil and associated chemicals of
water, or any device, such as a flocculation tank or a
clarifier, which removes petroleum derived compounds
f
rem
waste water.

42
“Weak Nitric Acid Manufacturing Process”:
Any acid
producing facility manufacturing nitric acid with a
concentration of less than 70 percent by weight.
,~lishingand mai..~, 4-i~p~
wood.
(Source:
Repealed at
_______________________________________
)
Ill.
Reg.
_____,
effective
Section 211.130
Accelacota
“Accelacota” means a pharmaceutical coating operation which
consists of a horizontally rotating perforated drum in which
tablets are placed.
a coating is applied bY spraying. and the
coating is dried by the flow of air across the drum through the
perforations.
(Source:
Added at
Section 211.150
Ill.
Reg.
_____,
effective
Accumulator
“Accumulator” means the reservoir of a condensing unit receiving
the condensate from a surface condenser.
(Source:
Added at
Ill.
Reg.
-__,
effective
______________
Section 211.170
Acid Gases
“Acid gases” means,
for the purposes of Section
9.4 of the
Environmental Protection Act
(the Act)
(Ill. Rev.
Stat.
1991,
ch.
111~,par.
1009.4)
415
ILCS 5/9.41, hydrogen chloride, hydrogen
fluoride and hydrogen bromide, which exist as gases, liquid mist,
or any combination thereof.
(Source:
Added at
Section 211.210
Ill. Reg.
_____,
effective
Actual Heat Input
“Actual heat input” means the quantity of heat produced by the
combustion of fuel using the gross heating value of the fuel.
“Woodworking”:
The shaDing,
sawing, grinding, smoothing,
oaucts of any form or shape of
(Source:
Added at
Ill. Reg.
_____,
effective

43
Section 211.230
Adhesive
“Adhesive” means any substance or mixture of substances intended
to serve as a joining compound.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.250
Aeration
“Aeration” means the practice of forcing air through bulk stored
grain to maintain the condition of the grain.
(Source:
Added at
Ill.
Reg.
,
effective________________
Section 211.290
Afterburner
“Afterburner” means
a control device
in which materials
in
gaseous effluent are combusted.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.310
Air Contaminant
“Air contaminant” means any solid,
liquid,
or gaseous matter,
any
odor, or any form of energy, that is capable of being released
into the atmosphere.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.330
Air Dried Coatings
“Air dried coatings” means any coatings that dry by use of air or
forced air at temperatures u~to 363.l5°K(194°F).
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.350
Air Oxidation Process
“Air oxidation process” means any unit process including
ammoxidation and oxychiorination which uses air or a combination
of air and oxygen as an oxidant in combination with one or more
organic reactants to produce one or more organic compounds.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________

44
Section 211.370 Air Pollutant
“Air pollutant” means
an air pollution aaent or combination of
such agents,
including any physical, chemical, biological,
radioactive
(including source material, special nuclear material,
and byproduct material)
substance or matter which is emitted into
or otherwise enters the atmosphere.
Such term includes any
precursors to the formation of any air pollutant, to the extent
that the relevant statute or rule has identified such precursor
or precursors for particular purpose for which the term “air
pollutant”
is used.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.390
Air Pollution
“Air pollution” means the presence in the atmosphere of one or
more air contaminants in sufficient quantities and of such
characteristics and duration as to be injurious to human, plant,
or animal life,
to health,
or to property, or to unreasonably
interfere with the enjoyment of life or property.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.410
Air Pollution Control Equipment
“Air pollution control equipment” means any equipment or
apparatus of a type intended to eliminate,
prevent, reduce or
control the emission of air contaminants to the atmosphere.
(Board Note:
The requirements to obtain permits for air
pollution control equipment,
in 35
Ill.
Adm. Code 20l.Subpart C,
apply to such equipment intended to eliminate,
prevent, reduce or
control the emissions of specified air contaminants from
stationary emission units.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.430
Air Suspension Coater/Dryer
“Air suspension coater/dryer” means a pharmaceutical coating
operation which consists of vertical chambers in which tablets or
particles are placed, and a coating is applied and then dried
while the tablets or particles are kept in a fluidized state by
the passage of air upward through the chambers.
(Source:
Added at
Ill.
Reg.
_____,
effective
________________
______________________________
)

45
Section 211.450
Airless Spray
“Airless spray” means a spray coating method in which the coating
is atomized by forcing it through a small opening at high
pressure.
The coating liquid is not mixed with air before
exiting from the nozzle.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.470
Air Assisted Airless Spray
“Air assisted airless spray” means a spray coating method which
combines compressed air with hydraulic pressure to atomize the
coating material into finer droplets than is achieved with pure
airless spray.
Lower hydraulic pressure
•is used than with
airless spray.
(Source:
Added at
Ill. Reg.
_____,
effective
________________
Section 211.490
Annual Grain Through-Put
“Annual grain through—put” unless otherwise shown by the owner or
operator, annual grain through—put for grain—handling operations,
which have been in operation for three consecutive years prior to
June 30,
1975,
shall be determined by adding grain receipts and
shipments for the three previous fiscal years and dividing the
total by
6.
The annual grain through-put for grain-handling
operations in operation for less than three consecutive years
prior to June 30,
1975,
shall be determined by a reasonable
three—year estimate; the owner or operator shall document the
reasonableness of his three—year estimate.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
______________________________
)
Section 211.510
Application Area
“Application area” means an area where a coating is applied by
dipping, spraying or other techniques.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.530
Architectural Coating
“Architectural coating” means any coating used for residential or
commercial buildings or their appurtenances,
or for industrial
buildings, which is site applied.

46
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
_______________________________
)
Section 211.550
As Applied
“As applied” means the formulation of a coating during
application on or
impregnation into a substrate,
including any
dilution solvents or thinners added at the source before
application of the coating.
(Source:
Added at
Ill.
Reg.
_____,
effective
______________
Section 211.570
Asphalt
-
“Asphalt” means the dark-brown to black cementitious material
(solid,
semisolid,
or liquid in consistency)
of which the main
constituents are bitumens which occur naturallY or as a residue
of petroleum refining.
(Source:
Added at
Ill. Reg.
_____,
effective
______________
Section 211.590
Asphalt Prime Coat
“Asphalt prime coat” means a low-viscosity liquid asphalt applied
to an absorbent surface as the first of more than one asphalt
coat.
(Source:
Added at
Ill. Reg.
_____,
effective
______________
Section 211.610
Automobile
“Automobile” means a motor vehicle which normally has four
wheels,
is used predominately for carrying 12 or fewer
passengers,
and
is not a light-duty truck.
(Source:
Added at
Ill.
Reg.
_____,
effective
______________
Section 211.630
Automobile or Light-Duty Truck Assembly Source
or Automobile or Light-Duty Truck Manufacturing
Plant
“Automobile or light—duty truck assembly source” or “Automobile
or light-duty truck manufacturing plant” means a source where
parts are assembled or finished for inclusion into
a finished
automobile or light—duty truck ready for sale to vehicle dealers,
but not including customizers,
body shops, and other repainters.

47
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.650
Automobile or Light-Duty Truck Refinishing
“Automobile or light-duty truck refinishing” means the repainting
of used automobiles and light-duty trucks.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
__________________________________
)
Section 211.670
Baked Coatings
“Baked coatings” means any coating which is cured or dried in an
oven where the oven air temperature exceeds 90°C(194°F).
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.690
Batch Loading
“Batch loading” means, with respect to solvent cleaning, the
process of loa~’-”-sa
~
of
j~~jV~dti~1
oarts
at the same time
for degr~sina
(Source:
Added at
_____
_______________
Ill.
Reg.
effective
)
Section 211.710
Bead—Dipping
of an
.
assembled tire bead into a
“Bead-dipping” means the dipping
solvent—based cement.
(Source:
Added at
Ill.
Reg.
Section 211.730
Binders
“Binders” means organic materials and
effective
resins which do not contain
VOM.
(Source:
Added at
Ill.
Reg.
effective
Section 211.750
British Thermal Unit
“British Thermal Unit” means the quantity of heat required to
raise one pound of water from 60°Fto 61°F (abbreviated btu).
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
)

48
Section 211.770
Brush or Wipe Coating
“Brush or wipe coating” means a manual method of applying a
coating using a brush, cloth, or similar object.
(Source:
Added at
Ill. Reg.
_____,
effective
______________
__________________________________
)
Section 211.790
Bulk Gasoline Plant
~j
“Bulk gasoline plant” means,
for purposes of 35
Ill.
Adm. Code 215, any gasoline storage and distribution
source that receives gasoline from bulk gasoline
terminals by delivery
vessels and distributes gasoline
to gasoline dispensing operations.
~j
“Bulk gasoline plant” means,
for purposes of 35
Ill.
Adm.
Code 218 and 219,
a gasoline storage and
distribution source with an average throughput of
76,000
1
(20,000 gal)
or less on
a 30—day rolling
average that distributes gasoline to gasoline
dispensing operations.
(Source:
Added at
Ill. Reg.
_____,
effective
______________
_________________________________
)
Section 211.810
Bulk Gasoline Terminal
“Bulk gasoline terminal” means any gasoline storage and
distribution source that receives gasoline by pipeline, ship or
barge,
and distributes gasoline to bulk gasoline plants or
gasoline dispensing operations.
(Source:
Added at
Ill. Reg.
_____,
effective
______________
Section 211.830
Can
“Can” means any cylindrical single walled metal container, with
or without a top,
cover,
spout or handles, with walls thinner
than 29 gauge
(0.0141
inch)
into which solid or liquid materials
may be packaged.
(Source:
Added at
Ill.
Reg.
_____,
effective
______________
Section 211.850
Can Coating
“Can coating” means any protective, decorative or functional
coating applied onto the surface of a can or a metal sheet or
metal part which
is made into a can.

49
(Source:
Added at
Ill.
Reg.
_____,
effective
Section 211.870
Can Coating Line
“Can coating line” means a coating line in which any protective,
decorative, or functional coating is applied onto the surface of
a can or a
m~t~1
~
or metal tart
tzh~~’h
is
~
into
a can.
(Source:
Added at
Ill. Reg.
effective
211.890
Capture
Section
“Capture” means the containment or recovery of emissions from ~r’
emission unit for direction into a duct which may be exhausted
through a stack or vent to a control device.
The overall
abatement of emissions from an emission unit with an add—on
control device
is
a function both of the catture efficiency and
of the control device efficiency
(Source:
Added at
Ill.
Reg.
effective
211.910
Capture Device
Section
“Capture device” means a hood, enclosed room,
floor sweep or
other means of collectina volatile
~
m~t~-$~1
or other air
contaminants into a duct.
The pollutant can then be directed to
a pollution control device such as an afterburner, carbon
adsorber.
fabric filter or scrubber.
Sometim~s
the term is used
loosely to include the
er’~nt1-r~1
device.
(Source:
Added at
Ill. Reg.
effective
Section 211.930
Capture Efficiency
“Capture efficiency” means, for purposes of 35
Ill. Adm.
Code 218
and 219, the weight of VON entering a capture system and
delivered to a control device divided by the weight of VON
generated by an emission unit,
during a particular time period,
expressed as a percentage.
(Source:
Added at
Ill.
Reg.
effective
Section 211.950
Capture System
“Capture system” means all equipment
(including, but not limite-i
to, hoods,
ducts,
fans,
ovens,
dryers,
etc.)
used to contain
collect and transport an air contaminant to
a control device.

50
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.970
Certified Investigation
“Certified investigation” means
a report signed by Illinois
Environmental Protection Agency
(Agency) personnel certifying
whether a grain—handling operation (or portion thereof)
or
grain—drvina operation is causing or tending to cause air
pollution.
Such report must describe the signatory’s
investigation,
including a summary of those facts on which the
signatory relies to certify whether the grain-handling or
grain-drying operation is causing Or
threatening or allowing the
discharge or emission of any contaminant into the environment so
as to cause or tend to cause air pollution in Illinois,
either
alone or in combination with contaminants from other sources,
or
so as to violate regulations or standards adopted by the
Pollution Control Board
(Board)
under the Environmental
Protection Act
(Act).
The certified investigation shall be open
to a reasonable public inspection and may be copied upon payment
of the actual cost of reproducing the original.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
Section 211.990
Choke Loading
“Choke loading” means that method of transferring grain from the
grain-handling operation to any vehicle for shipment or delivery
which precludes a free fall velocity of grain from a discharge
spout into the receiving container.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
Section 211.1010
Clean Air Act
“~CleanAir Act” means the Clean Air Act Amendments of 1970
(42
U.S.C.
~7401
et seq.),
as amended in 1977 and 1990.
(Source:
Added at
Ill.
Reg.
,
effective
_______________
Section 211.1050
Cleaning and Separating Operation
“Cleaning and separating operation” means that operation where
foreign and undesired substances are removed from the grain.
(Source:
Added at
Ill.
Reg.
,
effective
_______________

51
section 211.1090
clear Coating
“Clear coating” •eans coatings that lack color and opacity or are
transparent using
the
undercoat
as
a reflectant base or undertone
color.
(Source:
&dded at
___
Ill, keg.
____-,
effective
________________
______
)
Section 211.1110
clear Topcoat
“Clear topcoat” means the final coating which contains binders.
but not opaque pigments,
and is specifically foniulatedto form
a
transparent or translucent solid protective LiLt
(Source:
Added
at
___
Ill.
Reg.
_____,
effective
_______________
__________________________________
)
Section
211.1130
Closed
Purge
System
“Closed
purqe
system”
means
a
system
that
is
not
open
to
the
atmosphere
and
that
is
composed of pipin~.connections,
and,
if
necessary,
flow inducing devices that transport liquid or vapor
from a piece or pieces of equipment to
a control device,
or
return the liquid or vapor to the process line.
(Source:
Added
at
___
Ill. Rag.
_____
,
effective
________________
__________________________________
)
Section
211.1150
Closed
Vent
System
“Closed vent system” means
a system that is not open to the
atmosphere and is composed of piping,
connections, and,
if
necessary,
flow inducing devices that transport gas or vapor from
a piece or pieces of equipment to
a contrcl device.
(Source:
Added at
Ill.
fleg.
_____
effective
________________
__________________________________
)
Section
211.1170
coal
Refuse
“Coal
refuse”
means
waste
products
of
coal
mining,
cleaning
ar.d
ccal preparation operations contaIning coal. matrig material.
clay and other organic and inorganic material.
(Source:
Added at
Ill. Reg.
_____
affective
_______________
__________________________________
)
Section
211.1190
Coating
~j
“Coating”
means,
for
purposes
of
35
Ifl.
Adn.
Code
215.
p material applied
to
a
substrate
for
decorative.

52
protective or
shall include,
other
but
functional purposes.
Such material
are not limited to taints.
adhesives, diluents and thinners.
varnishes,
sealers,
“Coating” means,
for purposes of
35 Iii.
7~dm. Code 213
and 219.
a material applied onto or impregnated into a
substrate for protective.
gecorative.
or functional
purposes.
Such materials include,
but are not limited
t~c?I
oa~nts.yapiishes.
sealers, adhesives, thinners.
diluents.
and
inks.
(Source:
Added
at
Ill.
Reg.
____,
effective
_____________
___________________________________________
)
Section
211.1210
Coating
Applicator
“Coating
applicator”
means
equipment
used
to
apply
a
coating.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
______________
__________________________________
)
section 211.1230
coating Line
~j
“Coating line” means,
for rurposes
of 35
Ill. Adm.
Code
215.
an operation where
a surface coating
is applied to
a material and subse~uentlvthe coating
is dried andfor
cure
a.
pJ~
“Coating line” means.
for rurposes
of 35
Ill. Adm.
Code
218 and
2l~.
an operation cpnsist~n~
of
a series
of one
or fore coating applicators and any associfled
lash—off
areas, drying areas,
and ovens wherein
a
coating is applied,
dried.
and/cr cured.
A coating
line ends at the point where the coating
is dried
or
cured,
or prior to any subsequent antl~cptionof
a
different coating.
It is not necessary for an
operation
to have an oven or
a flash—off area
in order
to be included
in this definition,
(Source:
Added
at
Ill. Reg.
_____
effective
______________
Section 711.1250
Coating Plant
“Coating plant” means any building, structure or installation
that
contains
contiguous
or
a
coating
adiacent
line
and
properties
which
and
is
)ocated
Dn
which
is
owned
one
or
or
more
operated
by the same nerson
(or by persons under comnon control).
(Source:
Added at
Ill.
Peg.
_____
effective
__________________________________________
)

53
section 211.1270
coil Coating
“Coi
coating’~means any Drotective,
decorative or functional
coatina which
is applied onto any flat metal sheet or strip which
is delivered to the coatina line as a roll or coil,
unwound and
coated as
a continuous substrate.
(Source:
Added at
___
Ill.
Rag.
_____
effective
_______________
___________________________________________
)
SectiQn 211.1290
coil Coating Line
“Coil
c5,ptinci line” means a c?atini~line in which any protective,
decorative
oj fun?tional coating is applied onto any flat metal
sheet
or strip which is delivered to the coating line as
a roll
or coil.
ynwounU and
coated as
a continuous substrate.
(Source:
Added
at
___
Ill.
Beg.
,
effective
_______________
___________________________________________
)
Section 211.1310
cold Cleaning
“Cold cleaning” means the process cf cleaning and removing soils
froit surfaces by sPrayina.
brushing,
flushing,
or immersion while
maintaining the organic solvent below its boilina point.
Wipe
cleaning is not included in this definition.
(Source:
Added at
___
Ill.
Reg.
_____,
effective
_______________
___________________________________________
)
Section 211.1330
Complete Combustion
“Ceiliplete combustion” means a process
in which all carbon
contained in
a fuel or gas stream is converted to carbon dicxide.
(Source:
Added at
___
Ill.
Req.
_____,
effective
________________
___________________________________
)
Section 211.1350
component
“Corponent” means any piece of eguipment which has the potential
to leak volatile organic IDaterial
(VOM)
including,
but not
limited to.
pump
seals,
compressor seals,
seal oil degassing
vents.
‘oioeline valves,
pressure relief devices, process drains,
and open ended va3ves and lines,
and flanges.
For ~uroose~ of
Subyaçts 0 and R in
35
Ill.
Adm.
Code
215.
218
and 219.
this
definition excludes valves which are not externally regulated,
flanges,
and eauinrnent
in heavy liauid service.
For purposes
of
Subpart
0 of
35 Ill. Adm. Code 215.
213
and, 219, this defjr,ition
also excludes bleed ports of gear pumps
in polymer service.

54
(Source:
Added
at
Ill.
Req.
_____
,
effective
)
section 211.1370
Concrete Curing Compounds
“Concrete curing compounds” means any coating applied to freshly
~
concrete to retard the evaporation of
water.
(Source:
Added
at
___
Ill.
Reg.
_____
,
effective
_______________
__________________________________
)
Section 211.1390
concentrated Nitric Acid Manufacturing Process
“Concentrated nitric acid manufacturing process” means any acid
producing facility manufacturing nitric acid with
a concentration
equal to or qre~te~than 70 percent by weight.
(Source:
Added
at
___
Ill. Reg.
_____
,
effective
_______________
___________________________________________
)
Section 211.1410
Ccndensate
“Condensate” means vj~1atxleorganic liDuid separated from its
associated gases
which condenses due
to changes
in the
temDerature or pressure
and
remains li~jid~t standard
conditions.
(Source:
Added at
___
Ill.
Beg.
_____
,
effoctive
_______________
___________________________________________
)
Section 211.1430
Condensible PM—la
“Condensible PM—b” means PM-jo forred
iiunediately or shortly
after discharge to the atmosphere, as measured by the applicable
test
method
specified
in
35
Ill.
Adm.
Code 212.110.
Condensible
particulate
matter
exists
in
gaseous
and/pr
vapor
form
prior
to
rele~se
to
the
atmosphere.
e.g.,
in
the
stack,
and
focms
particulate matter upon condensation when subject to conditions
p1
cooling pr~ddilution in the atmosphere.
(Source:
Added at
Ill.
Rog.
_____,
effective
______________
__________________________________
)
Section 211.1470
Continuous Process
“Continuous process” means,
with respect to manufacture of
polystyrene resin,
a method of manufacture
in which the styrene
raw material
is delivered on
a continuous
basis tc the reactor in
which the styrene
is polymerized to polystyrene.
(Source:
Added at
Ill.
Reg.
_____
,
effective
______________
___________________________________________
)

55
Section 211.1490
Control Device
1CQntrol
devices
means
equipment
(such
as
an
afterburner.
adsorber,
fabric filter or scrubber) used to remove or prevent
the emission of
an air contaminant from
a contaminated exhaust
stream.
(Source:
Added
at
Ill.
Reg.
_____
effective
_______________
__________________________________
)
Section 211.1510
Control
Device
Efficiency
“Contrcl device efficiencyu means,
for purposes of
35
Ill. Adm.
code 218 and 219.
the weight
of VON generated by an emission Unit
which
is
destroyed
or
removed by a control device,
divided by the
weight
of
VON
generated
by
such
unit entering the control device.
during
a
particular
time
period,
exoressed
as
a
percentage.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
________________
___________________________________
)
section 211.1530 conventional Soybean Crushing Source
“Corivent:ona~soybean crughing source” means any hexane
extractlQn soybean crushtn~equipment that uses direct contact
steam for desolventizing and producing toasted soy meals.
(Source:
Added at
Ill. Reg.
_____
,
effective
_______________
___________________________________
)
Section 211.1550
Conveygrized Degrepsing
“Conveyprized degrepsing”
ujeans the continuous process of
cleaning and removing soils from surfaces utilizing either cold
or vaporized solvents.
(Source:
Added at
___
Ill. Re;.
_____
,
effective
_______________
___________________________________________
)
Section
211.157D
Crude
Oil
“Crude oil” means
a naturally occurring mixture which consists of
hydrocarbons and sulfur. nitr~~en.or oxygen derivatives
of
hydrocarbons and which
is
p
liciuld
at
standard
conditions.
(Source:
Added
at
Ill. Reg.
_____
,
effective
_______________

56
Section 211,1590
Crude Cii Gathering
“Crude
oil
qpthe~ing”
means
the
transportation
of
crude
oil
or
condensate after custody transt~rbetween
a production site and
a
at
___
Ill. Beg
Crushing
_____
effective
“Cr9hing” means
machine
such
as
harirnermill.
and
the
fragmentation of non—metallic minerals
p
jaw,
gyrators’,
cone,
roll,
rod,
mill,
:m~actor.
by
a
(Source:
Added at
Ill,
Beg.
_____
effective
Section 211.1630
“Custody
transfer”
Custody Transfer
and/or condensate after
producing operations.
processing
andlor
treating
in
the
from
storage
tanks
or
automatic
transfer
other
forts
of
transportation.
(Source:
Added at
—)
Ill.
Reg.
_____
effective
Section 211.1550
Cutback Asphalt
“Cutback asphalt” means any asphalt which has been liguified by
blending with petr9ieum solvents pther than residual
Cuel oil
arid
has not been emulsified with water.
(Source:
Added at
___
Ill.
Reg.
____,
effective
______________
___________________________________________
)
Section 211.1670
Daily—Weighted Average
‘1CM Content
“Daily—weighted average
VOl.! content” Feans the average
‘10K
content of two or more cpatthgs as apDlied on a coating line
during any day, taking into account tha fraction of total coating
volume that each coating represents,
as calculated with the
following equation:
VOlt
=
I
I
V.
C
IIVT
reception point.
(Source:
Added
)
Section 211.1610
systems to ni~elinesor
any
pleans the transfer
of oroduced petroleum

57
cqatinas
line
it.
as applied
units of ka
each
VOMIt
day on
(lbs
a coating
yaM/pal)
ot
coatina
(minus
water
and
any
compounds
which
are soecifically exempted from the definition
of VOM~.
The
number
of different coatings as applied
each day on a coating
line.
The
volume
of
epch coatincT
(minus water and
any
comoound~ w4ch
are
soecifically
exemoted
from the definition of VOM~ as applied each
day on a coating line in units of
1
(gal)
The
‘1GM content cf each coat:ng as ppplied
each day on a coating line
4n units of
kg
VCN/l
(lbs VON/gal)
of coating
(minus water
and any corupouj~swhich are specifjcally
exempted frcm the definition
of VOM)
.
arU
the
total
volume of all coatings
~
and any compounds which are speciticaijy
exempted froni the definition of VON)
as
applied each~4ayon~ coating lime in units
of
1
(galL,
(Source:
Added
)
at
Ill.
Reg.
effective
Section 211.1690
~fl~y”_mean~,for pprpose~qfPert 218
qzi ~ri~th~
consecutive
24 hours beginning at
1,2:00
PSI4
(midnight)
local time
or beginning at
a fixed tine consistent with the source’s
operating schedule,
as provided below.
A source may use
a day
b~gj~~ftgat
~tiare
other
than
midnight
which
is
consistent
with
its operating schedule provided that the owner or operator of the
source first notifies that Agency in writir.g of such alterr.ative.
describing why
it would be more reasonable to mpintain records
on
this basis.
The owner or operator shall notify the Agency
in
~
in the time
at
which
a
d~y
(Source:
Added at
Ill.
Reg.
_____
effective
=
The average
VOl.! content of two or
more
where:
VON.
I
ci
begins.
_____
______
)

58
Section 211.1710
Depreaser
“Degreaser”
means
ally
e,uipment
or
system
used
in
solvent
cleaning.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______
___________________________________
)
3~ction
21L.J.fl~
fl~v~y_Vessal
“Delivery vessel” ~eans afly tank truck or trailer equipped with
a
storage tank that
is used for the transport of gasoline to
a
stationary storace tank at a gasoline djspensing operation, bulk
gasoline plant,
or bulk gasoline terminal.
(Source:
Added at
111.
Req.
effective
)
SectjQn 211.1750
Dip Coating
“Dip coating’ means
a method of applying coatings in which the
part is submerged in a tank filled with the coating.
(Source:
Added at
Ill. Reg.
,
effective
)
Section 211.1770
Distillate Fuel Oil
“Distillate fuel oil” means
fuel oils of arade No.
1 or
2 as
specified in detailed requirements for fuel oil ASTM D—369—69
(1g71)
incorterated by reference
in 35
Ill.
Adm. code 218.112 and
219. 112.
(Source:
Added at
Ill. Reg.
,
effective
)
Section 211.1790
Drum
“Drum” means any cylindrical shi~pingcontainer of
13 to
110—gallon
capacity.
(Source:
Added at
Ill.
Reg.
effective
)
section 211,1810
Dry Cleaning Operation or Dry Cleaning
Facility
“Dry
cleaning
operation”
or
“Dry
cleaning
facility”
means
the
cleaning of fabrics using an essentially nonagueous solvent by
means
of one or ~noresolvent washes1 extraction of excess solvent
by spinning and dry±ngby tumbling tn an airstreain.
The dry
cleaning operation or facility includes, but
is not
limited to,

59
washers, drye~s.filter and purification systeiis.
waste disposal
systems, holding tanks, pumps and attendant piping and valves.
(Source:
Added at
Ill. Req.
_____
,
effective
_______________
___________________________________________
)
Section 211.1830
Dump—Pit Area
“Dump—pit area” means any area where grain
is received at a
grain—hand1in~or grain—drying operation.
(Source:
Added
at
Ill.
Peg.
_____
,
effective
________________
Section 211.1BSO
Effective Grate Area
“Effective grate area” means that area of
a dunp—pit grate
through which air nasses.
or would pass. when aspirated.
(Source:
Added at
Ill.
Rag.
_____
,
effective
________________
____________________________________________
)
Section 211.1870
Effluent Water Separator
“Effluent
water
separator”
9ans any
tan)c.
box.
suntp or other
actaratus
in which any organic material floating cn or entrained
or contained
in water entering such tank,
box. sump or other
apparatus is physically separated and removed frpi~such water
prior to outfall, drainage or recovery of such water.
(Source:
Added at
___
Ill.
Req.
_____•
effective
________________
___________________________________________
)
SeptjQn 211.1890
Electrostatic Bell or Disc Spray
tiElectrostatic
bell
or
disc
spray”
means
an electrostatic srrav
coating
n~ethod in
which
a
rapidly—spinning
bell—
or
disc—snaped
applicator is
used
to
create
a
fine mist and apply the coating
with high transfer efficiency,
(Source:
Added at
Ill.
Req.
_____
,
effective
_______________
)
Section 2fl.2910
Electrostatic Spray
“Electrostatic spray” means
a spray coating nethod
in which
opposite electrical charges are applied to the substrate ~nd the
cQating,
The coating ~s attractsd to the obiect due to the
electrostatic potential between
them.
(Source:
Added at
Ill.
Req.
_____,
effective
_______________
___________________________________________)

60
Section 211.1930
Emis sion
Rate
“Emi?ston
rate”
means,
Provison.
tl?e
tçital.
cpa
containriant discharged
if
not
ot
gntity of
into
the
herwise
stated
~ particular
atmosphere in
in
srec
any
a specifis
if led
air
one—hour
period.
For
example,
if not otherwise snecified
in 35
Ifl.
Adja.
Code 218 or 219.
emission rate ~epns the total quantity of
volatile
organic
material
discharged
into
the
atmosphere
in
any
one—hour period.
(Source:
Added at
Ill. Beg.
,
effective
)
Section 211.1950
Emission Unit
“Emission unit”
means
any
part
or
activity at a stationary source
that emits or has the potential to enit any air ~ol1utant.
(Source:
Added at
Ill. Reg.
,
effective
~
Section 211.1970
Enamel
“Enamel” means
a coating that
cl.Ires bY chemical cross—linking of
its base resip.
Enamels can be dist~nqiiishedfrpm lacQuers
because enamels are not readily resoluble
in their original
solvent.
(Source:
Added at
til. Reg.
,
effective
)
Section 211.1990
Enclose
lEncloss!
means.
for curpose of
35
fll.
Athu.
Code 2l5.481(c~.
21~.482(b)
.
218.481(c).
218.482(b). 219.481(c)
and 219.482(b).
to
cover
any volatile organic liquid surface that
is exposed tc the
atmosphere.
(Source:
Added at
Ill. Reg.
effective
)
Section 211.2010
End Sealing Corpound Coat
“End sea1in~conDound coat” means
p
can Coating applied to
Can
ends which functions as a gasket when the end is assembled onto
the can.
(Source:
Added
at
—)
Ill.
Reg.
_____
effective
Section 211.2050
Ethanol Blend Gasoline

61
“Ethanol blend gasoline” means
a ilixture of gasoline and at
least
9
ethanol by volume.
(Source:
Added at
Ill.
Rag.
_____
effective
________________
Section 211.2070
Excess Air
“Excess air” means air supplied in addition
to the theoretical
quantity necessary for coinolete combustion of all fuel
ar.d/or
combustible waste material.
(Source:
Added at
Ill. Reg.
_____•
effective
_______________
___________________________________________)
Section 211.2090
Excessive Release
~
release” means,
for pu~’pasesof 35
Ill. Adn. Code
215.144. 218.144 and 219.144.
p
discharge of more than
295
g
(0.55
Ibs)
of merc~ptansand/or hydroqen sulfide j~tothe
atnosphere
Sn
any 5—minute period.
(Source:
Added
at
Ill. Req.
_____,
effective
________________
___________________________________________ )
Section 211.2110
Existing Grpin—Drying Operation
“Exist4.n~
qrain—drying
operation”
m~ans any
ctnin-drying
operation
the
construction
or
modification
of which was commenced
prior
to
June
30,
1975.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
________________
___________________________________
)
Section 211.2130
Existing Grain—Handling Cperation
“Existing grain—handling
operation”
means any grain—handling
operation the construction or modification
of which was coxrnenced
prior to June
30.
1975.
(Source:
Added at
Ill.
Reg.
_____,
effective
_________________
___________________________________
)
Section 211.2150
Exterior Ease Coat
“Exterior base coat” means
a can ccatir~gaDplied to the exterior
of
a two—piece can body to provide protection to the metal or to
provide baclcground for any lithographic or pyjntjnn operation.
(Source:
Added at
Ill.
Reg.
_____
effective
_______________
___________________________________________)

62
Section 211.2170
Exterior End Coat
“Exterior end coat” means
a
can coating applied to the exterior
end of
a can to provide protection to the metal.
(Source:
Added at
Ill.
Reg.
_____
,
effective
________________
___________________________________________)
Section 211.2190
External Floating Rcof
“External floating roof” means
a cover
c’fer an ooen top storage
tank consisting of
a double deck
or pontoon single deck which
rests upon and
is supported by the volatile organic liquid being
contained and
is equipped with
a closure seal or seals to close
the space between the roof edge and tank shell.
(Source:
Added at
ill.
Reg.
_____
effect~.ve
_______________
___________________________________________)
Section 211.2210
Extreme Performance Coating
“Extreme
performance
coating” ~eans any coating which during
intended use
is exposed to any or all of the following;
ambient
weather conditiQns. temperatures consistently above 95°C(203~F~
detergents,
abr~si-veanp scouring agents,
solvents,
or corrosive
atmtosnheres.
(Source:
Added at
___
Lii.
Rag.
_____•
effective
_______________
___________________________________________)
Section 211.2230
Fabric Coating
“Fabric coating” ~neansany protective, decorative or functicnal
coating which
is applied onto or impregnated into
a textile
fabric which
is delivered to the coating pine as
a roll, unwound
and coated as
a continuous
substrate.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
_______________
___________________________________
)
Section 211.2250
FabrIc Coating Line
“Fabric coating line” means
a coating line in which
any
protective,
decorative,
or functional coating is anplied onto or
impregnated into a textile fabric which
is delivered to the
coating line as
a roll,
unwound and coated as a continuous
substrate.
(Source:
Added at
Ill.
Rag.
_____
effective
_______________
___________________________________________)

63
Section 211.2270
Federajlv Enforceable Limitations and
Conditions
“Federally enforceable limitations
and conditions” means all
limitations and conditions which are en~orcepbleby the
Administrator of the USEPA. including those requirements
developed pursuant to
40 CFR Parts
60 and 61: requirements within
any
applicable
implementation
plan;
and
any
permit
requirements
established
pursuant
tc
40
CR
52.21
or
40
CFR
52.737
or
undor
regulations aooroved oursuant to 40 CFR Part 51 Subpart
I.
40 CFR
51.266 and 40 CFR Part 70.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
________________
section 211.2310
Final Repair Coat
“Final repair coat” means,
with respect to automobile or
light-duty truck assembly
or manufacturing.
a ccptinc which
is
used to repaint topcoat which
is damaged during vehicle assenbly.
(Source:
Added at
___
Ill.
Reg.
_____,
effective
_______________
___________________________________
)
Section 211.2330
Firebox
“Firebex”
means
the
chamber
or
compartment
of
a
boiler
or
furnace
in which riaterials are burned,
but not the combustion chamber or
afterburner of
an incinerflpr.
(Source:
Added
at
___
Ill. Reg.
_____
,
effective
________________
___________________________________
)
Section 211.2350
Fixed—Roof Tank
“Fixed—roof
tank”
means
a
cylindrical
shell
with
a
permanently
affixed
roof.
(Source:
Added
at
___
Ii.
Reg.
____
,
effective
______________
Section
211.2370
Flexoqraphic Printin~
•‘Flexoqraphic printing” me~nsa
roll
printing
technique
in
which
the pattern to be applied
is raised above the printing roll and
the
jmpcje carrier
is made of rubber
or other elastrneric
materials.
(Source:
Added at
Ill. Reg.
_____
effective
_______________

64
Section 211.2390
Flexographic~Printing Line
“Flexographic printing linel rne~nsa printing line performing
flexographic printing.
(Source:
Added at
Ill. Reg.
-
~,
effective
___________
_______
)
Section 211.2410
Floating Roof
“Floating roof” means
a roof on a stationary tank,
reservoir,
or
other container which moves vertically upon change
ir. yoltr.e of
the 5tcred material.
(Source:
Added at
Ill.
Reg.
,
effective
)
Section 211.2430
Fountain Solution
“Fountain
solution”
means
the
solution
used
in
certain
methods
of
printing
which
is
applied
to
the
image tiate to maintain
hydrophilic propertias of
the
non—itiage
areas.
(Source:
Added at
Ill.
Reg.
,
effective
)
Section 211.2450
Freeboard Height
Mpreeboard height” jnoans.
for open top vapor degreasers, the
distance
from
the
ton
of
the
vapor
zone
to
the
top
of
the
degreaser
tank,
and
for
cold
gleaning
de~reasers,
the
distance
front the solvent to the top of the degreaser tank.
(Source:
Added at
Ill.
Reg.
,
effective
)
Section 211.2470
Fuel Combustion Enissign Unit or Fuel
Combustion
Emission
Source
“Fuel
combustion
emission
unit”
or
“Fuel
tombustion
emission
source” neans any furnace,
boiler.
or similar equ±nmqntused for
the primary Durpose
of producing heat or power
isv indirect heat
transfer.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
_______________
Section 211.2490
Fugitive Particulate Matter
“Fugitive
particulate
matter”
means any particulate itatter
emitted
into
the
atmosphere
other
tUan
through
a
stack,
provided
that
nothir.q
in this definition or in 35
Ill. Adm.
Code
212,

65
SubDart
K shall exemnt
other provisions of 35
any
Ill.
emission unit
Adm.
Code 212
frog co~flapce
wi~k
otherwise applicable
merely because of the absence of
p
stack.
(Source:
Added at
___
Ill. Rag.
_____
effective
_______________
section 211.2510
FuLl Operating Flowrate
“Full operatinc
flowrate”
Leans
maximum
operating
capacity
of
the
Source,
emission unit or process unit.
as acnlicable.
(Source:
Added at
___
Ill.
Req.
_____,
effective
_______________
____________________________________________
)
Section 211.2530
Gas Service
“Gas
service” means th?t the equipment
or
component contains
process fluid that is
in the gaseous state at operatincx
conditions.
(Source:
Added at
___
Ill. Req.
_____
,
effective
________________
)
Section
211.2550
Gas/Gas
Method
“Gas/gas
irethod”
means
either
of
two methods
for
detenining
VON
canture efficiency which rePi only on ~ps phase measurements.
The first method requires construction of
a temporary total
enclosure
(flfl
to
ensure
that
all
would—be
fugitive
emissions
are measured.
The second method uses the building or room which
houses the coating line,
printing line Cr other eraissicn unit as
an enclosure.
The second method requires that all other VOM
lines or emission units within the room be shut down while the
test
is performed, but all fans and blowers within the room must
be operated according to normal procedures.
(Source:
Added at
___
Ill.
Reg.
_____,
effscfive
________________
___________________________________
)
Section 211.2~7O
Gasoline
“Gasoline” means
any
petroleum distillate
or petroleum
distillate/alcohol
blend
haying
a Reid vapor pressure cf 27.6
kPa
or greater which
is used as a fuel for internal combustion
engines.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
Section 211.2590
Gasoline Dispensing Operation or Gasoline
Dispensing Facility

66
“Gasoline discensina operation”
or “Gasoline dispensing facility”
means any site where gasoline is tt~asferredfrom a stationary
storage tank to a motor vehicle gasoline tank used to provide
fuel to the engine of that motor vehicle.
(Source:
Added at
___
Ill.
Reg.
_____,
effective
_______________
Secticn 211.2650
Grain
“Grain”
means
the
whole
kernel
or
¶eed
of
corn,
wheat,
opts.
soybeans
and
any
other
cereal
or
oil
seed
olant
and
the
ncj~rmal
fines,
dust
and
~preign
matter
whij~h
results
from
harvesting,
hanfling or
conditioning.
The grain shall
be
unaltered by
grinding or processing.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
Section 211.2670
Grain—Drying Operation
“Grain—drying operation” neans any operaticn.
excluding aeration.
by which moisture is removed from grain anà which typically uses
forced ventilation with the addition of heat.
(Source:
Added at
___
Ill. Reg.
_____
effective
_______________
___________________________________________)
Section 211,2690
Grain-Handling and Conditioning Operation
‘Grain—handljnc and conditioning operation” ~leansa grain stDrage
facility and its associate grain transter.
ceaning,
drying.
grinding and mixing operations.
(Source:
Added at
___
Ill. Peg.
_____
effective
_______________
___________________________________________)
Section 211.2710
grain—Handling Operation
“Grain—handling operation” means any operation where one
or more
of the following grain—related processes
(other than grain—drying
operation,
portable grain—handling equipment,
one—turn storage
space,
and excluding flour mills and feed mills)
are pertox’raed:
receiving,
shipping, transferring,
storing.
liiixifln or treating of
grain or other processes pursuant
to nornal qrain operations.
(Source:
Added
at
Ill. Peg.
_____
effective
_______________
___________________________________________)
Section 211.2730
Green-Tire Spraying

67
“Green tire spraying” means the spraying of green tires,
both
4nside
ançl outside.
from
the tire during
wit~-iplease
molding and
comoou.mds which
prevent the tire
hçlp
trom
rempve air
sticking
to the mold atte~puring.
(Source:
Added at
__________________________________
)
Ill. Req.
_____
effective
Section 211.2750
Green Tires
“Green tires” means assembled tires before molding and curing
have
occurred.
(Source:
Added at
Ill.
Req.
_____
effective
Section 211.2770
GrQSS
Heatinq_Y~Lu~
“Gross heatxnr
value” means amount of heat produced when
a unit
quantity
of fuel
is burned to carb1n di1xide and water vapor,
and
the water vappr condensed as described
in ASTN D2015—6t. D900—55.
D1826—64 and D240—64 incorporated by reference
in Section 211.101
of this Part.
(Source:
Added
at
___
Ill.
Peg.
—)
______
effective
Section 211.2790
GrossVehi
cit
Weight
Rating
“Cro~svehicle
manufacturer
as
weight rfling” means
the maximum design
the value specified by the
loaded weight of
a single
vehicle.
(Source:
Added at
—)
Ill.
Peg.
_____
effective
Section 211.2910
Heated
Airless
Spray
“Heated airless
spray”
means
an
airless
spray
coating method
in
which the coating
is heated lust pflor to application.
(Source:
Added
at
—)
Ill.
Reg.
_____
effect:ve
Section 211.2330
Heatset
“Heatset”
Irigans
a class of
lithography which requires
a heated
dryer
to
solidify
the
printing
inks.
(Source:
Added
at
Ill.
Reg.
effective
)

68
Section 211.2850
Heatset—Web—Offset Lithographic Printing t~in~
“Heatset—web—offset lithographic printing line” means
a
Uthographic prjnting
jpe
in which
a blanket cylinder
is used to
transfer
ink
from
a
olate
cylinder
to
a
substrate
continuously
fed
from
a
roll
or
an
extension
process
and
an
oven
is
used
tg
solidify the printing inks.
(Source:
Added
at
___
Ill.
Req.
_____
,
effective
_________________
___________________________________
)
Section 211.2870
Heavy Liauid
“Heavy
liauid’1
means
liquid
with
a
true
vapor
pressure
of
less
than
0.3
Icpa
(0.04 psi)
at 294.39
(70°F)
established
in
a
standard
reference
text
or
as determined by ASTM method 02879-86
(incorporated
by
reference
in 35
Xli.
Adm.
Coae 218.112
and
219.112); or which hay 0.1 Reid Vapor Pressure as determined
by
?aSTh method D323—82
(j.ncprporated by reference in
35
Ill. Adn.
Code 215.105,
213.112 and 219.112);
or which when distilled
requires a temperature
of 421.959
(300°FI or greater to recover
10 cercent of the liquid as determined by ASTM method D86—82
(incorvorated by reference
iii
35 Iii. Adm.
Code 215.105. 218.112
and 219.112).
(Source:
Added at
___
Ill.
Reg.
_____;
effective
_________________
___________________________________
)
Section
211.2890
Heavy
Metals
“Heavy
metals”
means,
for
the
purposes
of
Se?tion
9.~ of
the
Act.
elemental,
tonic.
or
combined
forms
of
arsenic.
cadnuun.
mercury,
chromium,
nickel
and
lead.
(Source:
Added at
___
Ill. Reg.
_____
effective
_________________
___________________________________
)
Section
211.2910
Heavy
0ff—Highway
Vehicle
Products
“Heavy off—highway vehicle products” means heavy construction.
mining.
fBrming,
or material handling equipment
heavy industrial
engines; diesel—electric locomotives and associated Dower
generation equipment: and the constituent marts of such eauioment
or
engines.
(Source:
Added
at
Ill.
Req.
_____
,
effective
_______________
Section
211.2930
Heavy
0ff—Highway
Vehicle
Products
Coating
“Heavy
off—highway vehicle products coating” means
any
protective,
decorative or functional coating applied onto the

69
surface
of
heavy
off—highway
vehicle
products.
However,
a
high
temperature aluminum coating to
a diesel—electric locomotive
in
Cook County is not a heavy
off—highway vehicle products coating.
(Source:
Added
at
___
Ill.
Reg.
_____•
effective
_______________
___________________________________
)
Section 211.2950
HrVV
Off—Highway
Vehicle
Products
Coating
Line
“Heavy off—highway ve~ic~~
cro4ucts Qpating l4ne” mepn~a coating
jine
ip
wl)ich any
nroteçtive.
decorative.
cr
functional
coating
is applied onto the surface of heavy off-highway vehicle
products.
However,
application of
a high tenoerature aluminum
coating to a diesel—electric locomotive in Cook County ~s not
a
heavy off—highway vehicle products coating line or part of
a
heavy off-highway vehicle products coating line.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_________________
___________________________________
)
Section 211.2970
High Temperature Aluminur Coating
“High temoerature aluminum coating” means
a coating that is
certified to withstand
a temperature of 537.8°C (lOOC°E) for ~4
hours.
(Source:
Added at
ill.
Req.
_____,
effective
_______________
___________________________________
)
Section
211.2990
High
Volume
Low Pressure
(HVLP)
Stray
“High volume low pressure
CHVLP)
spray” means equipment used to
apply coatings
by means of
a spray gun which operates between
0.1
and 10 psig air pressure.
(Source:
Added
at
Ill.
Req.
_____
,
effective
________________
___________________________________
)
Section 211.3010
Hood
“Hood”
ipeans
a partial enclosure or canopy for capturing and
~xhaustng.
by means of
a draft
the organic y~pprsor other
funtes produced fron a coating line,
printing line or other
emission unit.
(Source:
Added at
Ill.
Reg.
_____
effective
________________
___________________________________________)

Section 211.3030
Hot Well
“Hot well” means the reservoir of
a condensing unit receiving the
condensate from
a barometric condenser.
(Source:
Added at
Ill.
Reg.
,
effective
)
Section 211.3050
Housekeeping Practices
“Hoyse)ce~pingprpctices” means those adtivitie~so?cifjcally
defined
in the list of housekeeping practjce~~evetoped by the
Joint EPA
Industry Tp~JçForce and included herein under
35
Iii.
Adn.
Code 212.461.
(Source:
Added ~t
Ill. Reg.
_____
effective
______________
___________________________________
)
Section
211.3070
Incinerator
erncinerator~tmeans p combustion apparatus
in which refuse is
burned.
-
(Source:
Added At
Ill.
Reg.
_____,
effective
_____________
Section 211.3090
Indirect Heat Tnnsfer
“Indirect
heat
transfer”
means
transfer
of
heat
in
such
a
way
that the source of heat
do-es not come into direct contact with
process materials.
(Source:
Added at
Ill.
Peg.
_____
,
effective
______________
___________________________________
)
Section 211.3110
Ink
“Ink” means
a coating used
in printing.
Impressing.
or
transferring words,
pictures,
designs or other images onto
a
substrate.
(Source:
Added at
___
Ill.
Peg.
_____
,
effective
______________
___________________________________
)
Section 211.3130
In—Process Tank
“In—process
tank”
means,
with
respect
to
~panufacture
of
~hanaceutical~.
a
container
used
for
mixing,
blending,
heating.
reacting
holding. crystallizinc~,evaporating
or cleaning
operations.
70

71
(Source:
Added
at
111.
Reg.
_____
,
effective
________________
)
Section 211.3150
In—Situ Sp~plingSvsters
“In—situ
sampling
systems”
means
nonexractive
sanplers
or
in—line
samplers,
(Source:
Added at
Ill. Beg.
_____
,
effective
_____________
_______
)
~ection 211.3170
Interior Body Spray Coat
~Interior body spray coat” means
a can coating applied
by spray
to the interior of
a can body.
(Source:
Added at
Ill. Peg.
_____
effective
___________
Section 211.3190
Internal—Floating Rocf
“Internal—floatina roof” means
a cover or roof in a fixed—roof
tank
which
rests
upon
and
is
supported
by
the
volatile
organic
liquid being contained and is eauipped with a closure seal or
seals to close the space between the roof edge and tank shell.
(Source:
Added at
Ill.
Req.
_____•
effective
_______________
)
Section 211.3210
Internal Transferring Area
“Internal transferring area” means areas and associated equipment
used
for convoying grain among the various arain operations.
(Source:
Added
at
___
Ill.
Peg.
_____,
effective
_______________
____________________________________________
)
Section
211.3230
Lacquers
“Lacquers”
means,
with
resoect
to
coating
of
wood
furniture,
any
clear
wood
finishes
formulated
with
nitrocellulosc
or
synthetic
resins to dry tv evaporation without chemical reaction,
including
clear lacquer sanding sealers.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
___________________________________________)
Section 211.3250
Large Appliance
•~Large appliance”
means
any
residential
and
corirnercial
washers,
dryers,
ranges,
refrigerators,
freezers,
water
heaters,

72
dishwashers,
trash
compactors,
air
conditioners,
and
other
~jnii1arproducts.
(Source:
Added at
Ill. Req.
~,
effective
______________
__________________________________
)
Section 211.3270
Large Appliance Coating
“Lar9e aPplianpe coatipg” meaps
flflV ~rotectivt. decorativç or
functional coating applied onto the surfa?e of lprqe a9~1jances
or to the constituent
metal
oartp (in~1udin~.but not inited to,
doors.
cases,
lips,
tanels.
and
interior support parts~ of large
appliances.
(Source:
Added
at
___
Ill.
Peg.
_____
,
effective
_______________
___________________________________
)
Section 211.3293
Large Appliance Coating Line
“Large appliance coating
line” means
p
coating line in which
any
trptective.
decorativ?.
or
functional
coating
is
applied
onto
the
~urf~cç
of
~açge
~~pliances
or
to
the
constituent
aetaj.
parts
(ipcll?dinQ
but
no~ imited
tç’
doors,
cases,
lids,
panels
and
interior
Darts)
of
large
appliances.
(Source:
Added
at
___
Ill.
Peg.
_____
effective
_______________
__________________________________
)
Section 211.3310
Light Liquid
“Light
licuid”
means
‘2pM
in
the
liauid
state
which
is
not
defined
as
heavy
liquid.
(Source:
Added
at
___
Ill.
Peg.
_____
effective
_______________
Section 211.3330
Light—Duty Trucic
“Light—duty truck” means any motor vehicle with
a gross veh:cle
weight rating
of 3.650 kg or less,
designed mainly to transport
trooerty.
(Source:
Added at
___
Ill. Reç.
_____
,
effective
_______________
Section 211.3350
Light Oil
“Light oil” means
a liquid condensed or absorbed from coke oven
gas composed of benzene. toluene.
and xvlene.
(Source:
Added at
Ill.
Peg.
_____
effective
_______________

73
Section 211.3370
Liquid/Gas Method
“Liquid/gas method” means either
of two methods for determining
‘tOM capture efficiency which require both gas phase and liquid
Dhase measurements and analysis.
The first method requires
construction of a temporary total enclosure
(TTE)
to ensure that
all would—be fugitive emissions are measured.
The second method
uses
the
building or
room
which houses the coating
line,
printing
line or other emission unit as an enclosure.
The second methQ~
reai,ires
that
all other VON lines or emissien units within the
room be shut down while the test
is performed,
but all fans and
blowers within the
room
must be ooerated according to norrnp:1
procedures.
(Source:
Added at
——
Ill.
Peg.
_____,
effectiye
_________________
_______
)
$ection
211.319_Q
kjauid—Mounted
Seaj.
“Liquid—mounted
seal”
means
a
primary seal mounted
in continuous
contact with the liquid between the tank wall and the floating
roof
edae
around
the
circumference
of
the
roof.
(Source:
Added
at
___
Ill.
Req.
_____,
effective
________________
__________________________________
)
Section
211.3410
Liquid
Service
“Liquid service” means that the equipment or component contains
process fluid that
is
in
a liquid state at operating conditions.
(Source:
Added at
___
Ill. Beg.
_____•
effective
________________
___________________________________________)
Section 211.3430
Liquids Dripping
tlLjqflj?s
dripping”
m9ns
any
visibje
leaking
from
p
seal
including
spraying,
misting,
clouding
and
ice
formation.
(Source:
Added
at
___
Ill.
Peg.
_____
,
effective
_________________
__________________________________
)
Section 211.3450
Lithoqraph!c Printing Line
“Lithographic printing lineM means
a web or sheetfed printing
line ii which each roll printer uses
a roll where both the image
and non—image areas are essentially
in the same plane
(‘olariographici
(Source:
Added
at
Ill.
Peg.
_____
,
effective
________________
__________________________________
)

74
Section 211.3470
Load—Out Area
“Load—out area” means any prep where grain is transferred from
the grain—handling operation to any veh:cle for shipment Cr
delivery.
(Source:
Added at
Ill. Req.
_____
,
effective
____________
___________________________________
)
Section 211.349D
Low_Solvent Coning
“Low solvent coating” means
a coating which contains less organic
solvent than the conventional coatings used by the industry.
Low
solvent coatings include water—borne, higher solids.
elecrtro—deposition and powder coatings.
(Source:
Added at
ill. Req.
,
effective
Section 211.3510
Magnet Wire
“Macmet
Wire”
~eans aluminum or popper wire which may
subsecuently be used in an electromagnetic device.
(Source:
Added at
Ill. Peg.
,
effective
)
Section 211.3530
Magnet Wire Coating
“Magnet wire coating’1 means any electrically insulating varnish
or enamel or other protective,
decorative or functional coating
applied onto the surface
of macnet wire.
(Source:
Added at
Ill. Rag.
,
effective
)
Section
211.3550
Magnet Wire Coating Line
“Magnet wire coating iine~means
a coating
line
in
which
any
electrically insulating varnish or enamel or other ttrotective.
decorative,
or functional coating
is
applied
onto
the
surface
of
magnet wire.
(Source:
Added
at
Ill.
Reg.
effective
)
Section 211.3570
Major Dump Pit
“Malor
dump
pit”
means
any
dump
pit
with
an
annual
qrair~
through—put
of
more
than
300,000
bushels,
or
which
receives
more

75
than
40
or
the
annual
grain
through—put of the grain-handling
operation.
(Source:
Added
at
Ill.
Reg.
____
effective
_____________
__________________________________
)
Section 211.3590
Malor 1’letrooolitan Area (WI
“Major Metropolitan
Area (14MM” means any county or group of
counties
which
is defined by the following Table:
MAJOR METROPOLITAN AREAS I~iILLINOIS (MMA’p~
COUNTIES INCLUDED IN
MMA
~
Champaign
ChicagQ
Cock.
L&ce~Yifl. p~Page2
Mcllenry. Kane. G~ujj~y,
Kendall._Kan)cakee
Decatur
Macon
Peoria
Peoria. Tazewell
Rockford
Winneingo
Rock Island
Moline
Rock
Island
Springfield
Sangarng~
St. Louis
(Illinois)
St. Clair, Madison
Bloomington
Norral
McLean
(Source:
Added
at
Ill.
Beg.
_____,
effective
_______________
)
Section 211.3610
Major Population Area
(MPA)
“Major Po~ulat~onArea
(MPA)” means areas of salor pcpufltion
concentration in Illinois,
as described below:
The area within the counties of Cook; Lake; DuPage;
Will:
the townships
of Burton.
Richmond, McHenry.
Greenwood.
Nunda, Door,
Algonquin,
Graftori and the
municipality of Woodstpck, plus
a zone extending
twc’
miles beyond the boundary of said nunicip~litylocated
in Mcffenry County; the townships of Dundee. Rutland.
Elgin, Plato.
St. Charles.
Campton.
Geneva, Dl~ckberry,
Batavia,
Sucax Creek and Aurora located in Kane County;
and the nunicibalities of Kankakee. Bradley and
Bourbonnais.
nlus a
zone extending two niles beyond the
boundaries of said nunicicalities in Kankakee County.
The area within the municipalities of Rocktord and
Loves Park.
plus
p zone extending two miles beyond
the
boundaries of said municipalities.

76
The area within the municipalities of
ROCK
Island,
Noline,
East Nouns. Carbon Cliff, Milan.
Oak Grove.
Silyis.
Uanpton. Greenwood and Coal Valley, plus a zone
extending two miles beyond the boundaries of said
municipalities.
The area within the municipalities of Galepburg and
East Galesburg. nlus
a zone Txtefldfla two miles beyond
the
boundaries of said municipalities.
The ~rea within the municipalities of Bartonv+lle.
P~oripand Peoria Heights. plus
a zone 1xtend~n~two
miles beyond the boundaries
of said nunpc.palities.
The area within the municipalities of Pekin. North
Pokin. Harauette
I-feiahts. Creve Coeur and East Peoria,
plus a zone extent~ingtwo miles beyond the boundaries
of said municipalities.
The
prep
within the municipalities of Bloomington and
Normal.
plus p zone extend:ng two miles beyond the
boundaries of
said
municipalities.
The area within the municipalities of Champaign.
Urbana
and Savoy.
plus
a zone extending two itiles beyond the
boundaries of said municipalities.
The area within the municipalities of Decatur.
Mt.
Zion.
Harristown and Forsyth,
pJ.us
a zone extending t~o
miles beyond the boundaries ~f said municipalities.
The prep within the municipalities of Springfield,
Leland Grove. Jerome.
Southern View, Grandview,
Sherman
and
Chathn.
olus
a
zone
extending
two
miles
beyond
the
boundaries
of
said
municit’aliUes.
The
prep
within
the
townships
of
Godfrey.
Foster.
Wood
River.
Fort
Russell,
Chouteau,
Edwardsville,
Venice,
Narieoki,
Alton,
Granite City and Collinsville located
in Madison County: and the townships of Stites.
Canteen,
Centreville.
Caseyville,
St. Clair.
Sugar Loaf
and Stookey located
in St. Clair County.
(Source:
Added at
Ill.
Reg.
_____
,
effective
________________
___________________________________________ )
Section 211.3630
Nanufacturin~Process
“Nanufacturing process” means
a method Whereby
a process emission
unit or series of process enission units is used to convert raw
materials,
feed stocks. subasserablies.
or other constituent parts

77
lato
a
yroduct.
either for saleor
for
use
in
a
subseauent
manufacturing oroce~L,
(Source:
Added
at
Ill. Reg.
,
effective
_____________-
___________________________________________ )
Section 211.3650
Marine Teninal
“Marine terrinal” means
a facility primarily engaged in loading
and unloading watercraft.
(Source:
Added
at
___
Ill. Reg.
_____,
effective
_________________
Section 211.3670
Material
Recovery
Section
“Material recovery section” meahs. with respect tc manufacture of
polystyrene resin,
any
ecuiDnient designed to transport and
recover styrene monomer
and
other impuritaes from other products
and by—products ~n a polystyrene plant,
including but not limited
to the stvrene devolatizer uniU~pndstyrene recovers’ unit.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
___________________________________________ )
Section
211.3690
Maxjmmn
Theoretical
Emissions
“Maximum
theoretical
ernissions”~ means
the
cuantity
of
volatile
organic
material
emissions
thatLtheoreticplly
could
be
emitted
by
a
stationary
source
before
add—On
controls
based
on
the
design
capacity
or
t~aximumproduction
capacity
of
the
source and 3760
hours per year.
The design capécity or maximum production
capacity includes use
of coatin~ts)or ink(s)
with the highest
volatile organic material
conteflt actually used
in practice by
the source, provided, however,
the Agency shall, when
appropriate, and upon request by the permit applicant,
limit the
“max4mçni th~oretipalemissions”- of
a source by the imposition of
conditions in
a federally enforeeable operating permit for such
source.
Such conditions
shall not be inconsistent with
requirements of the Clean Air Act,
as amended.
or any applicable
requirements established by theBoard.
Such conditions shall be
established in olace of design capacity or maximum production
capacity in calculating the
‘maximum theoretical
ernissions’ for
such source and may include,
among other things,
the
establishment of production limitations,
capacity limitations,
or
limitations on the volatile organic material content of coatings
or ±nks. or the hours of operation of any emission unit, or a
combination of any such li~itatjons.
Production or capacity
lipitations shall
be established on
a basis of no longer than one
month except
in those cases where
a limit spanning a longer
period of tine is appropriate.
In such cases,
a limit or
limitation must not exceed an annual
limit rolled on a basis of

77
into
a product,
either for sale or for use in
a subseguBnt
manufacturing process.
(Source:
Added at
Ill. Req.
_____
effective
_______________
section 211.3650
Marine Tertinal
“Marine terminal” means
a t~cilityprimarily engaged
in loadiig
and unlopUing wateroraft.
(Source:
Added
at
___
Ill. Req.
_____
effective
_______________
___________________________________________ )
Section 211.3670
Material Recovery Section
“Material recovery section” means, with respect to manufacture of
polystyrene resin,
any em~ipmentdesigned to transport and
recover styrene monomer and other impurities from other products
and by—prcducts
in a polystyrene plant.
incltding but not linited
to the styrene devolatizer unit
and
stvrene
recovery unit.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
___________________________________
Section
211.3690
Maxinurt
Theoretical
Emissions
“Maximum theoretical emissions” means the quantity of volatile
organic material emissions that theoreticaLly could be emitted
a stationary source before add—on controls based on the design
capacity or paxinu~nproduction capacity Qf the source ~nd 8760
hours per year.
The design capacity or maximum oroduction
capacity i1~cludesuse of coating(s~or ink(s~with the highest
volatile organic raterial content actually used in practice by
the source.
Drovided,
however, the Agency shall, when
appropriate, and upon request by the permit applicant,
limit the
“maximum theoretical emissions”
of
a source by the
imposition of
conditions
in
a
federally
enforceable
operating
permit
for
such
source.
Such
conditions
shall
not
be
ir~consistent
with
requirements
of
the
Clean
Air
Act,
as
amended,
or any applicable
requirements
established
by
the
Board.
Such
conditions
shall
be
established
in place of design capacity or maxlmun production
capacity in calculating the “maximum theoretical emissions” for
such source and
flay include, among other things, the
establishment of production limitations, caoac~tylimitations,
or
limitations
on
the
volatile
organic
material
content
of
coatings
or
inks,
or
the
hours
of
operation
of
any emission unit.
or
a
coiiibination
of
any
such
limitations.
Production
Cr
capacity
limitations
shall
be
established
on
a
basis
of
no
1on~icr than
one
nonth
except
in
those
cases
where
a
limit
spanning
a
lcnger
period
of
time
is
appropriata.
In
such
cases,
a
limit
or
limitation
must
not
exceed
an
annual
limit
rclled
on
a
basis
of

78
at most
a month: that is.
for example.
a monthly production or a
capacity level must be detennined for each parameter subject to
a
production or capacity limitation and added to the eleven prior
monthly levels for monthly comparison with the annual
limit.
Any
production or capacity limitations shall be verified through
appropriate recgrdkeeoinq.
(Board
Note:
The
USEPA
may
deem
operating
permits
which
do
not
canton
to
the
operating
permit
program
requirements
and
the
requirements
of
USEPA’S
underlying
regulations,
including
the
reauirement
that
liMtations
ba
aupntjfiable
and
enforceable
as
a
practical
i.atter.
not
“federally
enforceable.”)
(Source:
Added
at
111.
Beg.
effective
)
Section 211.3710
Metal Furniture
“Metal
furniture”
means
a
furniture
piece
5ncludinp.
btt
not
limited
tc.
tables,
chairs,
waste
baskets,
beds,
desks,
lockers.
benches, shelving, file cabinets,
lamps,
and room dividers made
in
whole
Cr
jfl
nart
of
metal.
(Source:
Added
at
—-
Ill. Req.
,
effective
)
Section 211.3730
Metal Furniture Coating
“Metal furniture coating” Leans any protective,
decorative or
-
functional coating applied onto the surface
of
any
metal
furr,jture
or
any
metal part which will
be
assembled
with
other
metal,
wood,
fabric,
plastic
or
glass
parts
to
form
metal
furr,jture.
However,
an
adhesive
is
not
4
metal
furniture
coating~
(Source:
Added
at
Ill. Rag.
,
effective
)
section
211.3750
Metal
Fun’.iture
Coating
Line
“Metal
furniture
coating
line”
means
a
coating
line
jnwhjchany
protective,
decorative,
or
functional
coating
as
applied
onto
the
surf~ce of any metal furniture or any
metal
part
which
will
b~
~ssembjed
with
other
metal,
wood1_Xabric
or
glass
parts
to
fCrm
metal
furniture.
Hcwever,
application
of
an
adhesive
is
not
a
iaeta3. furniture coating line Cr
par
pf
a metal furniture coating
(source:
Added at
Ill.
Req.
_____
,
effective
___________________________________________ )
Section
21:.3770
Metallic
Shoe—Type
SeaJ.

79
“Metallic shoe—type
seal” means
a primary or secondary seal
constnc~edof itptal sheets
(shoes) which ar
form a rino.
springs or levers which attach
e joined tog
the shoes to
ether
the
to
floating roof and
l~ioldthe shoes against the
coated membrane which
is susoended from the
tank wall,
shoes to the
and a
floating
roof.
(Source:
Added at
—)
Ill.
Req.
_____
effective
Section
211.3790
Miscellaneous Fabricated Product
Manufacturing Process
“Mjscellaneous fabricated product manufacturing process” means:
A manufacturing process involving one or more of the
following applications,
including any drying and
of formulations, and capable of emitting VON:
Adhesives to
f&b1. ~cnte p. pssp~bleports o~
products
Asphalt solutioms
to~aper_or
fiberh~ard;
Asphalt to paper or felt;
CoatLngs or dye to leather;
Coatings to nlastic:
Coatings
to rubber or glass:
Disinfectant rnateria 1 to manufactured
items;
Plastic
foam
scrap or “fluff”
Iron the manufacture
of roam containers mid packaging raterial to form
resin pellets
Resin solttions to fiber substances;
Rubber solutions to
Viscose solutions
I’
molds:
or food
or
casings.
The storage and handling of formulations associated
with the process described above and the use and
handling of organ~clipuiØs and other substances
Toy
clean—up
operations associated with the process
described in
this
definition
would
be
Included.
(Source:
Added at
111. keg.
_____
effective
curing

80
Section 211.3310
Miscellaneous Formulation ManufacturinQ
Process
“Miscellaneous formulation nnufacturing process” means:
A
manufacturing
process
which
compounds
one
or
more
of
the
following
and
is
capable
cf
emitting
VOM:
Adhesives;
Asphalt solutions:
Caulks,
sealants.
or waterproofing agents;
Coatings, other than paint and ink;
Concrete curing compounds;
Dyes;
Friction materials and compounds;
Resin solutions
Rubber
solutions;
or
Viscose solutions.
The storage and handlinu of formulations associated
with the process described above,
and the use and
handling of organic liauids and other substances for
clean—up oyerations assoc~atedwith the process
described
in this definition would be included.
(Source:
Added at
___
Ill. Reg.
_____
,
effective
____________
__________________________________
)
Section 211.3830
Miscellaneous Metal Parts and Products
“Miscellaneous metai parts and products” for the purpose of
35
Ill.
Admu.
Code
215.
Subpart
F.
shall include farm machinery.
garden machinery,
small appliances,
commercial machinery.
industrial machinery1
fabricated retal products and any other
industrial category zn which fetal parts or products under the
Standard Industrial Classification Code for Halor Groups
33.
34.
35.
35.
37.
38 or 39 are coated,
with the cxception of the
following:
coating lines subiect to 35
Iii. Mm. Code 215.204 (a)
through
(1)
and
(Ic).
architectural coatinas, automobile or
light—duty truck refinishing,
the exterior of marine vessels and
the customized top coating of automobiles and trucks
if
production is less than thirty—five vehicles per day.

81
(Source:
Added at
Ill.
Reg.
_____
,
effective
________
Section 211.3850
Miscellaneous Metal
Parts and Products
Coptinc~
“Miscellaneous
purooses of
35
metal
Ill.
parts and
Adm.
Code
products coptinp’
neans.
for
218 and 219. any protective.
decorative or functional coatina applied onto the surface of
any
metal part or metal product, even
if attached to or combined with
a nonmetal part or product
~j
IncludjDg byt
nc’t limited to tinderbody aptj—chip
(e.g..
underbody plastisol) putompbi~e
and
light-duty truc:c
cQptings
ki
But not i~ç~.uding
the following co@tings which afe
~ubiect to separate regulations:
can coatings, coil
coatings, metal furniture coatings,
large apDliance
coatings, magnet wire coatings,
and prime coat.
primer
surfacer coat, topcoat and final revair coat for
automobile and light-duty trucks;
and
çj~
Not including the following coatings:
architectural
coatings, automobile or light-duty truck refinishing
coatings, coatings applied to the extprio~of iparine
vessel~.coatings applied to the exterior of a+rPlanes.
customized topcoat for autçimobiles and j~rucks if
croduction is less than thtrtv-fiv~vehicles per day,
and l4ah temperature aluminum coating applied to
diesel—electric locomotives
in Cook County.
(Source:
Added at
___
Ill. Reg.
_____,
effective
_______________
___________________________________________ )
Section 211.3870
Miscellaneous Metal Parts or Products Coating
Line
“Miscellaneous
metal
oarts
or
oroducts
coating
line”
means,
for
purposes of
35 Ill.
Adrn. Code 218 and 219,
a coating line
in
which any protective,
decorative.
or functional coatIng
~S
applied onto the surface of any metal part or metal product,
even
if attached to or combined with
a nonmetal part or product
~j
Including but not lir.ited to underbody anti—chip
(e.g.,
underbody plastisol) auto~nobileand light—duty truck
coatings
~
But not including the following coatings which are
subiect
to sep~rateçe~ulations:
can coatings,
coil
coatings,
metal furniture coatings.
large appliance
coatings1
magnet wire coatings,
and prime
coat, primer

82
surfaceç coat.
tç?Pcoat and final reoflr coat for
automobile and light—duty trucks; and
çj~
Not including the following coatings:
architectural
coatings.
automobile or iignt—gurv
trucK
reIinisflin~
coatings,
coatings app’ied to the exterior of ijarine
vessels, coatings applied to the exterior cf airplanes,
customized topcoat for automobiles and trucks
if
production
is Less than thirty—five vehicles
per
day.
and high temcerature aluminum coating applied to
diesel—electric locomotives in Cook Caunty.
(Source:
Added at
Ill. Reg.
____—.
effective
-_______________
Secticn 211.3890
Miscellaneous Organic Cheitical Manuficturi~g
Process
~NisceJdaneous organic chemical ranufacturing process” means:
A manufacturing process which produces~by chemical
reaction, one or more of the following organic
compounds or mixtures of organic com~cundsand which
is
capable of emitting volatile organic Epterial
(VON):
Chemicals listed in Appendix A of 35
Ill. Adm.
Code
215.
218 or 219.
as applicable:
Chlorinated and sulfonated compounds;
Cosmetic, detergent,
soap, or surfactant
intermediaries or specialties and prodvcts;
Di.
psi
ii
cI_.tpj
to.
Food
additives~
Oil and petrolema product additives;
plasticizers:
Resins or polymers;
Rubber additives;
Sweeteners;
or
Varnishes.
The storage and handling of formulations associated
with the~prQcgssdescribe&above and the use and

83
handling of organic liuuids and other substances
for
cJ.epn-up oparpt~onpassociated with the process
described in this definition would be included.
(Source:
Added at
Ill.
Rag.
_____
effective
Section
211.3910
Mixina ODeration
“Mixing operation” means the operation
ingredients.
of which at
least one
is
a
of_combining
grain.
two
or
fore
(Source:
Added at
Ill. Req.
_____
effective
Section 211.3930
Nonitor
means tQ measure and record.
(Source:
Added at
___
Ill. Req.
_____
effective
Secticn 211.3970
Multiple Packac~eCoating
“Multiple uackaae ppptingM means a coating made from more than
one different ingredient which must be mixed prior to using and
has a limited Dot life due to Uia chemical reaction which occurs
upon mixing.
(Source:
Added
at
Ill. Reg.
,
effective
)
Section 211.3990
New Grain—Drying Operation
“New
grain—drying
operation”
means
any
grain—drying
operation
the
construction or modification pt which commenced on or after June
30.
1975.
(Source:
Added
at
Ill. Reg.
effective
)
Section 211.4010
New Grain—Handling Operation
“New
grain—handling
oneration~
means
any
grain—handling
operation
the
construction
or
modification
of
which
comiuenced
on
or
after
June
30.
1975.
(Source:
Added
at
Ill.
Req.
,
effective
)

84
Section 211.4030
Np
Detectable Volatile Organic Material
Emissions
“NQ detectable yplatile org~nicroatpria
emissions” weans
a
discharge
of volatile organic material into the atmosphere as
indicated by an instrument reading of less than 500 rpm above
background as determined in accordance with 40 CFR 60.485(c)
(incorporated by reference
in 35 Ill. Adm. Code 215.105.
218.112,
and 219.112~
(Source:
Added at
___
Ill. Reg.
_____
,
effective
________________-
___________________________________
)
Section 211.4050
Ion—contact Process Water Cooling Tower
“Non—contact process water cooling tower” means a towerlike
device in which water is cooled by contact with atmospheric air
and evaporation, where such water ha~been or will be used tor
cooling of a process stream where
‘tOM ~s wr~entw4thout
intentional direct contact of the cooling water and process
stream.
(Source:
Added at
___
Ill. Reg.
_____
,
effective
_________________
___________________________________________ )
Section 211.4070
offset
“Offset” means,
with resoect to printing,
use of
a blanket
cylinder to transfer ink from the plate cylinder to the surface
to be yrinted.
(Source:
Added at
___
Ill. Req.
_____
,
effective
________________
___________________________________
)
Section 211.4090
One Hundred Percent Acid
‘One hundred percent acid”
means.
with respect to sulfuric and
nitric acids,
acid with
a specific gravity of
l.820.5 at
300
C
in
the case of sulfuric acid and 1.4952 at
3p0
C
in the case of
nitric acid.
(Source:
Added at
___
Ill.
Req.
_____
effective
________________
___________________________________
)
section
211.4110
One—Turn
Storage
Space
“One—turn storage space” means that space used to store grain
with
a total
annual through—put not
in excess of the total bushel
storage of that space.
(Source:
Added at
Ill. Peg.
_____
effective
_______________

85
&ecticn 211.4130
opacity
“Opacity” means a condition which renders material partially or
wholly impervious to transmittance
of light and causes
obstruction
of an observer’s view.
For the purposes of these
r~aulations. the following ecuivalence between oDacity and
Ringplmanr shall be employed:
Opacity Percent
Ringplmpnn
.1Q
0.5
2.Q
IQ
3.5
IQ
1
Al
100
(Source:
Added
at
Ill. Req.
_____
,
effective
______________
Section 211.4150
Onague Stains
“Opacue
stains”
neans all stains that are not semi—transparent
Stains.
(Source:
Added at
___
ill. Req.
_____,
effective
_______________
)
Section 211.4170
Open Top Vanor Degreasing
~
top vapor degrepsing” means the batch process
of cleaning
and removing soils from surfaces
by condensing hot solvent vapor
on the colder metal
parts.
(Source:
Added at
Tfl.
Reg.
_____
,
effective
______________
___________________________________________ )
section 211.4190
Open—Ended Valve
~
valve”
Ileans any valve, except pressure relief
devices, having one side
of the valve
in cor.tact with process
fluid and one side open to the atmosphere,
either directly or
through open pjping.
(Source:
Added
at
___
II.
Reg.
_____,
effective
______________
section
211.4210
Operator
cf
a
Casoline
~ispensing
Operation
or
Operator
of
a GasoUns_Djspensirg_Facility

86
“OPerttor yf ~asyline dj.syensinci operation” or “Operator of
a
gasoline dispensing facility” meant any person who ~s the lessee
or
or operates, contz~oLsyr su~~rvises
p gasoline dispensing
operation or
a gasoline dispensing facility.
(Source:
Added at
Ill. Req.
_____,
effective
_______________
___________________________________________ )
Section 211.4230
Organic
Cornpour.d
“Organic compound” means any compound
of carbon,
excluding carbon
m~onoxide. carbcn dicxide. carbonic ~
metallic carbides
or
carbonates,
and ammcnium carbonate.
(Source;
Added
at
Ill.
Peg.
_____
,
effective
________________
___________________________________________ )
Section 211.4250
Organic Material and Organic Materials
~j
“Organic
materjalshl
means,
for
th~ purposes
of
Section
9.4
of the Act, any chemical compound of carbon,
including dili?ents and thinners which
are liguids at
standard conditions and which are used as dis~olvers.
viscosity reducers
Cr
cleaning
agents.
including
polychlorinated dibenzo-n—dioxins. polychiorinated
dibenzofurans
and
polynuclear
aromatic
hydrocarbons
but
exc1ud~ngmethane,
carbon monoxide, carbon dioxide.
carbonic acid, metallic carbonic acid,
metallic
carbide,
retallic
carbonates
and
ammoniun
carbonate
aze
not organic materials.
~
“Organic ~
means.
Lor the pIn-pose of
35
Ill.
Adm. Code 215.
218 and 219,
any chemical compound of
carbon including diluents and thinners which are
liquids at standard conditions and which are used as
dissolvers.
viscosity reducers,
or cleaning agents,
but
excluding methane,
carbon monoxide, carbon dioxide.
carbonic acid, metallic carbonic acid, metallic
carbide, metallic carbon~tes, and ammoniun carbonate.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______________
____________________________________________
)
Section 211.4270
Orcrpn~cVapor
“Organic vapor” means the gaseous phase of an organic material
or
a mixture of organic materials oresent in the atmosphere.
(Source:
Added
at
Ill.
Rag.
_____
,
offoctivc
_______________
___________________________________________ )

87
Section 211.4290
Oven
“Oven” means, with resDect to a coatIng line or printi~igline.
p
chamber within which heat
is used for
grie or more of the
following ~rposes:
dry,
bake. cure, or polymerize
a coating or
ink.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
________________
)
Section 211.4310
Overall Control
“Overall control” means the product of the capture efficiency and
the contro3
device efficiency.
(Source:
Added at
___
Ill.
Rog.
_____
,
effective
________________
__________________________________
)
SectiOn 211.4330
Overvarnish
“Overyarnish” means
a transparent coating applied directly over
ink or coatinri.
(Source:
Added at
___
Ill. Reg.
_____
,
effective
________________
)
Section 211.4350
Owner of p Gasoline Dispensing Operation or
Owner of a Gasoline Dispensing Facility
“Owner
of
a
gasoline
dispensing
operation”
or
“o~.mer
of
a
gasoline
djsnensir,p
facility”
means
any
person
who
has legal or
equitable
title
to
a
stationary
storage
tank
at
p
gasoline
dispensing operation.
(Source:
Added at
___
Ill. Reg.
_____
effective
________________
____________________________________________
)
Section 2114370
Owner or Operator
“Owner or onerator” means any person who owns, operates,
leases,
controls,
or supervises
p source,
an emission unit
or air
pollution control
equipment.
(Source:
Added
at
___
Ill. Reg.
_____
,
effective
_______________
Section 211.4390
Packaging Rotogravure Printing
“packaging rotogravure printing” means rotogravure crintira upon
paper,
paper board,
metal
foil,
plastic film,
and other
substrates, which are,
in subse~t1entoperations.
formed
ir.to
packaging products or labels for articles to be sold.

88
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______
__________________________________
)
Section 211.4410
PackagIng Rotogravure Printing Line
“Packaging rotoaravure printing line” means a rotogravure
Drinting line ~erformina packaging rotogravure printing.
(Source:
Added at
Ill. Req.
_____
effective
_______
__________________________________
)
Section 211,4430
Pail
“Pail” means any cylindrical shipping container of
1
to 12—gallon
capacity and constructed of 29—gauge and heavier n1ateria1~
(Source:
Added at
Ill. Req.
effective
)
Section 211.4450
paint Manufacturing Source or Paint
Manufacturing Plant
“Paint ranufacturing source” or “Paint manufacturing plant” means
source that fixes, blends. or compounds enamels,
lacquers.
sealers.
shellacs,
stains,
varnishes,
or pigmented surface
coatings.
(Source:
Added at
Ill. Rag.
effective
)
Section 211.4470
Paper
Coating
“Paper
coating”
means
any
protective,
decorative
or
functional
coating applied on paper,
plastic
fil9i.
or metallic
coil
to make
certain products.
including but
yiot liraited to adhesive tapes and
labels, book covers, post cards.
office copier paper. drafting
paoer. or pressure sensitive tao.ys.
For ourp1ses of
Ill. Adn.
Code 218 and 219.
paDer
coating
includes
coatings
applied
by
impregnation or saturation.
(Source:
Added at
Ill.
Peg.
,
effective
)
Section 211,4490
Paper Coating Line
Mopper
coating
line”
means
a
coating
line
in which any
protective1
decorative.
or
functional
coating
is
applied
on.
saturated
into.
or impregnated into paper, plastic film,
or
metallic foil to make certain Drcdupts, including but not Limited
to adhesive tapes and labels, bock covers, post cards,
office
copier paper,
drafting paper and pressure sensitive tapes.
For

purposes of 35 Ill.
Adm.
Code 218 and 219.
a paper coating line
includes saturation or impregnation.
(Source:
Added at
___
Ill. Reg.
_____
,
effective
_________________
Section 211.45:0
PartIculate Matter
“Particulate matter” means any sofld or limiid naterial,
other
than water, which exists
in finely divided form.
(Source:
Added at
___
Ill. Peg.
_____
,
effective
_______________
)
Section 211.4530
Parts
Per Million (Vplume~or PPM (Von
MPpt.ts
per million
(volume)” or “PPM (yol)” means
a volune/volurie
ratio which exores~esthe v?lumetric concentration
of gaseous
aj
contaminant
in a million unit v~lumneof gas.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
_______________
_____________________________
)
Section 211.4550
Person
“Person” means ~ny individual;
corporation; DartnershiD;
firm;
associatIon: trust; estate; public or
private
institution;
groups
stateLJ~unicipality;po’itical
subdivision of
a statej~~y
agency, department.
or instrumentality of the United States;
and
any officer,
agent,
or employee cf any of the above.
(Source;
Added
at
___
Ill. Reg.
_____
,
effective
_______________
___________________________________
)
Section 211.4590
petroleum
hPetroleumll means the crude oil renoved from the earth and the
oils derived
froit tar sands,
shale,
and coal.
(Source:
Added at
___
Ill.
Peg.
_____
,
effective
_______________
___________________________________
)
Section 211.4610
Petroleum Liquid
‘Petrcleumu liguid’
means cnide oil, condensate or any finished
Cr
intermediate product n~anufpcturedat
a ~etroleu~ refinery, but
not
including
Number
2
through
Number
6
fuel
oils
as
specified
in
ASTrI
D—396—69
(incorporated
by
reference
in
35
Ill.
Adra.
Code
218.112 and 219.112),
gas turbine fue
oils Numbers 2—CT through
4—~Pas specified in ASTN D—2880—71
(incorporated by reference
in
35 Ill. Ada.
code 216.112 and 219.112)
or diesel fuel oils

90
Nwthers 2—D and 4—D.
as specified in ASTM D—975—68
(incorporated
by referencej.jj.35
flj~
Adm.
Code
218.112
and
219.112).
(Source:
Aided
at
___
Ill.
Reg.
___
,
effective
_________
______
___________________________________________ )
Section
211,46~Q
Petroleum Refinery
“Petroleun refinery” means any source engaged in producing
gasoline, kerosene, distillate fuel oils,
residual ftel oils,
lubricants.
or
other
croducts
through
distillation
of
petroleum,
or
through
rec?istillation.
cracking.
or
reforming of unfinished
petroleum derivatives.
(Source:
Added at
___
Ill. Beg.
_____
effective
________________-
Section 211.4650
Pharnaceutical
“Pharmaceutical”
uteans any compound or mixture,
other than food.
used
in the prevention, diagnosis,
alleviation,
treatment,
or
cure of disease in human and animal.
(Source:
Added
at
___
Ill.
Peg.
_____,
effective
_______________
___________________________________
)
Section 211.4670
Pharmaceutical Coating Operation
“Pharmaceutical coatinq operation” means
p
device in which a
coating is applied to
a Dharulaceuticpl.
including air drying or
curin~of the coatinci.
(Source:
Added at
___
Ill. Beg.
_____
,
effective
________________
___________________________________
)
Section 211.4690
Pnctochemically Reactive Material
“photochenaically reactive material” means any Organic material
with an ag~regpteof more than
20 percent cf
its total volume
composed of the chemical compounds classified below
Cr
the
composition of which exceeds any of the following individual
percentage composition
limitations.
Whenever any Phctochenicaily
reactive material or any constituent of any organic iraterial may
be classified from its chemical structure into more than one
of
the above groups of organic materials.
~t shall be ccnsidered as
a member
of the most reactive group,
that
is.
the group having
the least allowable percent of the total organic naterials.
A combination of hydrocarbons,
alcohDls.
aldehyc~es,
esters,
ethers or ketones having an olefinic or
cyclo—olefinic types
of unsaturation:
5 percent.
This

91
deçip~tiondoes not apply to perchioroethylene or
trichicroethylene.
A combination of aromatic compounds with eight or more
carbon atoms
to the molecule exce~tethylbenzene:
B
tercent.
A combination of ethylbenzene. ketones having branched
hydrocarbon
s
tru
ctures or toluene:
20 percent.
(Source:
Added at
1)1. Reg.
_____
,
effective
)
Section 211.4710
Pigmented Coatings
“Pimnented coatingsi! means opaaue coatings containing binders and
colored pigments which are formulated to conceal the wood surface
either as an undercoat or topcoat.
(Source:
Added
at
___
Ill. Req.
_____
effective
_______________
Section
211.4730
Plant
“Plant” means,
for purposes other than 35
Iii. Mm.
Code 215.
218
and 219. all of the pollutant—emitting activities which belong to
the pa~neindustrial grouping,
are located
on one or more
contiguous or adiacent procerties.
and are under the control
of
the same person
(or persons under commoQcontrol),
except the
activities of any marine vessel.
Pollutant—enitti~qactivities
shall be considered as o~rtof the same industrial grouping
if
they belong to the sane malor group
(i.e..
which have the same
two—digit code)
as described
ir. the “Standard Industrial
Classific4tion Manual1” 1987 (incorDorated by reference
in
35
Ill. Adm, Code 218.i12 and 219.112).
(Source:
Added at
Ill. Reg.
-____
,
effective
_______________
Section 211.4750
Plasticizers
“Plasticizers” means substances added to
a polymer composition to
soften and add flexibility to the product.
(Source:
Added at
Ill. Rag.
_____
,
effective
_______
)
Section 211.4770
____
“FM-W” means particulate matter with an aerodynamic diameter
less than or equal
to
a nominal
10 znjcroneters.
as IneasuredS
the applicable test methods specified ~v rule.
Ambient air

92
concentrations for PM—b
are usually expressed
in micrograms per
cutic meter
(up/rn3)
(Source:
Added
at
___
Ill.
Reg.
_____
effective
_______________
__________________________________
)
Section 211.4790
Pneuri~atic.Rubber Tire Manufacture
“Pneumatic rubber tire manufacture” means the riroduction
c’t
pneumatic rubber tires with
a bead diameter up to but not
incluaina 20.0 inches and cross secticn dirension up to
12.8
inches.
but not includina specialty tires for antinue or other
vehicles when oroduced on eauioment secarate from normal
produ?tion lines for passenger or truck type tires.
(Source:
Added at
Ill. Req.
-____
,
effective
_______________
section 211.4810
Polybasic Organic Acid Partial Oxidation
Manufacturing Process
Mpoly~slc
organic
acid
partial
oxidation
manufacturing
process”
means any process involving partiaL oxidation of hydrocarbons
with air to manufacture nolybasic acids
or their anhydrides.
such
as maleic anhydride.
phthalic anhydride.
terephthalic acid.
jsophthaiic acid.
trimelletic anhydride.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
$ection
211.4870
Polystyrene
Plant
“Polystyrene plant” means any collection of prccess units and
associated storage facilities
at
a source engaged
it using
styrene to manufacture polystyrene resin.
(Source:
Added at
Ill. Reg.
_____
,
effective
________________
___________________________________________)
Section 211.4890
Polystyrene Resin
“Polystyrene
polymer
and
resin”
ieans
a
additives
which
substance
consisting
is
manufactured
at
a
of
styrene
oolystyrene
plant.
(Source:
Added at
Ill. Reg.
_____
effective
__________________________________
)

93
Section 211.492M
Portable Grain—Handling Eauii~ment
°Portablegrain—handling ecuigment”
(Source:
Added at
Iii.
Rag.
rJg~J,p1aa4,
1k! I•)
LtD.
S
(excluding tortable
c-rain dryers)
that is designed and maintained
to be movable primarily for use
in a non—continuous operat:on for
loading and unloading one—turn storage space and
is not
physically connected to the grain elevator, provided that the
manufacturer’s rated capacity of the eauionient
does not exceed
10.000 bushels per hour.
(Source:
Added at
___
Ill. Reg.
_____,
effective
_________________
___________________________________________)
section 211.4930
Portland Cement Manufacturing Process
Emission Source
“Portland cement manufacturing process emission source” means any
items of
process eguipment or manufacturing nrocesses used
in or
associated with the production of ‘oort1~ndcement,
inc’tuding,
but
not limited to.
a kiln1
clinker cooler
raw mill
system,
finish
m~1
¶vstem.
raw material dryer,
material storage bin or system.
naterial conveyor belt or other transfer system,
material
conveyor belt transfer point, bagging operation,
bulk unloading
station.
Cr bulk loading station.
_____
effective
________________
_________________
Cement Process or Portland
Plant
process” or “Portland cement nan~ifacturing
plant”
means
any facility or plant manufacturing portland cenent
by either the wet or dry process.
(Source:
Added
at
___
Ill.
Reg.
_____
,
effective
_______________
____________________________________________ )
Section 211.4990
Powar Driven Fastener Coatin~
“power driven fastener ccating” reans
the coatin~of
nail.
sta~~fe.brad ~nd çinish nail fasteners where such fasteners are
fabricated ~rot wire or rod çf O.O?54
inch diarnet~ror greater.
where such rasteners are bonded into coils
or strjps~such coils
and strips containing
a number
of such fasteners, which fasteners
are manufactured for use
in pcwer tools, and which fasteners must
conform with
fcrrnal
standards for specific uses estab1ished~y
various federal and national crganizaticns including
Specification FF—N-105b of the General Services Administration
dated August 23.
1977
(does not include any later arendments or
editions; U.S. Army Armament Research and Development Command.
Attn:
DRDAR—TST. Rock
Island.
IL 61201)
Bulletin UM—25d
ot the
Section 211.4950
“Portland cement
Portland
Manufacturing
Cement
Federa.

94
U.S. Department of Housing and Urban Develoument
Federal
Housing Administration dated Sectenber
5.
1973
(does not include
any later amendments or editions: Department of HUD.
547
W.
Jackson Blvd.. Room
ioos.
Chicago,
IL 60606).
and the Model
Building Code
of the Council
of Airterican Building Offipials.
and
similar standards.
For the purposes of this definitiori~tKe
terms “brad” and “finish nail” refer to
single leg fasteners
fabricated in the same manner as staples.
The application of
coatings to staple,
brad, and finish nail fasteners may be
asso~iatedwith the incremental rotting of
cyclic or repetitious manner
(incremental
such fasteners
in
a
fabrication)
or with
the forming of strips
of such fasteners as a unit from
a band of
wires
~unit fabrication).
(Source:
Added at
___
Ill. Rag.
____
,
effective
_______________
___________________________________________)
Section 211.5030
Pressure Release
‘Pressure release” means the emission of materials resulting from
system pressure being greater than set pressure of the pressure
relief device.
(Source:
Added
at
Ill. Req.
____
,
effective
_______________
___________________________________________)
Section
211.5050
Pressure
Tank
“Pressure tanlc” means
a
tanc
in which fluids are stor9d atg
pressure greater than atmosDheric pressure.
(Source:
Added
at
___
Ill. Reg.
_____,
effective
_______________
___________________________________________)
Section 211.5070
Prime Coat
“Prime coat” means the first of two or more coatings applied to
p
substrate
in
a multiple coat overation.
(Source:
Added
at
___
Ill. Reg.
_____
effective
___________________________________________ )
Section 211.5090
Primer Surfacer
Coat
“Primer surfacer coat” means ~ copting used to touch up areas on
the surface of automobile or light-duty truck bodies
not
adequately
covered
by
the
priir,e
coat before applicatior. of the
toD coat.
The prFiier surfacer coat
is applied between the prime
coat and topcoat.
An anti-chip coating applied to main body
parts
(e.g,.
rccker panels. bottom of doors and fenders,
and
leading e&a~ofroof)
is
a primer surfacer
coat.
The primer
referred to as ~ “guide cofl2~
sj.irfacer coat is ~t1so

95
(Source:
Added at
Ill. Reg.
_____
,
effective
—___________
Section 211.5110
Primer Surfacer ODeratj.op
“Primer surfacer operation” means the application area(s),
fiashoff area(s)
and oven(s)
that are used to apply and dry or
cure primer surfacer coat on
a single assembly line.
(Source:
Added at
___
Ill. Beg.
_____
effective
____________
Section 211.5130
Primers
“Primers” means any coatings formulated and applied to substrates
to provide
a firm bond between the substrate and subsequent
coats.
(Source:
Added at
Ill.
Reg.
effective
)
Section 211.5150
Printing
“Printing” means the application of words,
designs, pictures. Cr
other images to a substrate using
ink.
(Source:
Added
at
Ill.
Peg.
effective
)
Section 211.5170
Printing Line
“Printing line0 means an operation consisting of
a series
of one
or more roll printers and any associated roll coaters,
drying
areas,
and ovens wherein one or more coatings are applied,
dried.
and/or cured.
(Source:
Added
at
___
Ill.
Reg.
_____
effective
___________________________________________)
Section 211.5185
Prpcess
EITi$$joflSOUrc?
“Process emission source” means any stationary emission Source
other than
a
fuel combustion emission unit or an incinerator.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
_______________
___________________________________________ )
Section 211.5190
Process Emission Unit
“Process emission
‘unit” r.eans any staticnarv emission unit other
than a
fuel conthustionemjssJ,cji~njtor anj.nc:nerator.

96
(Source:
Added
at
Ill. Reg.
_____
,
effective
______________
)
Section 211.5210
Process Unit
“Process unit” peans eauio~ientand corponents assembled
to
troduce.
as interrediate
or final products. one or more
chemicals.
A process unit can operate independently if
supplied
with sufficient feed or raw materials ana sufficient storage
facilities for the product.
For purDoses of subpart 0 of
Parts
215. 218 and 219.
a Drocess unit must produce one or more of the
chemica’s listed
in Atoendiic A of 35
ill. Adn.
code 215,
218
or
219.
as applicable.
(Source:
Added at
Ill.
Reg.
_____
,
effective
__________
__________________________________
)
Section 211.5230
Process Unit Shutdown
“Process unit shutdown” means
a work practice or oDerational
procedure that stops production Iron
a process unit
or
part
oC~
process unit.
An unscheduled work practice or operational
orocedure that
StQpS
production from a process unit o~
part
of
a
process unit for less than 24 hours
is not a process
unit.
sln4tdown.
The ~zseof spare ecpiip~entand conoonents ~an4
tecimically feasible bvDassing of
eauiprrtent and components
without stqpping production is not a process unit shutdosm.
(Source:
Added at
Ill. Rag.
_____,
effective
______________
Section 211.5250
Process Weight Rate
“Process weight rate” means the actual wejgh~or engifle~ring
apprcxjtoation thereof 01 All materials except liquid and gaseous
fuels and combustion air introduced into any process per hour.
For a cyclical
cr
batch operation1 the process weight rate shall
be determined
by dividing such actual weight or engineering
apprcximation thereot by the number of hgurs of operation
excluding any tjwe durin~which the equipment
is idle.
For
continuous processes, the process weight rate shall be determined
by dividing sysh actual weight or engineering approximation
thereof by the number of hours in one complete operation.
excluding any tine during which the equipment is idle.
(Source:
Added at
Ill.
Rag.
_____
,
effective
______________
___________________________________________)
Section
211.5270
Production
Equipment
Exhaust
System
“Production eauipment exhaust system” reans
a system for
collecting and directing
into the atmosphere emissions
of

97
volatile organic material from reactors, centrifuges, and other
process emission units.
(Source:
Added
at
___
Ill. Peg.
_____
effective
_____________
___________________________________________)
Section 211.5310
Publication Rotoaravure Printinn Line
“Publication
rotogravure
printing line” means
a
rotogravure
printing line printing upon p@per which
IS subseQuently toned
into books.
mDgazines.
catalogues, brochures. directories.
newspaper suonlements or other types of non—Dackaginci printed
materials.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_________________
___________________________________________ )
Section 211.5330
Purged Process Fluid
“Purged process fluid” means liquid or vapor from
a process unit
that contains ‘volatile organic material and that results from
flushing or cleaning the sample line(s)
of
a trocess unit so that
an uncontaminated sample may then be taken for testing
~r
analysis.
(Source:
Added at
Ill.
Reg.
-~
_,
effective
_______________
— ________
)
Section 211.5350
Reactor
“Reactor” means a
vat,
vessel.
or other device
in which chemical
reactions take place.
(Source:
Added at
___
Ill.
Req.
_____
,
effective
_________________
_______
)
Section 211.5370
Reasonably Available Control Technology
(RACT)
“Reasonably available control technology
(RACT)” means the lowest
emission limitation that
an emission unit is cappble
of meeting
by the application of control technology that is reasonably
available considering technological and economic feasibility.
(Source:
Added at
Ill.
Reg.
_____
,
effective
_______________
)
Section 21:.541o
Refiner
“Refiner” means any person w~)oowns,
leases,
operates, controls.
or supervises
a refinery~

(Source:
Added
at
Lii.
keg.
98
effective
Section 211.54a0
Refinerv Fuel Gas
(Source:
Added
at
__________________________________________)
Ill.
Req.
_____
effective
Section 211.5450
Refinerv Fuel Gas System
“Refinery fuel gas system” means
a system £asollection
of
refinery fuel gas including, but
collecting tail gas from various
not 2imite~so.
prQcess units,
pjp~.ng
mixing
for
drums and
cpJ3trols,
and distribution piping.
(Source:
Added
at
Ill. Reg.
_____
effective
~çtion_211.5470
Refinery Unit or Refinery Process Unit
unit”
or “Refinerx
(Source:
Added
at
Ill. Rag.
_____
effective
Section 211.5490
Refrigerated Condenser
“Refrigerated condenser” means
a surface condenser
in which the
coolant supplied to the condenser has been cooled by
a u~echanical
device,
other than by
a cooling tower or ev~pprativespray
cooling, such
as refrigeration unit or steam chiller unit.
(Source:
Added
at
__________________________________________)
Ill.
Req.
_____
effective
Section 211.5510
Reia Vapor Pressure
“Reid ya~orpressure” means the absolute yaocr pressure of
volatile crude oil and volatile nonviscous Detroleum liauids
except liquified petroleum gases
as determined by the method
referenced
in the Section where the tejm
is used
or by ASTM
D323—89
(if not referenced
in the Section where the term
is
Code 218.112 and
qas.
“Refinery fuel gas” means any gas which
is
aenerated
petroleum refinery process unit and which
is conbusted at the
refinery. including any ~aseous mixture of natural gas and fuel
“Refinerv
hydrocarbons.
eciiithinnt whichare
p part of &_basic process operation such
distillation. hvdrotreatina.
cracking.
or reforming of
process init~ineaasa set_o~
as
used)
.
incorporated by reference
ii’.
35
Ill.
Adut,
219.112.

(Source:
Added
at
_________________________________
)
Ill. Reg.
99
_____
effective
Section 211.5550
Retair Coat
“Repair coat” means, with res~octto coating wood furn:ture.
coatings used to correct imperfections or damage to furniture
surface.
(Source:
Added
at
Ill.
Rag.
_____
effective
S~~ticn_21l.
5570
Repaired
“Repaired” ~1eans.for the purpose of Subpart
0 cf 35
Ill. Adm.
Code 215.
218 and 219.
that ecajigment or a component has been
adjusted.
or otherwise altered,
to eliminate
a
leak.
(Source:
Added at
iii.
Beg.
_____
effective
Section 211.5590
Residual Fuel Oil
“Residual fuel oil” means
fuel oils of arade No.
4.
5 and
6
as
specified in detailed reauirenents for fuel oils ASTM
D—396—6
(1971)
incornorated
by referen
Ca
in
35 Ill.
Adrn.
Code
218. 112 and
219.112.
(Source:
Added at
ill. Req.
,
effective
Section 211.5610
Restricted Area
“Restrthted
area” means the area within the boundaries
of any
llmunicipplityll as defined
in the Illinois Municipal
Code. plus
p
zone extending one mile beyond the boundaries of any such
runicipality having
a population of
1000 or more according to the
latest
federal
census.
(Source:
Added at
Ill. Reg.
effective
)
Section 211.5630
Retail Outlet
“Retail outlet” means any gasoline dispensing oneration at which
gasoline is sold or offered for sale for use
in rioter vehicles.
(Source:
Added
at
Ill. Beg.
_____
effective
)

100
section 211.5650
Ringelmann Chart
“Rinczelinann chpi-t”
neans
the chart oublished and described in the
Bureau of Nines.
U.S.
Department of
Interior.
Intoriiation
Circular 8333
(Revision of 1C7718)
Nay
1,
1967.
or any adaptation
thereof which has been approved by the Agency.
(Source:
Added at
111. Reg.
,
effective
)
Section 211.5670
Roadway
“Roadway” means any street. highway,
road,
alley,
sidewalk.
parking lDt.
airport, rail bed or terminal.
bikeway. pedestrian
mall Cr other structure used for transportation purposes.
(Source:
Added at
Ill. Beg.
-.
-
,
effective
—_______
~)
Section 211.5690
Roll Copter
“Roll coater” means an apparatus used
for
roll coating.
(Source:
Added
at
Ill.
Req.
,
effective
)
Section 211.5710
Roll Coating
“Roll coating” means
a method of applyinc~a coating to
a moving
substrate by means of rotating hard rubber. elastomeric or tietal
rolls.
(Source:
Added
at
Ill. Rag.
,
effective
)
Section 211.5730
Roll Printer
“Roll printer” neans an apparatus used for roll printing.
(Source:
Added at
Ill. Beg.
,
effective
Section 211.5750
Roll Printing
“Roll printing” means the method of printing by m~r1s
ot
a
series
of rolls, usually of hard rubbe~,or metal,
each with only partial
coverage.
(Source:
Added
at
Ill.
Rag.
_____
,
effective

101
section 211.5770
Rotogravure Printing
“Rotoorpvure printing” means roll printing in which the nattern
to be aDolied is recessed
in the roll relative to the non—image
area.
(Source:
Added at
Ill. Reg.
_____,
effective
_____________—-
__________________________________
)
Section 211.5790
Rotogravure Printing Line
“Rotogravure printing line” means
p printing line performing
rotoqravure printing.
(Source:
Added at
Ill.
Beg.
_____
,
effective
_______________
Section 211.5810
safety Relief Valve
“Safety relief valve” means a valve which
is normally closed and
which
js designed to open in order to relieve excessive pressures
within a vessel or pipe.
(Source:
Added at
___
Ill.
Reg.
____,
effective
_______________
___________________________________________)
Section 211.5830
Sandblasting
“Sandblasting” means the use of
a mixture of sand and air at high
pressures for cleaning and/or polishing any type
of surface.
(Source:
Added
at
Ill. Req.
_____,
effective
_______________
___________________________________________)
Section 211.5850
sanding Sealers
“Sanding scalers” means any coatinas fornulated for and applied
to bare wood for sanding and to seal the wood for subsequent
applicaticn of varnish.
To be considered
a sanding scaler
a
coating must be clearly labelled as
such.
(Source:
Added
at
Ill. Req.
_____
,
effective
_______________
___________________________________________)
Section 211.5870
Screening
“Screening” neans separating tatgrial according to size by
pressing undecsizpd material through one or more ruesh surfaces
(screens)
in series,
and retaining oversized material o~the mesh
surfaces
(screens)

102
(Source:
Added at
Ill.
Beg.
_____
,
effective
________________
__________________________________
)
Section 211.5890
sealer
“sealer” ~fleans
a coating containing binders which seals wood
prior to the application of the subsequent coatings.
(Source:
Added at
Ill. Reg.
____,
effective
______________
Section 211.591D
Semi—TransDarent Stains
“Semi—transparent stains” means stains containing dyes or semi.—
tønsparent piqments which are forrmqlated to enhance wood graj~
a~ndchange the color of the surface but not to conceal the
~sxface, Including,
but not limited to.
sap stain,
toner,
flQp—grain raising stains, Dad stain.
or spatter stain.
(Source:
Added at
Ill.
Req.
_____
effective
_______________
________
)
Section 211.5930
Sensor
“Sensor” means
a device that measures a physical quantity or the
chanae in
a physical quantity such as temperature, pressure,
flow
rate.
PH.
or liquid level.
(Source:
Added
at
Ill. Beg.
____,
effective
______________
___________________________________________)
Section 211.5950
Set of Safety Relief Valves
“Set of safety relief valves” neans one or more safety relief
valves designed to open in grder to relieve excessive Dressures
in the same vessel
or pipe.
(Source:
Added
at
Ill.
fleg.
,
effective
_______________
__________________________________
)
Section 211.5970
Sheet Basecoat
“Sheet basecoat” means
a coating applied
to
metal
when
the
metal
is
in sheet forr to serve as either the exterior or interior of
a
can for either two—piece or three—piece cans.
(Source:
Added
at
Ill. Reg.
_____
,
effective
_______________
__________________________________
)

:03
Section 211.5990
Shotblasting
“Shotblasting” means the use of
a mixture of any metallic or
non—metallic substance and air at high pressures for cleaning
and/pr polishing any tvoe of surface.
(Source:
Added at
Ill. Reg.
_____
,
effective
_______________
___________________________________
)
Section 211.6010
Side—Seam Spray Coat
“Side—seam spray goat” means
p can coating applied to the seam of
a three—piece can.
(Source:
Added at
___
Ill.
Rog.
_____
,
effective
_________________
___________________________________________)
Section 211.6030
Smoke
“Broke” means small gas—borne particles resulting from incomplete
corbustion,
consisting predoilinately but not exclusively of
carbons
ash and other combustible material, that form
a visible
plume in the air.
(Source:
Added at
___
Ill. Rag.
_____,
effective
_______________
)
Section 211.6050
Smokeless Flare
“Smokeless
flaretr means
a combustion unit and the stack to which
it
is
affixed
in which organic material achieves combustion by
burning in the atmosphere such that the smoke
or
other
particulate matter emitted to the atmosphere from such combustion
does nct have an appearance density or shade darker that No.
1 of
the Ringler.ann Chart.
(Source:
~dded at
___
Ill.
Reg.
_____
,
effective
_______________
)
Section
211.6070
Solvent
‘1Solvent” means
a
liquid substance that is used to dissolve or
dilute another substance.
This term includes, but
is not limited
to organic materials used as dissolvers. viscosity reducers.
degreasing agents,
or cleaning agents.
(Source:
Added at
211.
Reg.
_____
,
effective
_______________
__________________________________
)

104
Section 211.6090
solvent Cleaning
“Solvent cleaning” means the process of cleaning soils
fror
surfaces by cold cleaning,
open
toD
vapDr degreasing,
or
convevorized degreasing.
(Source:
Added
at
Ill.
Rag.
_____,
effective
___________________________________________)
Section 211.6130
source
“Source’
means
any
stationary
source
(or
any
aroup
of
stationary
sources
that
~re
located
on
one
or
more
contiguous
or
~diacent
proøerties,
and
are
under
conan
control
of
the
same
person
or
yersons
under
commor,
control) belonging to
a single major
industrial
grDppjng.
For
the
purposes
of
defining
“source,”
a
statignary
source
or
group
of
stationary
sources
shall
b?
considered
part
of
a
single
industrial
aroupjng
it
all
of
the
pollutant
emitting
activities
at
such
source
or
group
of
sources
on
contiguous
Cr
adjacent
orovertv
belong
to
the
same
Nalor
Group
j~.e.. all have
the
same
two—digtt
code)
as
described
in
the
Standard Industrial Classification Manual,
1987 (incorporat~4by
refc~rencein 35JJJ. Mm.
Code 218.112 and 219.112).
(Source:
Added at
Ill. Reg.
_____
,
effective
__________________________________
)
Section 211.6150
Specialty High Gloss Catalyzed Coating
“Specialty
birth
gloss
catalyzed
coating”
means
commercial
contract finishing of material prepared for printers and
lithographers where the finishing tro~essuses a solvent—borne
coating. fonulated with
a catalyst,
in
a quantity of
no more
than 12,300 gallons/year as supplied, where the coating machines
are sheet fed and the coated sheets are brought to
a minimum
surface temperature of 1900
F.
and where the coated sheets are to
achieve the minimum specular reflectance
index of 65 measured at
a
60 degree angle with ~ gloss neter.
~Source: Added at
Ill.
Req.
,
effective
)
Section 211.6190 $pecaalty Soybean Crushing Source
“Specialty
soybean ejushinci sI?urc~’means any hexane extraction
soybean crushing eguipment using indirect steam heat in f~ashor
vapor desolventizers as the primary method
of desciventizing and
producing specialty solvent extracted soy flakes,
grits
or flour.
(Source:
Added
at
Ill.
Peg.
_____
,
effective
___________________________________________
)

105
Section 211.6210
Stlash Loading
“Splash loading” means
a
method of loading
a tank,
railroad tank
car, tank truck.
or trailer by use of other than
a submerged
loading nine.
(Source:
Added at
Ill. Reg.
_____,
effective
_______________
__________________________________
)
Section 211.6230
stack
“Stack”
means
a
flue
or
condu~t.
free—standing
with
exhaust
pojt
above
the
roof
of
the
bujlding
on
which
it
is
mounted,
by
which
air
contaminants
are
emitted
into
the
atmosphere.
(Source:
Added at
___
Ill.
Reg.
_____
effective
_______________--
_________)
Section 211.6270
standard Conditions
“Standard conditions”
means
a temperature of 70°Fand
a pressure
of 14.7 psia.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
___________________________________________)
Section 211,6290
standard Cubic Fogt
tscf)
“Standard
cubic
foot
(sof)”
means
the
vclume
of
one
cubic
foot
of
gas at standard conditions,
(Source:
Added at
___
Ill.
Peg.
_____,
effective
_______________
__________________________________
)
Section 2fl.6310
Start—Up
“Start—up” i~eansthe setting in operaticn of an emission unit for
any
purpose.
(Source:
Added at
Ill.
Beg.
_____
,
effective
_________________
___________________________________________)
Section 211.6330
Stationary Emission Source
“Stationary emission source” means an emission source which
is
not
self—propelled.
(Source:
Added
at
Ill.
Peg.
_____
effective
_______________
___________________________________________)

106
Section
211.6350
stationary
Erission
Unit
Wstationary emission ~
means an
eniissicn unit which
is not
se~f—propejled.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
____________
___________________________________
)
Section 211.6370
Stationary Source
~ reans any buildinu.
structure,
facility,
or
~1nwt7wnTs~i.iu
installation that emits or nay emit any air pollutant.
(Source:
Added at
Ill.
Peg.
_____
,
effective
____________
___________________________________
)
Section 211.6390
Stationary
Storage Tank
“Stationary storage
tanic’
eans
~)y
container
of
l1;uid
QgaS
which
is designed ap&gonstructed to remain at one site.
(Source:
Added
at
___
Ill.
Reg.
_____,
effective
____________
____________________________________________ )
Section 211.6410
storage Tank or Storage Vessel
“Storage tank or storage vessel” reans any tank,
reservoir or
container used for the storage of licuid or gaseous
material.
(Source:
Added
at
Ill.
Beg.
_____
,
effective
____________
___________________________________
)
Section 211.6430
Styrene Devolatilizer Unit
•‘Styrenp devolatilizer unit” neans eguinment Derforming the
function of separating unreacted stvrene monomer and other
volatile conponents
frorft Dolystyrene in
a vacuunt devolatilizer.
(Source:
Added
at
Ill. Reg.
_____
,
effective
______________
___________________________________
)
Section 211.6450
Styrene Recovery Unit
“Styrene recovery unit” means equipment performing
the function
of separating styrene monomer from other less volatile components
of the styrene devolatilizer unit’s output.
The separated
styrene nonomer may be reused as a
raw
material
in the
polystyrene plant.
(Source:
Added
at
Ill.
Beg.
_____
,
effective
________________
__________________________________

107
Section 211.6470
Submerged Loading Pipe
fl
“Submerged loading
pipe’!
means,
for purposes
of 35
Iii.
Adm.
Code 215.
any loading pipe the discharge opening
of which is entirely submerged when the liquid
level
is
6 inches above the bottom of the
t~r.c.
When applied to
a tank which is loaded from the side.
“submerged
loading t4~e”means
arty loading pipe the discharge of
which is entirely subme~qedwhen the liquid level
is 15
inches or two times the loading pipe diameter.
whichever
greater,
above
the
bottom of the
tank.
Th? deçinition shall also apply to any loading pipe
which is continuously submerged during loading
operations.
ki
“Submerged
loading
pipe”
means,
for
purposes
of
35
Ill.
Adm.
Code
218
and
219.
any
discharge
pipe
or
nozzle
which
meets
either
of
the
followina
conditions:
fl
Where
the
tank
is
filled
from
the
top,
the
end
of
the discharge pipe or nozzle must be totally
submerged when the ha-aid level
is
15 cm
(6 inj
above the bottom of the tank.
fl
Where the tank
is filled from the side,
the
disoharae
pipe
or nozzle must be totally submerged
when the liquid level
is 46 cm
(18
in,4 above the
bottom of the tank.
(Source:
Added
at
Ill. Reg.
_____,
effective
_______________
___________________________________
)
Section 211.6490
Substrate
“Substrate” means the surface onto which
a coating
is applied or
into which
a
coating
is impregnated.
(Source:
Added at
Ill.
Req.
_____
,
effective
________________
____________________________________________
)
Section
211.6510
Su1fur~c
Acid
Mist
“Sulfuric acid mist” means sulfuric acid mist as ireasured
according to the method specified
in 35 Ui. Adm. Code
214.101(b).
(Source:
Added at
Ill.
Peg.
_____
,
effective
_______________
___________________________________
)

108
Sectian 211.6530
Surface Condenser
“Surface
condenser”
means
a
device
which
removes
a
substance
from
a gas stream by reducing the temoerature of the stream,
without
direct contact between the coolant and the stream.
(Source:
Added at
___
Ill. Req.
_____
,
effective
_______________
section 211.5550
Synthetic Organic Chemical
or Polymer
Manufacturing Plant
“Synthetic organic chemical or polyner manufacturing plant”
means
a source
that
produces,
as intermediates or final products.
chemicals or polymers.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
_______________
____________________________________________ )
Section 211.6570
Tablet Coating Operation
“Tablet
coating
operation”
means
a
pharmaceutical
coating
operation in which tablets are coated.
(Source:
Added at
Ill.
Req.
_____
effective
_______________
____________________________________________)
Section 211.6590
Thirty Day Rolling Average
“Thirty day rDllin~
average”
~Tiepn$any value aritirnetically
averaged cver any consecutive thirty days.
Source:
Added
at
___
Ill.
Reg.
ffective
_______________
____________________________________________
)
Section
211.6610
Three—Piece
Can
“Three—piece can” means
p can whicI
is made from
a rectangular
sheet and two circular
ends.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
_________________
____________________________________________
)
Section 211.6670
Topccat
“Topcoat” means a ocating applied to
a substrate
in
a multiple
coat operation other than prime coat,
primer surfacer coat or
final repair coat.

(Source:
Added at
Ill. Beg.
,
effective
______________
___________________________________________)
Section
211.6590
Topcoat
Operation
“Topcoat operation” means the appljcatjcn are~fs)~jiash-off
area(s)
,
and
oven(s)
used
to
apply
and
dry
or
cure
the
topcoat
j~xceptfinal off—line repair) on automobile or light—duty truck
bodias or body parts pj~asin~gieass~bly_line.
(Source:
Added at
Ill.
Reg.
-.
,
effective
__________
Section 211.6730
Transfer Efficiency
“Transfer efficiency” weans
the
ratio
of
the amount of coating
solids deoosited onto
a part or product to the total arount of
cpptin~solids used,
during
a particular time period.
(Source:
Added at
Ill.
Req.
_____,
effective
_______________
___________________________________________)
Section
211.6750
Tread
End
Cerenting
“Tread end ceruenting” means the application of a solvent—based
cement to the tire
(Souroc:
Added at
Ill. Reg.
_____,
effective
______________
___________________________________________)
Sectior.
211.6770
True Vapor Pressure
“True
vapor
pressure”
means
the
equilibrium
partial
pt-ossurc
exerted by
a volatile organic
liguid as determined
in accordance
with
methods
described
in
American
Petroleum
institute
Bulletin
2517,
“EvapOration
Loss
From
Floating
Roof
Tanks.”
second
edition.
February
1980
(incorporated
by
reference
in
35
Ill.
Adm.
Code
218.112
and
219.112),
(Scurce:
Added
at
___
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
Section
211.6790
Turnaround
“Turnaround”
means1
with
respect
to
a
ref
in?ry
process
unit,
the
procethire
çf
pu~tin~
down
an
operating
rpfinerv
unit.
emptv4ng
gaseous
and
liguid
contents
to do insPel?tlon. maintenance and
repair
works
and
putting
the unit back intg production.
(Source:
Added at
Ill.
Rag.
_____
,
effective
_________________
___________________________________________)

Section 211.6B10
Two—Piece Can
“Two—piece can” means
a can that consists
of
p
body manufactured
i.e.,
drawn,
from
a single piece of metal and one top or end.
(Source:
Added at
___
Ill. Peg.
_____,
effective
________________
)
Section
211.6850
Undertread
Cementing
“Undertread
cementu,g”
means
the
application
of
a
solvent—based
cement
to
the
underside
of
a
tire
tread.
(Source:
Added
at
___
Ill. Rcg.
_____
,
effective
_______________
___________________________________________ )
Section 211.6370
unregulated Safety Relief Valve
“Unregulated
safety
relief
valve”
means
a
safety
relief
valve
which
cannot
be
actuated
by
a
means
other
than
high
pressure
in
the pipe or vessel which it protects.
(Source:
Added
at
___
Ill.
Beg.
_____,
effective
_________________
)
Section
211.6890
Vacuum
Producing
System
“Vacuum producing system” means any reciprocating,
rotary.
or
centrifugal blower or compressor or any
1et elector or device
that creates suction from a pressure below atmospheric and
discharges against a greater pressure.
(Source:
Added at
___
Ill.
Rag.
_____,
effective
_______________
___________________________________________)
Section 211.6910
Vacuum Service
“Vacuuiu
service”
means,
for
the
purpose
of
Subpart
0
of
this
35
Ill.
Adm.
Code
215.
218
and
219.
equipment
or
a
component
which
is
operating
at
an
internal
pressure
that
is
at
least
S
kPa
(0.71
psial
below
ambient
pressure.
(Source:
Added
at
Ill.
Reg.
_____,
effective
________________
__________________________________
)
Section
211.6930
valves
Not
Externally
Regulated
“Valves
not
externally
regulated”
means
valves
that
have
no
provisicn
for
external
adjustment
or
governance
during
their
operation,
such
as
in—line
chock

111
(Source:
Added
at
Ill. Req.
_____
,
effective
________________
___________________________________________)
Section
211.6550
Vapor
Balance
System
ItVapor
balance
system”
means
any
combination
cf
pipes
or
hoses
which
creates
a
closed
system
between
the
vapor
spaces
of
an
unloading
tank
and
a
receiving
tank
such
that
vapors
displaced
from
the
receiving
tank are transferred to the tank being
unlcaded.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
Section 211.6970
Vacor Collecticn System
“Vapor
collection
system”
ne~ns all
piping,
seals,
hoses.
connections.
pressuxe—vpcuunl
vents.
an~ other
components
between
the
gasoline
delivery
vessel
and
the
vppor
processing
unit
and/pr
the
storage
tanks
and
vapor
holder.
(Source:
Added
at
___
111.
Reg.
_____•
effective
____________--
Section
2fl.6990
Vapor
Control
System
“Vapor
control
system”
means
any
system
that
lirriit
or
prevents
release
to
the
atmosphere
of
organic
material
in
the
vapors
displaced
from
a
tank
during
the
transfer
of
gasoline
or
other
volatile
organic
liquid.
(Source:
Added
at
___
Ill.
Req.
_____
effective
_______________
___________________________________________)
Section
211.7010
Vapor—Nountep
Primary
Seal
“Vapor—mounted
pri~tary
seal’1
means
a
primary
seal
mounted
with
an
air
space
bounded
by
the
botton
of
the
primary
seal,
the
tank
wall,
the
liguid
surface
and
the
floating
roof.
(Source:
Added
at
Ill.
Reg.
_____,
effective
______________
______
)
Section
211.7030
Vapor
Recovery
Systeit
“Vapor
recovery
system”
means,
with
respect
to
a
storage
tank.
storing
a
volatile
organic
liquid.
a
vapor
gathering
system
capable
of
collecting
all
volatile
organic
material
(VON)
vapors
and
gases
discharged
from
the
storage
tank
and
p
vapor
dispcsal
system capable of 1~rocessingsuch VON vapors and gases so
as to
preventtheir emission to the_atnosphere.

112
(Source:
Added at
___
Ill.
Reg.
_____
effective
_______________
Section 211.7070
vinyl Coating
!iLirnO- coatjng” means~nyprotective, decorative or functional
coating or ink applied to vinyl
or urethane
or vinyl or urethane
coated fabric which is delivered to
a coating line or printing
line as
a roll, unwound ~nd coated as
a continuous substrate.
However.
a plastisol
is not a vinyl
coating.
(Source:
Added at
Ill. Reg.
_____
effective
_______________
___________________________________________)
Section 211.7090
vinyl Coating Line
“Vinyl
coating
line”
means
a
ccatinq
line
in
which
any
protective,
decorative
or
functional
coating
or
ink
is
applied
onto vinyl or urethane
or
vinyl
or
urethane
coated
fabric
which
is delivered
tc
a coating line or printing line as
a roll.
unwound and coated as a continuous substrate.
However.
aDolicaticn of
a ~lastiyoJ.to vinyl or urethane or vinyl
or
urethane coated fabric is not
a vinyl coating line or part of
a
vinyl coating line.
(Source:
Added
at
Ill.
Req.
_____
,
effective
_________________
___________________________________________ )
Section 211.7110
Volatile Organic Liquid
(VOL)
“Volatile organic licn4d
(VOL)” moans
any substance which is
liquid
at
storage
ccnditjpns
and
Which
contains
volatile
organic
material.
(Source:
Added at
___
Ill.
Reg.
_____
,
effective
_______________
___________________________________________)
Section 211.7130
Volatile Crganic Material Content (VOMC~
“VolatilG organic material content
(VONC)”
means,
for the purpose
of
35 Ill.
Adm.
Code 215,
the emissions of vciatile organic
rnaçerial
which
would result çron the exposure of
a coating.
printing
ink,
fountain
solution,
tire
spray,
dry
cleaning
waste
or other similar material to the air,
including any drying or
cur~ng
in the absence of any control equipment.
VOMQ is
typically expressed as kilogram
(kg) VON/liter
(lb VO~/gallon~of
coating Cr coating solids,
or kg VON/kg
(lb VOM/lb)
of coating
solids,
coating or material.
(Source:
Added at
Ill.
Req.
_____
,
effective
_______________
___________________________________________)

113
Section 211.7150
Volatile Organic Materipl
rVox)
or Volatile
Organic
Cornpour.d
(VOC~
“Volatile organic material (VOH~”or “Volatile organic compound
(VOC~”means
~nv
conoound of carbon,
excluding carbon monoxide,
carbon dioxide, caitonic acid, metallic carbides or carbonates.
and ammonjum carbonate, which participates in atluospheric
photochemical reactions.
a).
This incLudes any such organic coipcound other than the
following.
which have been determined to have
npg~igiblephotochentical reactivity:
Methane; ethane:
methviene chloride (dichlonpetJ~ane).
1,1,1—trichiorethane
Iroethyl
chloroform);
1,1,1—trichloro—2,2,2—trifluorocthane (CFC—l13)
trichlorofluorcrne?h~T~C-flT~
dichiorodifluoromethane
(CFC—12) : chiorodiflucromethane
(CFC—22) trifluoromethane
(FC—23); 1,2-dichloro
1,1,2,2—tetrafluprocthanc
~CFC—fl4)
cloropentafluoroethane (CFC—115);
1.1.1—trifluoro
2.2-dachioroethane (HCFC-123)
14,1.2—tetrafluorç.ethane (HFC—~4a)
;
1.1—~1?hloro
—fl~Moroett1ane ($çFC—141b)
1—chlorc
1. 1—difluoroethane
(HCFC—142b~
2—chloro—1.l,1.2—tetratluoroethane
(HCFC—124)
p~ptafluoroethane (HFC—125)
1.1.2.2—~etratluoroethane
HiFC—134)
~
(IFC—143a)
1,1—difluroethane
(HFC—152p1 : pnd perfluorocarbcn compounds which fall
into these c)~asses:
fl
Cyclic,
branched.
or linear, completely
fluorinated alkanes
fl
Cyclic,
branched,
or linear,
cornDletelv
Iluorinated ethers with no unsaturations:
fl
Cyclic,
branched,
or linear,
conpletely
fluorinated tertiary amines with no unsaturations:
ani
~
Sulfur containing pertlucrocarbons with nc
unsaturations and with sulfur bonds only to carbon
and
fluorine.
~).
For purposes
of determining VON emissions and
compliance with enissions iimits.
VUN waLl
De measured
by the test methods in the approved implementation nlan
or
40
CFR
Part
60, Appendix A,
incorPorated by
reference at
35
Ill. Adm.
Code
215.105.
~1~.ll’2.and
219.112,
as applicable
or by spurce—specitic test
methods which have been established pursuant to a
permit issued pursuant to a program approved or

114
promulgated under Title V of the Clean Air Act or under
40 CER Part
51, Subpart
I or Appendix S.
incoroorated
by reference at
35 IlL.
Adn.
Code 218.112 and 219.112
or under 40 CFR Part 52.21.
incorporated by reference
at 35 Ill.
Adm. Code 218.112 and 219.112.
as
applicable.
Where suchanflhod
also measures
co.oounds with negligible photochemical
react.jyj.t_y1
these negligibly—reactive comcounds nay be excluded as
VON if the atount of such compounds
is accurately
auantified,
and such exclusions
is apprcved by the
Agency.
gj~
As
a Precor,ditjon tc.exclucling these
negligibly—reactive compounds as VOM or at ~ny time
thereafter,
the
Agency
may require an owner or operator
to provide monitoring or testing methods and results
demonstrating, to the satisfaction of the Agency,
the
amount of negligibly—reactive compounds
in the source’s
emissions.
~j
The
USEPA
shall
not
be
bound
by
any
State
determination
as to appropriate methods for testing or monitoring
negligibly-reactive corpounds
if such determination
is
not reflected
in any of the test methods
in subsection
(b)
above.
(Source:
Added at
Ill.
Reg.
_____,
effective
_______________
___________________________________________)
Section 211.7170
volatile Petroleum Liquid
“Volatile
petroleum
liquid”
means
any~petroleum
liquid
with
a
true vapor pressure that
is greater than 1.5 psia
178 millimeters
of mercury)
at standard conditions.
(Source:
Added at
Ill.
Reg.
effective
)
Section 211.7190
wash Coat
“Wash
coat”
means
a
coating
containing
binders
which
seals
wood
surfaces, prevents undesired staining, and controls penetration.
(Source:
Added at
Ill.
Reg.
_____
effective
_____________
___________________________________________)
Section 211.7210
Wa9tewater
(Oil/Water)
Separator
“Wastewater
(oil/water)
separator” means any device or piece of
eqmp,i,ent which utilizes the difference
in density between oil
and water
to remove oil and associated chenicals from water. or

115
any device,
such as
a flocculation tank or
a clarifier,
which
removes
petroleum
derived
compounds
from
waste
water.
(Source:
Added at
Ill. Reg.
_____
,
effective
_______________
___________________________________
)
Section
211.7230
Weak
Nitric
Acid
Manufacturing
Process
“Weak nitric acid manufacturing process” ~ueansany atid producing
facility nDnufacturing nitric acid with
a concentration of less
than 70 tercent
by
weight.
(Source:
Added
at
___
Ill.
Rag.
_____
,
effective
________________
)
Section
211.7250
web
“Web”
uieans
a
substrate
which
is
coated
or
printed
as
a
continuous substrate after being unrolled from the roll
in which
the substrate is delivered to
p line.
(Source:
Added at
___
Ill. Rag.
_____,
effective
_______________
___________________________________
)
Section 211.7270
Wholesale Purchase
Consumer
“Wholegain r,urchase
consumer” means any person or orppni?ption
that
turchases
or
obtains
gasoline
from
a
supplier
for
ultimate
consu,iptipn or u~ein aotor vehicles and receives delivery of
gasoline into
a storage tank with
a capacity
ot at least 2082
Liters
(550 gallcnsl owned and controlled by that person.
(Source:
Added at
___
fli. Req.
_____
effective
_______________
section_aLL7293
Wood
Furniture
“Wood furniture” means room furnishings including cabinets
(kitchen.
batt~. and vanity).
tattles,
chairs,
beds,
sofas.
shutters. ~rt nbiects, wood panelina.-wncd floori.ncz.
and any
other coated furnishings made of wood, wood composition.
or
fabricated wood materials.
(Source:
Added
at
Ill.
Reg.
_____
effective
____________
____________________________________________
)
Section 211.7fl0
Wood Furniture
Coatii,g
“Wood furniture coating” Deans any protective,
decorative or
functional coating applied to wood
furniture
or wood furniture
parts.

116
(Source:
Added at
Ill. Reg.
_____
,
effective
__________________________________
)
Secticn
211.7330
wood
Furniture
Coatina
Line
“Wood
furniture
coating
trotective.
decorative,
line”
means
a
or functional
coating
coating
line
in which
is anDlied to
any
wood
furniture
or
wood
furniture
Darts.
(Source~
Amended
at
___
Ill.
Reg.
______,
effective
Section
211.7353
Woodworking
“Wosdijorking”
means
the
shaping,
sawing.
grinding,
smoothing.
~o1ishin~
and
iiakin~i into
products
of
any
form
or
shape
of
wood.
(Source:
Added
at
Ill.
Reg.
_____
,
effective
_____________

117
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE
B:
AIR POLLUTION
CHAPTER I:
POLLUTION CONTROL BOARD
SUBCHAPTER
c:
EMISSIONS STANDARDS
AND
LIMITATIONS
FOR STATIONARY SOURCES
PART 218
ORGANIC MATERIAL EMISSION STANDARDS
AND
LIMITATIONS FOR THE
CHICAGO AREA
SUBPART A:
GENERAL PROVISIONS
Section
218.100
218.101
218.102
218.103
218. 104
218.105
218. 106
218.107
218.108
218.109
218.110
218.111
218.112
Section
218. 181
218.182
218.183
Introduction
Clean-up and Disposal OpcrationsSavings Clause
Abbreviations and Conversion Factors
Applicability
Definitions
Test Methods and Procedures
Compliance Dates
Operation of Afterburners
Exemptions, Variations, and Alternative Means of Control
or Compliance Determinations
Vapor Pressure of Volatile Organic Liquids
Vapor Pressure of Organic Material or Solvent
Vapor Pressure of Volatile Organic Material
Incorporations by Reference
Separation Operations
Pumps and Compressors
Vapor Blowdown
Safety Relief Valves
Solvent Cleaning in General
Cold Cleaning
Open Top Vapor Degreasing
SUBPART B:
ORGANIC EMISSIONS FROM STORAGE AND LOADING OPERATIONS
Section
218.121
Storage Containers
218.122
Loading Operations
218.123
Petroleum Liquid Storage Tanks
218.124
External Floating Roofs
218.125
Compliance Dates
(Repealed)
218.126
Compliance Plan (Repealed)
SUBPART C:
ORGANIC EMISSIONS FROM MISCELLANEOUS EQUIPMENT
Section
218.141
218.142
218.143
218. 144
SUBPART
E:
SOLVENT CLEANING

118
218.184
218.185
218.186
Conveyorized Degreasing
Compliance Schedule
(Repealed)
Test Methods
SUBPART
F:
COATING OPERATIONS
Section
218.204
218.205
218.206
218.207
218.208
218.209
218.210
218.211
a
a, ‘~
a
~*.,
Emission Limitations for Mariufactur~--’
Daily-Weighted Average Limitations
Solids Basis Calculation
Alternative Emission Limitations
Exemptions from Emission Limitations
Exemption from General Rule on Use of Organic Material
Compliance Schedule
Recordkeeping and Reporting
SUBPART
G:
USE OF ORGANIC MATERIAL
Section
218.301
218.302
218.303
218.304
Section
218.401
218.402
218.403
218.404
218.405
SUBPART
Section
218.421
218.422
218.423
218.424
218.425
218.426
218.427
218.428
218.429
218.430
Use of Organic Material
Alternative Standard
Fuel Combustion Emission Sources Units
Operations with Compliance Program
SUBPART H:
PRINTING AND PUBLISHING
Flexographic and Rotogravure Printing
Applicability
Compliance Schedule
Recordkeeping and Reporting
Heatset-Web-Offset Lithographic Printing
Q:
LEAKS FROM SYNTHETIC ORGANIC CHEMICAL AND POLYMER
MANUFACTURING
EQUIPMENT
PLANT
General Requirements
Inspection Program Plan for Leaks
Inspection Program for Leaks
Repairing Leaks
Recordkeeping for Leaks
Report for Leaks
Alternative Program for Leaks
Open-Ended Valves
Standards for Control Devices
Compliance Date
(Repealed)

119
SUBPART R:
PETROLEUM REFINING
AND
RELATED INDUSTRIES;
ASPHALT MATERIALS
Section
218.441
218.442
218.443
218.444
218.445
218.446
218.447
218.448
218.449
218.450
218.451
218.452
218.453
Petroleum Refinery Waste Gas Disposal
Vacuum Producing Systems
Wastewater (Oil/Water) Separator
Process Unit Turnarounds
Leaks:
General Requirements
Monitoring Program Plan for Leaks
Monitoring Program for Leaks
Recordkeeping for Leaks
Reporting for Leaks
Alternative Program for Leaks
Sealing Device Requirements
Compliance Schedule for Leaks
Compliance Dates
(Repealed)
SUBPART
5:
RUBBER AND MISCELLANEOUS PLASTIC PRODUCTS
Section
218.461
218. 462
218 .463
218. 464
218.465
218.466
Manufacture of Pneumatic Rubber Tires
Green Tire Spraying Operations
Alternative Emission Reduction Systems
Testing and HonitoringEmission Testing
Compliance Dates
(Repealed)
Compliance Plan
(Repealed)
SUBPART T:
PHARMACEUTICAL MANUFACTURING
Section
218.480
Applicability
218.481
Control of Reactors, Distillation Units, Crystallizers,
Centrifuges and Vacuum Dryers
218.482
Control
of
Air
Dryers,
Production
Equipment
Exhaust
Systems and Filters
Material Storage and Transfer
In—Process Tanks
Leaks
Other Emission Sources Units
Testing
Monitoring for Air Pollution Control Equipment
Recordkeeping for Air Pollution Control Equipment
SUBPART V:
AIR OXIDATION PROCESSES
Section
218.521
218.525
218.526
218.527
Definitions
(Repealed)
Emission Limitations for Air Oxidation Processes
Testing and Monitoring
Compliance Date
(Repealed)
218.483
218.484
218.485
218.486
218.487
218.488
218.489

120
Section
218.541
SUBPART W:
AGRICULTURE
Pesticide Exception
Section
218.561
218.562
218.563
Section
218.581
218.582
218.583
218.584
218.585
218.586
Section
218.620
218.621
218.623
218.624
218.625
218.626
218.628
218.630
SUBPART
X:
CONSTRUCTION
Architectural Coatings
Paving Operations
Cutback Asphalt
SUBPART Y:
GASOLINE DISTRIBUTION
Bulk Gasoline Plants
Bulk Gasoline Terminals
Gasoline Dispensing
Facilities
-
Storage
Tank
Filling
Operations
Gasoline Delivery Vessels
Gasoline Volatility Standards
Gasoline Dispensing Facilities Operations
-
Motor Vehicle
Fueling Operations
SUBPART
Z:
DRY CLEANERS
Perchloroethylene Dry Cleaners
Exemptions
Leaks
Compliance Dates
(Repealed)
Compliance Plan
(Repealed)
Exception to Compliance Plan
(Repealed)
Standards for Petroleum Solvent Dry Cleaners
Operating Practices for Petroleum Solvent Dry Cleaners
Program for Inspection and Repair of Leaks
Testing and Monitoring
Exemption for Petroleum Solvent Dry Cleaners
Compliance Dates
(Repealed)
Compliance Plan (Repealed)
SUBPART AA:
PAINT AND INK MANUFACTURING
Applicability
Exemption for Waterbase Material and Heatset-Offset Ink
Permit Conditions
Open-~IopMills, Tanks,
Vats or Vessels
Grinding Mills
Storage Tanks
Leaks
Clean Up
Section
218.601
218.602
218.603
218.604
218.605
218.606
218.607
218 .608
218.609
218.610
218.611
218. 612
218.613

121
Applicability of Subpart EB
Emissions Limitation at Polystyrene Plants
Emissions Testing
Applicability of Subpart BB
(Renumbered)
Emissions Limitation at Polystyrene Plants
(Renumbered)
Compliance Date (Repealed)
Compliance Plan
(Repealed)
Special Requirements for Compliance Plan
(Repealed)
Emissions Testing
(J~enumbered)
SUBPART PP:
MISCELLANEOUS FABRICATED PRODUCT MANUFACTURING
PROCESSES
Section
218.920
218.923
218.926
218.927
218.928
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART
QQ:
MISCELLANEOUS
FORMULATION MANUFACTURING
PROCESSES
Section
218.940
218.943
218.946
218.947
218.948
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART RR:
MISCELLANEOUS ORGANIC CHEMICAL MANUFACTURING
PROCESSES
Section
218.980
218.983
218.986
218.987
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Compliance Schedule
Recordkeeping and Reporting
SUBPART BB:
POLYSTYRENE PLANTS
218.636
218.637
Section
218.640
218.642
218.644
218.875
218.877
218.879
218.881
218.883
218.886
Section
218.960
218.963
218.966
218.967
218.968
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART TT:
OTHER EMISSION
£,OURCES UNITS

122
218.988
Testing
SUBPART UU:
RECORDKEEPING AND REPORTING FOR NON-CTC SOURCES
Section
218.990
Exempt Emission Sources Units
218.991
Subject Emission Sources Units
Section
218.Appendix
A:
List
of Chemicals Defining Synthetic
Organic Chemical and Polymer
Manufacturing
Section 218.Appendix
B:
VOM Measurement Techniques for Capture
Efficiency
Section 218.Appendix
C:
Reference Test Methods en4 For Air
Oxidation Processes Procedures
Section 218.Appendix
D:
Coefficients for the Total Resource
Effectiveness Index
(TRE)
Equation
AUTHORITY:
Implementing Section 10 and authorized by Section
28.5 of the Environmental Protection Act
(Ill.
Rev.
Stat.
1991,
ch.
111½,
par.
1010),
(P.A.
87—1213, effective September
26,
1992)
415
ILCS 5/10 and 28.5.
SOURCE:
Adopted at R9l-7 at 15 Ill.
Reg.
12231,
effective August
16,
1991;
amended in R91—23 at 16
Ill. Reg.
13564, effective
August 24,
1992;
amended in R9l—28 and R91—30 at
16 Ill.
Reg.
13864,
effective August 24,
1992; amended in R93—
at 17 Ill.
Reg.
—,
effective _______________________
SUBPART A:
GENERAL PROVISIONS
Section 218.100
Introduction
a)
This Part contains standards and limitations for
emissions of organic material and volatile organic
material from stationary sources located in the Chicago
area, which is comprised of Cook,
DuPage,
Kane, Lake,
McHenry and Will Counties and Aux Sable Township and
Goose Lake Township in Grundv CountY and Oswego
Township in Kendall County.
b)
Sources subject to this Part may be subject to the
following:
1)
Permits required under 35
Ill.
Adm.
Code
201-- ~
2)
Air quality
standards under
35
Ill.
Adm.
Code

123
c)
This Part is divided into Subparts which are grouped as
follows:
1)
Subpart A:
General Provisions~
2)
Subparts B-F:
Emissions from equipment and
operations in common to more than one industry;
3)
Subpart G:
Emissions from use of organic
material;
4)
Subparts
H—en4
~:
Special r~ulesfor various
industry groups.
~j
Subpart
TT:
Rules
for emission units not
otherwise addressed.
~J
Subpart UU:
Recordkeeping and reporting for
equipment and operations addressed by Subparts PP,
QQ,
RR,
and
TT.
(Source:
Amended
at
Ill.
Reg.
______,
effective
____________
Section 218.101
and Disposal OpcrationSavings Clause
Emission of organic material released during clean-up operations
and disposal shall be included with other omissions of organic
material from the related emission source or air pollution
control
equipment
in
determining total emissions.
~j
Every owner or operator of an emission unit formerly
subject
to
35
Ill.
Adm.
Code
Part
215
shall
have
complied with its standards and limitations by the
dates and schedules ap~licpbleto the emission unit in
accordance with 35
Ill.
Adxn.
Code 215 or upon initial
start—up.
All compliance dates or schedules found in
35
Ill. Adm.
Code 215 are not superseded by this Part
and
remain
in
full
force
and
effect.
~j
Nothing in this Part shall affect the responsibility of
any owner or oPerator that is now or has been subject
to
the
FIP
to
comply
with
its
requirements
thereunder
bY the dates specified in the FIP.
(Source:
Section
repealed,
new
Section
adopted at
_____
Ill.
Reg.
_______,
effective
-
)
Section 218.102
Abbreviations and Conversion Factors
a)
The following abbreviations arc used in this Part:

124
ACTN
American Society for Testing and Materials
bbl
barrels
(42 -gallons)
°C
degrees
Celsius
or
centigrade
cm
centimeters
cu in
cubic inches
degrees
Fahrenheit
FIP
Federal
Implementation
Plan
ft
feet
~S.
2
-
-
--
-
-
-
S.
,~
.,~
gpm
gallons per minute
g/molc
grams
per
mole
gal
gallons
hr
hours
-in
inches
O~
degrees Kelvin
kcal
kilocalorics
kg
kilograms
kg/hr
kilograms
per
hour
in
3
SIP
‘—a”
sq
in
4-
meter
l1tL~
liters per second
pounds
lbs/hr
pounds per hour
lbs/gal
pounds per gallon
Tt’T
~
-~-.4...-.
14,.-.44--
~a.’.FW’~-4.
~-a~J_..as
V ~
SaattS
I..
I
I
I
I
11~U~T~
cubic meters
milligrams
-Negagrams,
metric
~
I
1
I
S.
•~•~
Mg
ml
mm
minutes
NJ
megajoulco
mm
Hg
millimeters
of
mercury
NDO
natural
draft
opening
ppm
parts
per
million
ppmv
parts
per
million
by
volume
psi
pounds per square inch
psia
pounds
per
square
inch
absolute
psig
pounds
per
square
inch
gauge
ocf
standard cubic feet
~-‘~‘
standard
cubic
meter”
-a
State
Implementation
temporary total end
square
centimeters
square
inches
English ton
English ton

125
t14~~
~
~
~
VOC
volatile
organic
compounds
VOL
volatile
organic
liquids
VON
volatile
organic
materials
1-
InL
~11__1_..
r_..S.._....
~
English
Metric
1 gal
3.785
1
ip~ia
6.897
kPa
(51.71 ;~mHg)
2.205
lbs
1
bbl
i
.w/gai.
ii~i,t~uu
mg/i.
0.907
Hg
0.907 Hg
1
ton
1 T
The
abbreviations
and
conversion
factors
of
35
Ill. Adm. Code 211
apply
to
this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section
218.103
Applicability
The provisions of this Part shall apply to all sources located in
the
Chicago
area,
which is composed of Cook,
DuPage, Kane,
Lake,
McHenry e~
~
Will Counties, e~
Aux Sable Township e~
~
Goose
Lake
Township in Grundy County
e~
~
Oswego Township in
Kendall
County.
a)
The provisions of this Part shall become effective
on July
1,
1991 with the following exceptions:
1)
The provisions of this Part shall become effective
on September
1,
1991
for each appellant,
including
the constituents represented by appellants who are
associations, who has appealed the federal
implementation plan
(FIP)
for the Chicago area
(Illinois Environmental Regulatory Group v. USEPA,
No.
90-2778
(and consolidated cases)
(7th
Cir.)).
2)
1
kg
159.0
1
_4
,_
_r~
~
applicable to any individual cource or category of
sources which has appealed the FIP shall
be
stayed
to the extend that such individual source or
category
of
sources
received
a
stay of the
effectiveness
of
the
FIP
from
USEPA
or
from a

126
court.
When the court has taken final action or
when UCEPA has published in the
Federal
Register
final
action to revise or affirm
the provisions of the FIP specifically applicable
to
such
individual
source
or
category
of
sources
or
such
stay
is
terminated,
the
Board
shall
take
corresponding action,
if necessary,
by the
adoption
of
a
peremptory
rule
pursuant
to
35
Ill.
Adm. Code 102.347 and Section 5.03 of the
Administrative
Procedure
Act
(Ill.
Rev.
Stat.
1989,
ch.
127,
oh. 1OO5.03).~g
effectiveness
of
any
provision
of
this
Part
aPplicable
to
any
individual
source
or
cate~orv
of
sources
which
has
appealed
the
FIP
shall
be
stayed
to
the
extent that such individual source or
category of sources received a stay of the
effectiveness of the FIP, pending reconsideration,
from the USEPA or from the court
in the FIP appeal
cited
in
subsection 218.103(a)’ (1) above.
When
USEPA
has
published
in
the
Federal Register final
action
to
revise
or
affirm the
provisions
of
the
FIP specifically applicable to such individual
source or category of sources or such stay is
otherwise terminated, the Board shall take
corresponding action and the Agency shall submit
such
action
to
USEPA for approval.
Until such
time as USEPA approves the corresponding amendment
to
this
Part, the FIP rule shall remain the
applicable implementation Plan for that source or
cate~orv
of
sources under the Clean Air
Act.
3)
The
provisions
of
this
Part
shall
become
effective
on
November
15,
1992
for
all
sources
located
in
Aux Sable Township or Goose Lake Township in
Grundy County or in Oswego Township in Kendall
County.
b)
The provisions of the Part shall not apply to Viskase
Corporation;
Allsteel,
Incorporated;
Stepan
Company;
or
Ford Motor Company to the extent such source has
obtained an adjusted standard from the Board or an
exclusion from the General Assembly for any Subpart of
this
Part
or
of
35
Ill.
Adm.
Code
215.
(Board Note:
Subsection 218.103(b)
of this Section shall be
effective at the federal level only upon approval by USEPA.)
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.104
Definitions

127
The following
terms
are
defined
for
the
purp
of
this
Part.
“Accelacota”
means
a
pharmaceutical
coating
operation
which
consists
of
a
horizontally
rotating
perforated
drum
in which tablets are placed,
a
coating
is
applied
by spraying, and the coating is dried by the flow of
air
across
the
drum
through
the
perforations.
“Accumulator”
means
the
reservoir
of
a condensing unit
receiving the condensate from a surface condenser.
“Acid Cases” means for the purposes of Section 9.4 of
the Environmental Protection Act
(the Act)
(Ill.
Rev.
Stat.
1987,
oh.
111 1/2, par. 1009.4), hydrogen
chloride, hydrogen fluoride and hydrogen bromide, which
exist as gases,
liquid mist,
or any combination
thereof.
“Actual emissions” means the actual quantity of VON
emissions from an emission source during a particular
time period.
“Actual Heat Input” means the quantity of heat produced
by the combustion of fuel using the gross heating value
of the fuel.
“Adhesive” means any substance or mixture of substances
intended to nerve
~
~
ioirrinu comnound
_,
——--—--~~
-
“Afterburner” means a control device in which materials
in gaseous effluent arc combusted.
“Air contaminant” means any solid,
liquid,
or gaseous
matter, any odor,
or any form of energy, that is
capable of being released into the atmosphere from an
emission source.
“Air dried coatings” means any coatings that dry by use
of air or forced air at temperatures up to 363.15~Y~
(194°F)
“Air pollution” means the presence in the atmosphere of
one or more air contaminants in sufficient quantities
and of such characteristics and duration as to be
injurious to human, plant,
or animal
life,
to health,
or to property,
or to unreasonably interfere with the
enjoyment of life or property.
“Air
polluti...~.
control
~
~
or
facility
of
a type intended to eliminate, prevent,
ri~diier
r~i—
r~r,ntrn1
thx-’
t—ml —u-d r~nnf
‘~r~eei
fi ed
~ I r
b—.~
•~
p
—‘
p
V4 1
P4-
44-
~4-4-~
4-
4-
~-
p
-

128
“Air suspension coater/dryer” means
a pharmaceutical
coating operation which consists of vertical chambers
in which tablets or particles are placed, and a coating
is applied and then dried while the tablets or
particles are kept in a fluidizcd state by the passage
of air upward through the chambers.
“Airless spray” means a spray coating method in which
the coating is atomized by forcing it through a small
opening at high pressure. The coating liquid is not
mixed with air before exiting from the nozzle.
“Air-asdisted airless spray” means a spray coating
method which combines compressed air with hydraulic
pressure to atomize the coating material into finer
droplets than
is achieved with pure airless spray.
Lower hydraulic pressure
is used than with airless
spray.
“Allowable emissions” means the quantity of VON
emissions during a particular time period from a
stationary source calculated using the maximum rated
capacity of the source (unless restricted by federally
enforceable limitations on operating rate, hours of
operation,
or both)
and the most stringent of:
the
applicable standards
in 40 CFR Parts
60 and 61; the
applicable implementation plan;
or a federally
enforceable permit.
“Ambient air quality standards” means those standards
designed to protect the public health and welfare
codified in 40 CF~tPart 50 and promulgated from time to
time by the UCEPA pursuant to authority contained in
Section
108 of the Clean Air Act,
42 U.S.C.
7401 et
seq.,
as amended from time to time.
“Applicator” means a device used in a coating line to
apply coating.
“As applied” means the exact formulation of a coating
during application on or impregnation into a substrat~.
“Architectural Coating” means any coating used for
residential or commercial buildings or their
appurtenances,
or for industrial buildings,
which
is
site applied.
“Asphalt”
means the dark—brown to black cementitious
material
(solid,
semisolid, or liquid
in consistency)
of which the main
constituents
are bitumens which occur
naturally or as a residue of petroleum refining.

“Aophalt Prime Coat”
129
a low-viscosity liquid
S.
~puui~
uppiicu
i~.u
~inabsorbent surface
uu
~nc
LiL~I~.
OL
more
than one asphalt coat.
11-Automobilc” means a motor vehicle capable of carrying
no more than 12 passengers.
“Automobile or light-duty truck assembly plant” means a
facility where parts are assembled or finished for
eventual inclusion into a finished automobile or light-
duty
truck ready for sale to vehicle dealers, but not
including customizers, body shops,
and other
rcpaintcrs.
means
“Bead-Dipping”
the dippi..., sf
.....
~
ti~.
bead
into a solvent based cement.
I
S.__1
—4—
__1_.~
_4_
_4
“Bituminous coatings” means black or brownish coating
materials which are soluble in carbon disulfidc, which
consist mainly of hydrocarbons, and which are
obtained
-a.-
-from naturai acposits ~
from the
41-stillation of
~
oils
t,~
of
1,.,.. ~
of ~
“British Thermal Unit”
means the quantity of heat
--
---
~-“--‘~
‘-~
water from 60°Fto 61°F
required t
-(abbreviated btu).
wipe coating” means
a
coating using
--4...~_&h-,
~43
“Automobi~.
-
-
light-duty truck refinishing”
..,~...
the
~epainting of used automobiles and light-duty trucks.
“Baked coatings” means any coating which is cured
or
dried in an oven where the
p0°C(104°F).
oven air temperature exceeds
“Batch Loading” means the process of loading a number
e-f individual parts at the same time for degreasing.
_S.’L_I
i-~1r~th,rn
applying~
object.
“Bulk gasoline plant” means a gasoline storage and
distribution facility with an average throughput of
76,000
1
(20,000 gal)
or less on a 30 day rolling
average that distributes gasoline to gasoline
dispensing facilities.
“Bulk Gasoline Terminal” means any gasoline storage and

130
distribution facility that receives gasoline by
pipeline, ship or barge,
and distributes gasoline to
b-ulk
_.__.IZ__
_1S._
___
___4~__
____~_
~.IJ1II1LI~
yJ.ULIL.o
or
yUUO.L.LIiL~
Ui~JCfl~.Lfly
I
~JL~l
1 IL1LG
“Can” means any metal container, with or without a top,
cover, spout or handles,
into which solid or liquid
materials arc packaged.
“Can coating” means any coating applied on a singl-e
walled container that
is manufactured from metal
sheets
thinner than 29 gauge (0.0141
in.).
“Can coating
means a facility that includes one or
more can coating line(s).
“Can coating line” means a coating line in which any
protective, decorative, or functional coating is
applied onto the surface of cans or can components.
“Capture” means the containment or recovery of
emissions from a process for direction into a duct
which may be exhausted through a stack or vent to a
control device.
The overall abatement of emissions
from a process with an add—on control device is a
function
both
of the capture efficiency and of the
~~ntrt~)
~‘-‘~.rir-c~
~-
A
~
~
e~e-~4~,solvent or othe~
a duct.
The pollutant can then be
used loosely to include the
ci device.
“Capture efficiency” means the fraction of all VON
generated by a process that are directed to an
abatement or recovery device.
“Capture system” means all equipment
(including, but
not limited to, hoods,
ducts,
fans,
ovens,
dryers,
etc.) used to contain, collect and transport an air
pollutant to a control device.
“Clean Air Act” means the Clean Air Act of 1963,
as
amended, including the Clean Air Act Amendments of
1977,
(42 U.S.C.
7401 et seq.),
and the Clean Air Act
Amendments of
1990,
(P.L.
101—549).
“Clear coating” means coatings that lack color and
opacity or are transparent using the undercoat as
a
reflectant base or undertone color.
b~
4-
‘-~~1:’
4aJ~
pollutanto
mt
“Capture
-.
-p
device” means
-
~-‘--~-‘--~
enclosed
other
1HL~1flL1
~

131
“Clear topcoat” moans the final coating which contains
binders,
but not opaque
pigments,
and is specifically
formulated to form a transparent or translucent solid
protective film.
“Closed
p.4~._P
~
means a system that ..snot
to the atmosphere and that i~
of piping,
ooen
conncctionL~,
~iflu~ ii~ncoc~~1ry, L.LOW
.LIluuuiny ueviue~
that transport liquid or vapor from a piece or pieces
of equipment to a control device,
or return the liquid
or vapor to the process line.
“Closed vent system” means a system that is not open to
the
atmosphere
and
is
composed
of
piping,
connections,
and,
if necessary,
flow inducing devices that transport
gas or vapor from an emission source to a control
device.
“Coating” means a material applied onto or impregnated
into
a
substrate
for
protective,
decorative,
or
functional purposes. Cuch materials include, but arc
not
limited
to,
paints,
varnishcs,sealcrs,
adhesives,
thinners,
dilucnts,
and
inks.
“Coating~:applicator”means equipment used to apply a
coating.
“Coating line” means an operation consisting of a
series
of
one
or
more
coating
applicators
and
any
associated flash-off areas, drying areas,
and ovens
wherein a surface coating is applied, dried, or cured.
(It is not necessary for an operation to
have an oven,
or flash-off area,
or drying area to be included in
this definition.)
“Coating plant” means any plant that contains one or
more coating line(s).
“Coil” means any flat metal sheet or strip that is
rolled or wound in concentric rings.
“Coil coating” means any coating applied on any flat
metal
sheet or strip that comes in rolls or coils.
“Coil coating facility” means
a facility that includes
one or more coil coating line(s).
“Coil coating line” means a coating line in which any
protective, decorative or functional coating is appli-e4
onto the surface of flat metal sheets,
strips, rolls,
or coils for industrial
or commercial use.

132
“Cold cleaning” means the process
of cleaning and
removing soils from surfaces by spraying, brushing,
flushing,
or
immersion
while maintaining the organic
solvent below its boiling point.
Wipe cleaning is not
ineludrd
in this
dr’-firiitinn..
“Complete Combustion” means a process in which all
carbon contained in a fuel or gas stream is converted
to carbon dioxide.
“Component” means, with respect to synthetic organic
chemical and polymer manufacturing equipment,
and
petroleum refining and related industries,
any piece of
equipment which has the potential to leak VON
including,
but not limited to, pump seals, compressor
seals,
seal oil degasoing vents, pipeline valves,
pressure relief devices, process drains, and open ended
pipes.
This definition excludes valves which are not
externally regulated,
flanges,
and equipment in
heavy
liquid service.
For purposes of Subpart Q of this
Part, this definition also excludes bleed ports of gear
pumps in polymer service.
“Concrete curing compounds” means any coating applied
to freshly poured concrete to retard the evaporation of
water.
“Condensate” means volatile organic liquid separated
from its associated gases, which condenses due to
changes in the temperature or pressure and remains
liquid at standard conditions.
“Continuous process” means, with respect to polystyrene
resin,
a method of manufacture in which the styrcne raw
material is delivered on a continuous basis to the
reactor in which the styrene is polymerized to
polystyrene-.
“Control device” means equipment (such as an
afterburner or adsorber) used to remove or prevent
the
emission of air pollutants from a
contaminated exhaust
stream.
“Control device efficiency” means the ratio of the
pollution prevented by a control device and the
pollution introduced to the control device,
expressed
as a percentage.
“Conveyorized dcgreasing” means the continuous process
of cleaning and removing soils from surfaces utilizing
either cold or vaporized solvents.

133
“Crude oil” means a naturally occurring mixture which
consists of hydrocarbons and sulfur,
nitrogen,
or
oxygen derivatives of hydrocarbons and which is a
liquid at standard conditions.
“Crude oil gathering” means the transportation of crude
oil or condensate after custody transfer between
a
production facility and a reception point.
“Custody transfer” means the transfer of produced
petroleum and/or condensate after processing and/or
treating in the producing operations,
from storage
tanks or automatic transfer facilities to pipelines or
any other forms
of tr~i~rnrn-tation.
“Cutback Asphalt” means any asphalt which has been
liquified by blending with petroleum solvents other
than residual fuel oil and has not been emulsified with
water.
“Daily-weighted average VON content” means the average
VON content of two or more coatings as applied on a
coating line during any day,
taking into account the
fraction of total coating volume that each coating
represents,
as calculated with the following equation:
VOM~
E
V1
Ci
J/Vp
i—1
where:
VON~
The average VON content of two or more
coatings as applied each day on a
coating line in units of kg VON/l
(lbs
VON/gal) of coating (minus water and any
compounds which are specifically
exempted from the definition of VON),
The number of dif-ferent coatings as
applied each day on a coating line,
-c-f
each
_..
.,
~~4a
a
..
and any compounds which arc specifically
exempted from the definition of VON)
as
applied each day on
a coating line in
units
of
1
(aa~
vi
Cj
The VON content of each coating as
applied each day on a coating line in

134
units of kg VON/i
(lbs VON/gal) of
coating (minus water and any compounds
which arc specifically exempted from the
definition of VON),
and
The total volume of all coatings (minus
water and any compounds which are
sn~eifi esi lv
~vrmnted
from
the
dcfinitionofVOM)
on a coating line
as
in
applied
units of
each day
1
(gal).
“Day” means the consecutive 24 hours beginning at 12:00
AN
(midnight)
local time.
“Degreaser” means any equipment or system used in
solvent cleaning.
“Delivery vessel” means any tank truck or trailer
equipped with a otorage tank
t is uscd for the
transport oi gasoiinc
‘co a
s’ca’ci.onary storage tank at a
gasoline dispensing facility, bulk gasoline plant,
or
bulk gasoline terminal.
“Dip coating” means a method of applying coatings in
which the part is submerged in a tank filled with the
coating.
“Distillate Fuel Oil” means fuel oils of grade No.
1 or
2 as specified in detailed requirements for fuel oil
ASTH D—369—69
(1971).
“Dry Cleaning Facility” means a facility engaged in the
cleaning of fabrics using
an essentially nonaqueous
solvent by means of one or more solvent washes,
extraction of
excess solvent by spinning and drying by
tumbling in an airstream.
The facility includes, but
is not limited to,
washers, dryers,
filter and
purification systems, waste disposal systems, holding
tanks,
pumps and attendant piping and valves.
“Effluent Water Separator” means any tank,
box,
sump or
other apparatus in which any organic material floating
on or entrained or contained in water entering such
tank,
box, sump or other apparatus is physically
separated
and removed from such
water
prior to outfall,
PP~~Pfl#ttfl~tTP
#441
#•~~~4
Vt
4’
r-~
-.—
dra
aas,.
.~
IS
a.
IS
V
7
IS
4...
.a
.4
‘—‘_-4..
“Electrostatic bell or disc spray” means an
electrostatic spray coating method in
rapidly-spinning bell- or disc-shaped
which a
applicator
is

135
used to create a fine mist and apply the coating with
high transfer efficiency.
‘_4t1 IS
ha
z”~
~
~
.4.1i
._a. aj~•~~
?r—.~~~j_
A,
S~
S_-
~_
A..
a_O•~:
~-~Th
“Exterior base coat” means a coating applied to the
exterior of a can body,
or flat sheet to provide
protection to the metal or to provide background for
any lithographic or printing operation.
“Exterior end coat” means a coating applied to the
exterior end of a can to provide protection to the
metal.
“External floatin~~~
-
-
storage tank consisting of a double deck or pontoon
single deck which rests upon and is supported by the
volatile
organic liquid being contained and
is equipped
with
a closure seal or seals to close the space between
the roof
“Electrostatic spray” means a spray coating method in
which opposite electrical charges arc applied to the
substrate and the coating.
The coating is attracted to
the object due to the electrostatic potential between
them.
“Emission Rate” means total quantity of any air
contaminant discharge into the atmosphere in any
one—hour period.
“Emission source” and “source” mean any facility from
which VON is omitted or capable of being emitted into
the atmosphere.
“Enamel”
means
a coating that cures by chemical
cross-linking of its base resin.
Enamels can be
distinguished from lacquers because enamels are not
readily resoluble in their original solvent.
“Enclose” means to cover any VOL surface that is
exposed to the atmosphere.
“End sealing compound coat” means
a compound applied to
can ends which functions as a gasket when the end is
assembled onto the can.
“Excess Air” means air supplied in addition to the
theoretical quantity necessary for complete combustion
of all fuel and/or combustible waste material.
“Excessive release” means
a discharge of more than 295
g
(fl~c
lbs)
of mercaotans and/rn
h’~-,-w--”-
‘~iilfir~r’
into
ge and tank shell.

“Extreme environmental conditions” means exposure to
any or all of the following: ambient weather
conditions;
temperatures consistently above 95°C
(203°F);detergents; abrasive and scouring
agents;
solvents;
or corrosive atmospheres.
“Extreme performance coating” ~
-~““—-
duriiiy intcnaea use is exposes
extreme environmental
c-anditions.
“Fabric coating” means any coating applied on textile
fabric.
Fabric coating includes the application of
coatings by impregnation.
“Fabric coating facility” means a facility that
includes one or more fabric coating lines.
“Fabric coating line” means a coating line in which any
protective,
decorative,
or functional coating or
reinforcing material is applied on or impregnated into
~te~tile
f~hrie..
3-
“Federally enforceable” means all limitations and
conditions which are enforceable by the Administrator
including those rrcmircments developed rmrsuant
to
~fl
#~‘T)
~
~1\
4-A
54.
-
-
-
-
1-equirements within any applicable
implementation plan;
and any permit requirements
established pursuant to 40 CFR 52.21 or under
pursuant to 40 CFR Part 51 Subpart
regulations approved
I and 40 CFR 51.166.
“Final repair coat” means the repainting of any
which
is damaged during vehicle assembly.
topcoat
-“-F4rcbox” means the chamber or compartment of a boiler
or furnace in which materials are burned, but not the
combustion chamber or afterburner of an
incinerator.
“Fixed—roof tank” means a cylindrical shell with a
permanently affixed roof.
“Flexographic printing” means the application of words,
designs, and pictures to a substrate by means of
a roll
printing technique in which the pattern to be applied
is raised above the printing roll and the image carrier
is made of clastomeric materials.
“Flexographic printing line” means a printing line in
which each roll printer
uses a roll with raised areas
for applying an image such as words, designs,
or
pictures to a substrate.
The image carrier on the roll
is made of rubber or other elastomoric materia1-~--
136

137
Il-Floating roof” means a roof on a stationary tank,
~-eservoir,or other container which moves vertically
upon change in volumc of the stored material.
“Fountain solution” means the solution which is applied
to the image plate to maintain hydrophilic properties
of -the non—image areas.
“Freeboard Height” means for open top vapor degreasers,
the distance from the top of the vapor zone to the top
of the degreaser tank.
For cold cleaning dcgrcaserc,
the distance from the solvent to the top of the
degreacier tank.
“Fuel combustion emission source” means any furnace,
boiler, or similar equipment used for the primary
purpose of producing heat or power by indirect heat
transfer.
“Fuel gas system” means a system for collection of
~efincry fuel gas including, but not limited to, piping
f-or collecting tail -gas from various process units,
mixing drums and controls, and distribution piping.
“Cac service” means that the component contains process
fluid that is in the gaseous state at operating
conditions.
“CaD/gas method” means either of two methods for
determining capture which rely only on gas phase
measurements.
The first method requires construction
e-f
a temporary total enclosure
(TTE)
to ensure that all
would-be fugitive emissions arc measured.
The second
method uses the building or room which houses the
facility as an enclosure. The second method requires
that all other VON sources within the room be shut down
while the test is performed, but all fans and blowers
within the room must be operated according to normal
procedures.
means
“Gasoline”
.a.4,J
petrol~.a..~.distill~4--
distillate/alcohol blend having a Reid
of 27.6 kPa or greater which is used as a fuel for
internal combustion engines.
petroL..~
oressure
“Gasoline dispensing facility” means any site where
gasoline
is transferred from a stationary storage tank
to
a motor vehicle gasoline tank used to
to the engine of that motor vehicle.
provide fuel
“Green Tire Spraying” means the spraying of green
tires,
both inside and outside, with release compounds

138
which help remove air from the tire during molding and
prevent the tire from sticking to the mold after
curing.
“Green Tires” means assembled tires before molding and
curing have occurred.
“Cross vehicle weight” means the manufacturer’s gross
weight rating for the individual vehicle.
“Cross vehicle weight rating” means the value specified
by the manufacturer as the maximum design loaded weight
of a single vehicle.
“Heated airless spray” means an airless spray coating
method in which the coating is heated just prior to
application.
“Heatset” means a class of web-offset lithography which
requires a heated dryer to solidify the printing inks.
“Heatset-web-offset lithographic printing line” means a
lithographic printing line in which a blanket cylinder
is used to transfer ink from a plate cylinder to a
substrate continuously fed from a roll or an extension
~
—~n,i -~r~
nvi—ri
I ~
i,sr’d to
sni
i di fv
thr~ r,r1
inks.
“Heavy liquid” means liquid with a true vapor pressure
of less thsn
fl1
IrPn
(flfl~ ~ti~
~t 2~4~°V
(7fl°F~I
-
established in a standard reference text or as
determined by ASTM method D2879-86 (incorporated by
reference in Section 218.112); or which has 0.1 Reid
Vapor Pressure as determined by ASTN method D323-82
-(-incorporated by reference in Section 218.112); or
which when distilled requires a temperature of 42l.95°K
(300°F) or greater to recover 10 percent of the liquid
as determined by ASTN method D8C-82
(incorporated by
reference in Section 218.112).
“Heavy
off-highway vehicle products” means,
for the
purpose of Subpart F of this Part,
heavy construction,
mining,
farming,
or material handling equipment; heavy
industrial engines; diesel—electric locomotives and
associated power equipment; and the components of such
equipment or engines.
I~T~Tr~wy
fl
c.i~J
r-
n
r~r
~-
4-~
ff—high.._~
tlJ~~.~j
‘u~e#~
_-~~-i~
faci’
~y”
means a facility that includes one
or more
heavy
off-highway vehicle products coating line(s).

139
“Heavy off-highway vehicle products coating line” means
a -coating line in which any protective,
decorative,
or
functional coating is applied onto the surface of heavy
off-highway vehicle products.
“High temperature aluminum coating” means a coating
that is certified to withstand a temperature of 537.8°C
(1000°F) for 24 hours.
“Hood” means a partial enclosure or canopy for
capturing and exhausting,
by means of a draft, the
organic vapors or other fumes rising from a coating
pr-oceso or other source.
“Hood capture efficiency” means the emissions from a
process which are captured by the hood and directed
into a control device, expressed as a percentage of all
emissions.
“Hot well” means the reservoir of a condensing unit
receiving the condensate from a barometric condense~
“Hour” means a block period of 60 minutes
(e.g.,
1:00am
tc- 2:00am).
“In-process tank” means
a container used for mixing,
blending,
heating, reacting, holding,
crystallizing,
evaporating or cleaning operations in the manufacture
of pharmaceuticals.
“In-situ Sampling Systems” means nonextractive samplers
or in-line samplers.
“In vacuum service” means,
for the purpose of Subpart Q
of this Part,
equipment which
is operating at an
internal pressure that
is at least
5 kPa
(0.73 psia)
below ambient pressure.
“Incinerator” means a combustion apparatus in which
refuse is burned.
“Indirect heat transfer” means transfer of heat in such
a way that the source of heat does not come into direct
contact with process materials.
“Ink” means
a
coating used in printing,
impressing,
or
transferring an image onto
a substrate.
“Interior body spray coat” means a coating applied by
spray to the interior of
a can
body..

140
“Internal—fbating roof” means a cover or roof in a
fixed roof tank which rests upon and
is supported by
the volatile organic liquid being contained and is
equipped with a closure coal or seals to close the
space between the roof edge and tank Dhell.
ItT
~
,.Ip
...s,#4tp~.
t~pp~
finishes formulated
ahJ
tha
U
IS
.4.
~I.ta.
.4 IS IS~.t
with
nitroccilulose or synthetic rca~..._.~___2
evaporation without chemical reaction, including clear
lacquer sanding scalers.
“Large appliance” means any residential and commercial
washers,
dryers,
ranges,
refrigerators, freezers, water
heaters,
dishwashers, trash compactors,
air
conditioners, and other similar products.
“Large appliance coating” means any coating applied to
the component metal parts
(including, but not limited
to,
doors, cases,
lids,
panels, and interior support
parts)
of residential and commercial washers,
dryers,
ranges,
refrigerators,
freezers, water heaters,
dishwashers, trash compactors,
air conditioners, and
other similar products.
“Large appliance coating facility” means a facility
that includes one or more large appliance coating
line(s).
“Large appliance coating line” means a coating line in
which any protective,
decorative,
or functional coating
is applied onto the -surface of large appliances.
“Light liquid” means VON in the liquid state which is
not defined as heavy liquid.
“Light-duty truck” means any motor vehicle rated at
3,850 kg gross vehicle weight or less,
designed mainly
to transport property.
“Liquid/gas method” means either of two methods for
determining capture which require both gas phase and
liquid pha3e measurements and analysis.
The first
method requires construction of a TTE.
The second
method uses the building or room which houses the
facility as an enclosure.
The second
method requires
that all other VON sources within the room be shut dowr
while the test is performed,
but all fans and blowers
within the room must be operated according to normal
a.
‘S ‘S

141
“Liquid-Mounted Coal” means a primary seal mounted in
continuous contact with the liquid between the tank
wall and the floating roof edge around the
circumference of the roof.
“Liquid service” means that the equipment or component
contains process fluid that is in a liquid state at
operating conditions.
“Liquids Dripping” means any visible leaking from a
seal including spraying, misting, clouding and ice
formation.
“Lithographic printing line” means a printing line,
except that the substrate is not necessarily fed from
an unwinding roll,
in which each roll printer uses a
roll where both the image and non—image areas are
essentially in the same plane
(planographic).
“Low Solvent Coating” means a coating which contains
less organic solvent than the conventional coatings
used by the industry.
Low solvent coatings include
water—hnri-~~-higher solids, clcctro-dcposition and
towdcr
‘‘~‘
“Magnet wire” moans aluminum or copper wire formed into
an electromagnetic coil.
“Magnet wire coating” means any coating or electrically
insulating varnish or enamel applied to magnet wire.
“Magnet wire coating facility” means
a
facility that
includes one or more magnet wire coating line(s).
“Magnet wire coating line” means a coating line in
which any protective,
decorative,
or functional coatii~g
is applied onto the surface of
a magnet wire.
“Malfunction” means any sudden and
unavoidable failure
of air pollution control equipment,
process equipment,
or a process to operate
in a normal or usual manner.
Failures that are caused entirely or in part by poor
maintenance, careless operation,
or any other
preventable upset condition or preventable equipment
breakdown shall not be considered malfunctions.
“Manufacturing process” means a method whereby a
process emission source or series of process emission
r~used
to vn~
mnte~in 1 s
-
fefld
stocks
-
nto a prodr
either for sale or for use as a component in
a
subsequent manufacturing process.

142
designed to transport and recover styrene monomer and
ether impurities from other products and by—products in
a polystyrene plant,
including but not limited to the
styrene devolatilizer unit and styrene recovery unit.
“Maximum theoretical emissions” means the quantity of
volatile organic material emissions that theoretically
could be emitted by a stationary source before add—on
controls based on the design capacity or maximum
production capacity of the source and 8760 hours per
year.
The design capacity or maximum production
capacity includes use of coating(s)
or ink(s) with the
highest volatile organic material content actually used
in practice by the source.
Provided, however, the
Agency shall, when appropriate, and upon request by the
permit applicant,
limit the “maximum theoretical
emissions” of
a source by the imposition of conditions
in a federally enforceable operating permit for such
source.
Such conditions shall not be inconsistent with
requirement of the Clean Air Act,
as amended,
or any
applicable requirements established by the Board.
Such
conditions shall be established in place of design
capacity or maximum production capacity in calculating
the “maximum theoretical emissions” for such source and
may include, among other things, the establishment of
production limitations, capacity limitations, emission
limitations,
or limitations on the volatile organic
material content of coatings or inks, or the hours of
operation of any emission source, or a combination of
any such limitations.
Production or capacity limitations shall be established
on basis of no longer than one month except in those
cases where a limit spanning a longer period of time is
appropriate.
In such cases,
a rolling limit”
shall be
employed.
Any production or capacity limitations shall
be verified through appropriate recordkecping.
(Board
Note:
The USEPA may deem operating permits which do
not conform to the operating permit program
requirements and the requirements of USEPA’s underlying
regulations, including the requirement that limitations
be quantifiable and enforceable as a practical matter,
not
“fedc-~r-i1lv ~nfn~cr’-thle
“~
~~..1
“Metal furniture”
means
a furniture piece including,
but not limitcd to,
tables,
chairs, waste b~skcts,
.,_1..I.__I
~
“Metal furniture coating” means any non—adhesive
eoating applied to any furniture piece made of metal
or

143
any metal part which is or will be assembled with other
metal,
wood,
fabric, plastic or glass parts to form a
furniture piece
including,
but not limited to,
tables,
chairs, waste baskets,
beds,
desks,
lockers,
benches,
shelving, file cabinets,
lamps, and room dividers.
This definition shall not apply to any coating line
coating miscellaneous metal parts or products.
“Metal furniture coating facility” means
a facility
that includes one or more metal furniture coating
line(s).
“Metal furniture coating line” means a coating line in
which any protective,
decorative,
or functional coating
is applied onto the surface of metal furniture.
“Metallic shoe—type seal” means a primary or secondary
seal constructed of metal sheets
(shoes) which are
joined together to form a ring,
springs, or levers
which attach the shoes to the floating roof and hold
the shoes against the tank wall,
and a coated fabric
which is suspended from the shoes to the floating roof.
“Miscellaneous fabricated product manufacturing
process”~means:
-
A manufacturing process involving one or more of the
following applications,
including any drying and curing
of formulations,
and capable of emitting VON:
embl
products
Asphalt solutions to paper or fiberboard
Asphalt to paper or felt
Coatings or dye to leather
Coatings to plastic
Coatings to rubber or glass
iterial to manufactured items
Plastic foam scrap or “fluff” from the manufacture
of foam containers and packaging material to form
resin pallets
Rosin solutions to fiber substances
Viscose solutions for food casings

144
The storage and handling of formulations associated
with the process described above, and the use and
handling of organic liquids and other substances Lor
clean-up operations associa-cca wi’cn tne r~ocess
described in this definition.
“Miscellaneous formulation inunuLaw..uring process”
means:
A manufacturing process which compounds one or more of
the following and is capable of emitting VON:
Adhesives
Aci~ai~a
~
haISaIA
~.aIS4S?
Caulks,
scalants,
or waterproofing agents
Coatings,
other than paint and ink
Concrete curing compounds
Dyes
Friction materials and compounds
Resin solutions
Thibber solutions
solutions
The storage and handling of formulations associatod
with the process described above,
and the use and
handling of organic liquids and other substances for
clean-up operations associated with the process
“Miscellaneous metal parts or products” means any metal
part or metal product, even
if attached to or combined
with a nonmetal part or product,
except cans, coils,
metal furniture,
large appliances, magnet wire,
automobiles,
ships, and airplane bodies.
“Miscellaneous metal parts and products coating” means
any coating applied to any metal part or metal product,
even if attached to or combined with a nonmetal part or
product,
except cans, coils, metal furniture,
large
appliances,
and magnet wire.
Prime coat,
prime
surfacer coat,
topcoat, and final repair coat for
automobiles and light-duty trucks are not miscellaneous
metal parts and products coatings.
However, underbody

145
anti-chip (e.g., underbody plastisol)
automobile and
light-duty truck coatings are miscellaneous metal parts
and products coatings.
Also,
automobile or light-duty
truck refinishing coatings, coatings applied to the
exterior of marine vessels,
coatings applied to the
exterior of airplanes,
and the customized topcoating of
automobiles and trucks if production is less than 35
vehicles per day are not miscellaneous metal parts and
products coatings.
“Miscellaneous metal parts or products coating
facility” means a facility that includes one or more
miscellaneous metal parts or products coating lines.
“Mi~~
means:
--
~nr-ruv-i
rn-ganlc chemical manufacturing
prrires’~”
—J
compounds or mixtures of
capable of emitting VON:
~_••_h__4__.~_~
...-~
..t-..4
—.~--..
4
Chemicals listed
in Appendix A of this Part
~niorinatco ana suitonatco compounas
Cosmetic, detergent,
soap,
or surfactant
intermediaries or specialties and products
Diciinfcctants
Food
sdditives
Oil and petroleum p
ri
_....&..~
additives
Dolymers
Rubber additives
~wccLcners
Varnishes
The storage
with the pr
“Miscellaneolls
means a coating line in which any protective,
decorative,
or functional coating is applied onto the
surface of miscellaneous metal parts or products.
-
.--
products coating
liT’-”~
d handling of form
sci described above

146
handling of organic liquids and other substances for
clean-up operations associated with the process
“Multiple package coating” means a coating made from
more than one different ingredient which must be mixed
prior to using and has a limited pot life due to the
chemical reaction which occurs upon mixing.
“No Detectable Volatile Organic Material Emissions”
means a discharge of volatile organic material into the
atmosphere as indicated by an instrument reading of
less than 500 ppm above background as determined in
accordance with 40 CFR 60.485(c).
“Offset” means, with respect to printing and publishing
operations,
usc of a blanket cylinder to transfer ink
from the plate cylinder to the surface to be printed.
“Opaque stains” means all stains that are not semi-
transparent stai~s-~-
“Open top vapor degreasing” mcans the batch process of
cleaning and removing soils from surfaces by condensing
hot solvent vapor on the colder metal parts.
“Open-ended valve” means any valve, except pressure
~elief devices, having one side of the valve in contact
with process fluid and one side open to the atmosphere,
either directly or through open piping.
“Operator of Gasoline Dispensing Facility” means any
person who is the lessee of or operates, controls or
supervises a gasoline dispensing facility.
“Organic compound” means any compound of carbon,
exclUding carbon monoxide, carbon dioxide, carbonic
acid, metallic carbides or carbonates,
and ammonium
carbonate.
“Organic material” means any chemical compound of
carbon including dilucnts and thinners which arc
liquids at standard conditions and which arc used as
dissolvers,
viscosity reducers,
or cleaning agents,
but
excluding methane,
carbon monoxide,
carbon dioxide,
carbonic acid, metallic carbonic acid, metallic
carbide, metallic carbonates,
and ammonium carbonate.

coatings.
147
“Paper coating” means any coating applied on paper,
plastic film,
or metallic foil to make certain
prosucts,
including
(but not limited to)
adhesive tapes
and labels, book covers, post cards, office copier
r~-~nrr
drriftinri
r~r~er
or pressure sensitive tapr’s~
~——~-.—~
I
~
~
.r——z——..-
I
Paper coating includes the application of coatings by
impregnation and/or saturation.
“Paper coating facility” mcans
a facility
lines.
that includes
one or more paper coating
“Paper coating line” means
protective,
decorative,
or
a coating
functional
line
in
coating
which
is
any
“Organic vapor” means the gaseous phase of an organic
material or a mixture of organic materials present in
the atmosphere.
chamber within which heat is used for
-“Oven” means a
one or more or enc roi..iowlng purposes:
ary,
Daicc,
curc,
or polymerize a coating or ink.
“Overall control” means the product of the capture
efficiency and the control device efficiency.
“Overvarnish” means a transparent coating applied
directly over ink or coating.
“Owner of Casoline Dispensing Facility” means any
person who has legal or equitable title to a stationary
storage tank at a gasoline dispensing facility.
“Owner or operator” means any person who owns,
operates,
leases,
controls,
or supervises an emission
source or air pollution control equipment.
“Packaging rotogravure printing” means rotogravure
printing upon paper, paper board, metal
foil, plastic
film,
and other substrates, which are,
in subsequent
operations,
formed into packaging products or labels
for articles to be sold.
“Packaging rotogravure printing line” means a
rotogravure printing line in which surface coatings are
applied to paper, paperboard,
foil,
film, or other
substrates which are to be used to produce containers,
packaging products,
-or labels for articles.
‘Paint manufacturing plant” means
a plant that mixes,
blends,
or compounds enamels,
lacquers,
scalers,
shellacs,
stains, varnishes,
or pigmented surface

148
applied on, saturated into,
or impregnated into paper,
plastic film,
or metallic foil to make certain
products,
including
(but not limited to) adhesive tapes
and labels, book covers,
post
cards,
office copier
paper,
drafti-mg paper,
and pressure sensitive tapes.
“Parts per million
(volume)” means a volume/volume
r~it.iu
WILLUI1
cxpreo~.ccthe volumetric concentration of
gaseous air contaminant in a million unit volume of
gas.
“Person” means any individual, corporation,
partnership, association,
State, municipality,
political subdivision of a State; any agency,
department,
or instrumentality of the United States;
and any officer,
agent,
or employee thereof.
“Petroleum” means the crude oil removed from the
earth
and the oils derived from tar sands,
shale,
and coal.
Liquid”
...,a.
~
J~a.IS
4~i#&~~a.
~ciat a
~~ified
ii”
2-D and 4-D, as
— p
~1T-~
f’
~
~
condensate
ISa.
“Petroleum refinery” means any facility engaged in
producing gasoline, kerosene, distillate fuel oils,
residual fuel oils,
lubricants,
or other products
through distillation of petroleum,
or through
redistillation,
cracking,
or reforming of unfinished
petroleum derivatives.
“Pharmaceutical” means any compound or mixture,
other
than food, used
in
the nrevention, diagnosis,
uiicviaeion,
treatment,
or cure
or u~wci~.u~c
in
nuiu~n~ind
animal.
“Pharmaceutical coating operation” means a device in
which a coating is applied to a pharmaceutical,
including air drying or curing of the coating.
£
-
means
- ~..
P~-~-r
S
*
IS..aa....*..a
ISP
1 1y React
a
‘S
£*~
—.
a-~~
—~
A
UJ
ISa.
material with an aggregate of more than 20 percent of
its
total volume composed of the chemical compounds
classified below or the com~osition of which exceeds
any of the following individual percentage composition
limitations.
Whenever any photochemically reactive
m~teri-~l
or
-~r~v
constituent of any oraanie material may
4 4—.
~
4_~,._-~.i__~,4-
pL~..Lu.LCuffl
Number
6 fuel
reLilicry,
L)UL
flOL.
oils as specified
iItc.LuUiIly HumiJer
s.
Lrlrougt-1
in ASTM D-396—69,
ga-s
turbine fuel
•-
oils
ASTH
Numbers 2—CT
fl-~flfl 71
or
through
diesel
4-CT as
fuel
oils
Numhe,-s
specified in ASTN D-975-68
l-..p
~
.c~.

149
than one of the above groups of organic materials it
shall be considered as a member of the most reactive
n-rour,
-
thst
is
-
the
~rnun
h..,vi
n~ the
1et
~1
1ohl
e
pcrccnt of the
tota....
A combination of aromatic compounds with eight or
more carbon atoms to the molecule except
A combination of ethylben
branched hydrocarbon stru
percent.
ketones having
cs or toluene:
20
“Pigmented coatings” means opaque coatings containing
binders and colored pigments which are formulated to
conceal the wood surface either as an undercoat or
topcoat.
“Plant” -means all of the pollutant-emitting activities
which belong to the same industrial grouping, are
located on one or more contiguous- or adjacent
properties, and are under the control of the same
person
(or persons under common control), except the
activities of any marine vessel.
Pollutant-emitting
activities shall be considered as part of the same
industrial grouping if they belong to the same “Major
Croup”
(i.e., which have the same two-digit code)
as
described in the “Standard Industrial Classification
Manual,
1987”
(incorporated by- reference in Section
218. 112).
“Plasticizers” means a substance added to a polymer
composition to soften and add flexibility to the
product.
“Pneumatic Rubber Tire Manufacture” means the
production of pneumatic rubber tires with a bead
diameter up to but not including 20.0 inches and cross
section dimension up to 12.8
inches, but not including
specialty tires for antique or other vehicles when
produced on equipment separate from normal production
lines for passenger or truck type tires.
~4-~
~r
manufacture po.Lystyrene
A combination of hydrocarbons, alcohols,
aldehydcs, esters,
ethers or -ketones having an
clefthis s~syels-slefinic types of unsaturation~
5 percent.
This definition does not apply to
pcrchlorocthylcne or trichloraethylene.
PThnt”
means
any
plant using styr~net~

4
150
styrenc polymer and additi.~
..~
a~
~raoturea ~t
a polystyrene plant.
“Pressure Release” means the emission of materials
resulting from system pressure being greater than set
pressure of the pressure relief device.
“Pressure Tank” means a tank in which fluids are stored
at a pressure greater than atmospheric pressure.
“Prime coat” means the first of two or more coatings
applied to a surface.
“Prime surfacer coat” means a coating used to touch up
ar-cas on the surface of automobile or light-duty truck
bodies not adequately covered by the prime coat before
application of the top coat.
The prime surfacer coat
is applied between the prime coat and topcoat. An
anti-chip coating applied to main body parts
(e.g.,
rocker panels, bottom of doors and fenders,
and leading
edge of roof)
is a prime surfacer coat.
“Primers” means any coatings formulated and applied to
substrates to provide a firm bond between the substrate
and oubscauent goats.
I
“Printing”
~
the applicati~~.
-Sf-
..~..a......,
~
~AA4
pictures to a substrate using
.i.nit.
“Printing line” means an operation consisting of
a
series of one or more roll printers and any associated
roll coaters,
drying areas, and ovens wherein one or
more coatings are applied,
dried,
and/or cured.
“Process” means any stationary emission source other
than a fuel combustion emission source or an
i
nei
ner-~tor
“Process Unit” means components assembled to produce,
as intermediate or final products,
one or more of the
chemicals listed in
35
Ill. Adm. Code 218 Appendix A.
A process unit can operate independently if supplied
with sufficient feed or raw materials and sufficient
storage facilities for the product.
“Process Unit Shutdown” means a work practice or
operationaiprocedure that stops production from a
process unit or part
r,f r~
r~ocess
ur~it
~.n iinscheclnlerl
work
~a.
~
~,a.
ISIS’S~~a.~
~hat ~
production from a process unit or part of a proce~
un-I-f
frn—
1 r’ss fh~n 7A
hnwrs
i
not
n nrocess
unit
-
.-_..pnpn.,.p
4—

which the coolant supplied
cooled by a mechanical
devi~..-,
tower or evaporative spray cooling,
sugn as
refrigeration unit or steam
chiller unit.
151
&~utdown. The usc of spare components and technically
feasible bypassing of components without stopping
production is
not
a process unit shutdown.
“Production equipment exhaust system” means a system
f-or collecting and directing into -the atmosphere
emissions of volatile organic material from reactors,
centrifuges, and other process emission sources.
“Publication rotogravure printing line” means a
rotogravure printing line in which coatings are applied
to paper which is subsequently formed into books,
magazines,
catalogues,
brochures, directories,
newspaper supplements, or other types of printed
material.
“Purged Process Fluid” means liquid or vapor from a
process unit that contains volatile organic material
and that results from flushing or cleaning the sample
line(s)
of a process unit so that an uncontaminated
sample may then be taken for testing or analysis.
“Reactor” means a vat,
vessel,
or other device in which
chemical reactions take place.
“Reasonably Available Control Technology
(P.ACT)” means
the lowest emission limitation that an emission source
is capable of meeting by the application of control
technology that is reasonably available considering
technological and economic feasibility.
“Refiner” means any person who owns,
leases,
operates,
controls,
or supervises a refinery.
“Refinery Fuel Gas” means any gas which is generated
by
a petroleum refinery process unit and which
is
combusted at the refinery, including any gaseous
mixture of natural gas and fuel gas.
“Refinery unit, process unit or unit” means a set of
components which are a part of a basic process
operation such
as distillation, hydrotreating,
cracking,
or reforming of hydrocarbons.
“T??—fri
rirr—it,—d
condenser”
mesns
~
sii~f
r conden~er
I n
-.
condenser
--
other than by
has
a
been
COOliA~

152
“-Reid vapor pressure” means the standardized measure of
the
vapor pressure of a liquid in pounds per square
inch absolute
(Psia)
at 100°F(37.8°C).
“Repair coatings” means coatings used to correct
imperfections or damage to furniture 3urface.
“Repaired” means,
for the purpose of Subpart
Q
of this
Part, that equipment component has been adjusted,
or
c-~thcrwise ~1tcrr’d
tr~ci imin~te ~
“Residual Fuel Oil”
fuel oils of
~
No.
4,
5
and 6 as specified in detailed requirements for fuel
oils A.S.T.M.
D-396—69
(1971).
“Retail Outlet” means any gasoline dispensing facility
at which gasoline is sold or offered for sale for use
in motor vehicles.
“Roll coater” means an apparatus in which a uniform
layer of coating is applied by means of one or more
rolls across the entire width of a moving substrate.
“Roll printer” means an apparatus used in the
application of words,
designs, and pictures to a
s-ubstrate, usually by means of one or more rolls each
with only partial coverage.
“Roll printing” means the application of words,
designs,
and pictures to a substrate usually by means
of a series of hard rubber or metal rolls each with
only partial coverage.
“Roller coating” means a method of applying a coating
to a sheet or strip in which the coating
is transferred
by a roller or seriesof rollers.
“Rolling limit” means that a limit or limitation must
not exceed an annual limit rolled on a basis of at most
a month monthly basis; that is, for example,
a monthly
production or capacity level must be determined for
each parameter subject to a production or capacity
limitation and added to the eleven prior monthly levels
for monthly comparison with the annual limit.
“Rotogravure printing” means the application of words,
designs,
and pictures to a substrate by means
of a roll
printing technisue in which the pattern to be applied
recessed rclQtivc to the non—image

•~
— S.
153
~eas
for applying an image to a substrate.
“Safety relief valve” means a valve which
is normally
closed and which is designed to open in order to
relieve excessive pressures within a vessel or pipe.
p.—__,,
~
~
pp.-4-4....-.~.
~
‘~
Candi..-.,
.__e_..-~...a.
~
*•~IS
a.ISa.
....—l._
~
for
and
applied to bare wood for sanding and to seal the wood
for rnibscguent
nnnlicition
of virnish.
To he
I
i
L.
“Sealer” means
wood prior to
a
the
coating containing
application of the
binders which seals
subsequent
coatings.
——~.~~————.,
or
~i-~-c-i-
“Set of safety relief valves” means one or more safety
relief valves designed to open in order to relieve
4
4-1~
“Sheet basecoat” means a coating applied to metal when
the metal
is in sheet form to serve as cither the
exterior or interior of a can for either two-piece or
“Side-seam spray coat” means a coating applied to the
scam of a three-piece can.
~L
L~
ing.
_~I~
~
S.
.1
2
Sensor”
dev-ica that
az~raca physical
quantity or the change in a physical quantity such as
temperature, pressure,
flow rate,
pH,
or liquid level.
“Semi-transparent stains” means stains containing dyes
or semi-transparent pigments which are formulated to
enhance wood grain and change the color of the surface
but not to conceal the surface,
including,
but not
limited to,
s~n
stnivi
toner,
non—rzrain r~-~isinristains,
pad stain,
-
t-
-
“Single coat” means one coating application applied to
a metal surface.
“Solvent” means a liquid substance that
dissolve or dilute another substance.
“Solvent cleaning” means the process of
is used
cleaning
to
soils
from
surf~ccs
h~jcold
elc~nin~
onen ton
~nnr
—J
2
ISr1zcddcgr~~

“Specified air contaminant” means any air contaminant
as to which this Part contains emission standards or
ether specific limitations.
11-S-plash loading” means a method of loading a tank,
railroad tank car, tank truck, or trailer by use of
ether than a submerged loading pipe.
“-Stack” means a flue or conduit, free-standing or with
exhaust port above the roof of the building on which it
is mounted,
-by
which air
contaminants are emitted into
the atmosphere.
-11-Ctandard conditions” means a temperature of 70°Fand a
pressure of 14.7 psia.
“-Standard cubic foot (scf)” means the volume of one
eubic foot of gas at standard conditions.
“Standard Industrial Classification Manual” means the
Etandard Industrial Classification Manual
(1987),
~-upcrintenc1ent
of Documents, U.S. Government Printing
Office, Washington,
DC 20402
(incorporated by reference
in Section 218.112).
“Start-up” means the setting in operation of an
-
emission source for any purpose.
“Stationary emission source” mean an emission source
which is not self-propelled.
“Storage
tank or
~t~r~c
vessel” means any
~
--
“Ctyrenc Devolatilizer Unit” means equipment performing
the function of separating unrcactcd styrcnc monomer
and other volatile components from polystyrene in a
vacuum devolzitilizer.
“Ctyrcnc
Recovery Unit” means equipment performing the
function
-of -separating
styrene monomer from other less
volatile components of the styrenc devolatilizer unit’s
eutput.
The separated styrene monomer may be reused as
a raw material
in the polystyrene plant.
“Submerged loading pipe” means any discharge pipe or
~-ozrle which
meets either of the following conditions:
154
tank,—r~~a..~4a.
.ir contai..ISa.
......ed for the .~.orageof
VOL.
Where the tank is filled from the top,
the end of
the discharge pipe or nozzle must be totally

155
Whore the tank is filled
discharge pipe or nozzle
when the liquid level
is
bottom of the tank.
L4M~
~.a.
LA ~
La
applied or
‘I
the surfa
into which
~
coatL.~
onto which
--
I
-
imp
ting
i
“Surface condenser” means a device which removes a
substance from a gas stream by reducing the temperature
ef the stream, without direct contact between the
coolant and the stream.
“Synthetic Organic Chemical or Polymer Manufacturing
Plant” means a plant
thçtt produces, as intermediates or
final products, one or more of the chemicals or
polymers listed in 35 Ill. Adm. Code 218 Appendix A.
“Tablet coating operation” means a pharmaceutical
coating operation in which tablets arc coated.
“Thirty-day rolling average” means any value
arithmetically averaged over any consecutive
thirty-days.
“Three piece can” means a can which is made from a
~-ectangularsheet and two circular ends.
“Topcoat” means a coating applied in
a multiple
co-at
operation other than prime coat,
final repair coat,
or
prime surfacer coat.
“Topcoat operation” means
all topcoat spray booths,
flash—off areas,
and bake ovens at a facility which are
used to apply,
dry,
or cure the final coatings (except
final off-line repair)
on components of automobile or
light-duty truck bodies.
“Transfer efficiency” means the ratio of the amount of
eoating solids deposited onto a part or product to the
total amount of coating solids used.
“Tread End Cementing” means the application of a
solvent-based cement to the tire tread ends.~
“True vapor pressure” means the equilibrium partial
pressure exerted by a volatile organic liquid as
determined in accordance with methods described in
American
P~trnleum
Tn~titute
Bulletin
251-7---
submerged when
4-~
the liquid level
is
15 cm
(6 in.)
nn of the tank.
from the side,
the
must be totally subm
A_~
~~_L_1
a
~rged

wncn
155
submerged
above the
when the liqui
bottom of the
d 1ev
tank.
el is 15 cm
(6
in.)
Where the tank is filled from the side,
the
dischwne
-nine
or
nocc’~ie
must
he totally
(1R
in
submerged
~htwc
fhe
the liquid level is
bottom of the tank.
“Substrate” means the surface onto which a coating is
applied or into which a coating is impregnated.
“Surface condenser”
incans a -device which removes a
a.
~
by rcduc.4
of the stream, without direct contact between the
noolsnt
snil the
stresm
oubstance f~”
“Synthetic Organic Chemical or Polymer Manufacturing
Plant” means a plant that produces,
as intermediates or
final products, one or more of the chemicals or
polymers listed in 35
Ill. Adm. Code 218 Appendix A.
“Tablet coating operation” means a pharmaceutical
coating operation in which tablets are coated.
“Thirty—day rolling average” means any value
arithmetically averaged over any consecutive
thirty-days.
“Three—piece can” moans a can which is made from a
rectangular sheet and two circular
ends—.
“Topcoat” means a coating applied in a multiple coat
operation other than prime coat,
final repair coat,
or
prime surfacer coat.
“Topcoat operation” means all topcoat spray booths,
flash-off areas,
and bake ovens at a facility which arc
used to apply,
dry,
or cure the final coatings
(except
final off-line repair)
on components of automobile or
light-duty truck bodies.
“Transfer efficiency” means the ratio of the amount of
coating solids deposited onto a part or product to the
total amount of coating solids used.
“Tread End Cementing” means the application of a
solvent-based cement to the tire tread ends.
“True vapor pressure” means the equilibrium partial
pressure exerted by a volatile organic liquid as
determined in accordance with methods described in
American Petroleum Institute Bulletin 2517,
a...—.
-
--

operating refinery unit,
emptying
con-
to do inspection,
and ,~..ngthe unit
back
into
~.
tents
—I,——,
maintenance
“Two—piece can” means
a can which is drawn from a
shallow cup and requires only one end to be attached.
“Undcrcoatcrs” means any coatings formulated for and
applied to substrates to provide a smooth surface for
subsequent coats.
“Undcrtread Cementing” means the application of a
solvent—based cement to the underside of a tire tread.
Unregulated safety relief valve” means a safety relief
valve which cannot be actuated by a means other than
high pressure in the pipe or vessel which it protects.
“Vacuum producing system” means any reciprocating,
rotary, or centrifugal blower or compressor or any jet
ejector or device that creates suction from a pressure
below atmospheric and discharges against a greater
pressure.
“Valves not externally regulated” means valves that
have no external controls,
such as in-line check
valves.
“Vapor balance system” means any combination of pipes
or hoses which creates a closed system between the
vapor spaces of an unloading tank and a receiving tank
such that vapors displaced from the receiving tank are
transferred to the tank being unloaded.
“Vapor collection system” means all piping,
seals,
hoses, connections, pressure—vacuum vents,
and other
possible sources between the gasoline delivery vessel
and the vapor processing unit and/or the storage tanks
and vapor holder.
“Vapor control system” means any system that limits or
prevents release to the atmosphere of organic material
in the vapors displaced from a tank during the transfer
of gasoline.
“Vapor-Mounted Primary Seal” means
a primary seal
mounted with an air space bounded by the bottom of the
156
“Evaporation Loss
edition, February
From
1980
Floating Roof
(incorporated
Tanks,” second
by reference in
Lection 218.112).
“Turnaround” means the procedure of shutting down an
aascous
LA~~La
.-~-OpUCti~I1
-
LaLa~
14~_~~i:4
and
a.
IS7La*a.
.jork,

157
primary sczil,
the tank wall,
the liquid surface and thc
floating roof.
“Vapor recovery system” means a vapor gathering system
capable of collecting all VON vapors and gases
discharged from the otorage
tank
and a vapor disposal
system capable of processing such VON vapors and gases
s-a as to prevent their emission to the atmosphere.
“Vehicle” means a device by which any person or
property may be propelled, movcd,
or drawn upon a
highway, excepting a device moved exclusively by human
power or used exclusively upon stationary rails or
tracks.
“Vinyl coating” means any topcoat or printing ink
applied to vinyl coated fabric or vinyl sheets.
Vinyl
coating does not include plastisols.
“Vinyl coating facility” means a facility that includes
one or more vinyl coating line(s).
“Vinyl coating line” means a coating line in which any
protective,
decorative er functional coating is applied
onto vinyl coated fabric or vinyl sheets.
“Volatile organic liquid
(VOL)” means any substance
which
irs liquid at storage conditions and which
contains volatile organic compounds.
“Volatile organic material
(VON)
or volatile organic
compound (VOC)” means “volatile organic material (VON)
or volatile organic compound (VOC)”,
as that term is
defined in 35
Ill. Adm. Code Part 211.
-“-Volatile Petroleum Liquid” means any petroleum liquid
with a true vapor pressure that is greater than 1.5
psia
(78 millimeters of mercury)
at standard
conditions.
“Wash coat” means a coating containing binders which
seals wood surfaces, prevents undesired staining, and
controls penetration.
“Wastewater
(Oil/Water)
Ceparator” means any device or
piece of equipment which utilizes the difference in
density between oil and water to remove oil and
assooiu~caonesniczi.i.s trom waLer,
or
~nv
gcvice,
a flocculation tank or a clarifier, wnicn rcmov
~F~n1~um
derivcd oomoounds from waste water.

158
“Web” means a substrate which is printed in continuous
roll-fed presses.
-“-Wood furniture” means room furnishings including
eabinota (kitchen,
bath, and vanity), tables,
chairs,
beds,
sofas,
shutters, art objects, wood paneling, wood
-flooring,
and any other coated furnishings made of
wood,
wood composition,
or fabricated wood matcrials--
“Wood furniture coating facility” means a facility that
-includes -one or more wood furniture coating line(s).
“Wood furniture coating line” means a coating line in
which any protective, decorative, or functional coating
4~sapplied onto wood furniture.
Il-Woodworking” means thc shaping, sawing,
grinding,
smoothing,
polishing, and making into products of any
form or shape of wood.
The definitions of 35 Ill. Adm. Code 211 apply to this Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.105
Test Methods and Procedures
a)
Coatings, Inks and Fountain Solutions
The following test methods and procedures shall be used
to determine compliance of ~
applied coatings,
inks,
and fountain solutions with the limitations set forth
in this Part.
1)
Sampling:
Samples collected for analyses shall be
one—liter taken into a one—liter container at a
location and time such that the sample will be
representative of the coating as applied
(i.e.,
the sample shall include any dilution solvent or
other VOM added during the manufacturing process).
The container must be tightly sealed immediately
after the sample is taken.
Any solvent or other
VON added after the sample is taken must be
measured and accounted for in the calculations in
subsection
(a) (3)
of this Section.
For multiple
package coatings, separate samples of each
component shall be obtained.
A mixed sample shall
not be obtained as it will cure in the container.
Sampling procedures shall follow the guidelines
presented in:

159
A)
ASTM D3925—8l(1985)
standard practice for
sampling liquid paints and related pigment
coating. This practice is incorporated by
reference in Section 218.112 of this Part.
B)
ASTM E300-86 standard practice for sampling
industrial chemicals. This practice is
incorporated by reference in Section 218.112
of this Part.
2)
Analyses:
The applicable analytical methods
specified below shall be used to determine the
composition of coatings,
inks, or fountain
solutions as applied.
A)
Method 24 of 40 CFR 60, Appendix A,
incorporated by reference in Section 218.112
of this Part, shall be used to determine the
VON content and density of coatings.
If it
is demonstrated to the satisfaction of the
Agency and the USEPA that plant coating
formulation data are equivalent to Method 24
results, formulation data may be used.
In
the event of any inconsistency between a
Method 24 test and a facility’s formulation
data,
the Method 24 test will govern.
B)
Method 24A of 40 CFR Part 60, Appendix A,
incorporated by reference in Section 218.112
of this Part,
shall be used to determine the
VOM content and density of rotogravure
printing inks and related coatings.
If it is
demonstrated to the satisfaction of the
Agency and USEPA that the plant coating
formulation data are equivalent to Method 24A
results, formulation data may be used.
In
the event of any inconsistency between a
Method 24A test and a facility’s formulation
data, the Method 24A test will govern.
C)
The following ASTM methods are the analytical
procedures for determining VON:
i)
ASTM Dl475-85: Standard test method for
density of paint, varnish, lacquer and
related products.
This test method is
incorporated by reference in Section
218.112 of this Part.
ii)
ASTM D2369-87: Standard test method for
volatile content of a coating. This test

160
method is incorporated by reference in
Section 218.112 of this Part.
iii) ASTM D3792-86: Standard test method for
water content of water—reducible paints
by direct injection into a gas
chromatograph. This test method is
incorporated by reference in Section
218.112 of this Part.
iv)
ASTM D4017-81(1987):
Standard test
method for water content in paints and
paint materials by the Karl Fischer
method. This test method is incorporated
by reference in Section 218.112 of this
Part.
v)
ASTM D4457-85: Standard test method for
determination of dichloromethane and
1,1,1, trichloroethane in paints and
coatings by direct injection into a gas
chromatograph.
(The procedure
delineated above can be used to develop
protocols for any compounds specifically
exempted from the definition of VOM.)
This test method is incorporated by
reference in Section 218.112 of this
Part.
vi)
ASTM D2697-86: Standard test method for
volume non—volatile matter in clear or
pigmented coatings.
This test method is
incorporated by reference in Section
218.112 of this Part.
vii) ASTM D3980—87: Standard practice for
interlaboratory testing of paint and
related materials. This practice is
incorporated by reference in Section
218.112 of this Part.
viii)ASTM El80—85: Standard practice for
determining the precision data of ASTM
methods for analysis of and testing of
industrial chemicals. This practice
is
incorporated by reference in Section
218.112 of this Part.
ix)
ASTM D2372-85: Standard method of
separation of vehicle from solvent—
reducible paints. This method is

161
incorporated by reference in Section
218.112 of this Part.
D)
Use of an adaptation to any of the analytical
methods specified in subsections
(a) (2) (A),
(B), and
(C)
of this Section may not be used
unless approved by the Agency and USEPA.
An
owner or operator must submit sufficient
documentation for the Agency and USEPA to
find that the analytical methods specified in
subsections
(a) (2) (A),
(B), and
(C)
of this
Section will yield inaccurate results and
that the proposed adaptation is appropriate.
3)
Calculations:
Calculations for determining the
VON content, water content and the content of any
compounds which are specifically exempted from the
definition of VON of coatings, inks and fountain
solutions as applied shall follow the guidance
provided in the following documents-i-.:
A)
“A Guide for Surface Coating Calculation”,
EPA-340/1-86-016,
incorporated by reference
in Section 218.112 of this Part.
B)
“Procedures for Certifying Quantity of
Volatile Organic Compounds Emitted by Paint,
Ink and Other Coatings”
(revised June 1986),
EPA-450/3-84-0l9,
incorporated by reference
in Section 218.112 of this Part.
C)
“A Guide for Graphic Arts Calculations”,
August 1988, EPA-340/l-88-003,
incorporated
by reference in Section 218.112 of this Part.
b)
Automobile or Light-Duty Truck Test Protocol
fl
The protocol for testing, including determining
the transfer efficiency~of coating app1icators~
at primer surfacer operations and topcoat coating
operations at an automobile or light-duty truck
assembly facility source shall follow the
procedures in:”Protocol for Determining the Daily
Volatile Organic Compound Emission Rate of
Automobile and Light-Duty Truck Topcoat
Operations”
(“topcoat protocol”), December 1988,
EPA-450/3-88-018,
incorporated by reference in
Section 218.112 of this Part.
21
Prior to testing pursuant to the topcoat protocol,
the owner or operator of a coating operation
sublect to the topcoat or primer surfacer limit in

162
Sections 218.204(a) (2) or 218.204(a) (3)
shall
submit a detailed testing proposal specifying the
method bY which testing will be conducted and how
compliance will be demonstrated consistent with
the topcoat protocol.
The ~ro~osal shall include,
at a minimum,
a comprehensive elan (including a
rationale)
for determining the transfer efficiency
at each booth through the use of in-plant or pilot
testing, the selection of coatings to be tested
(for the purpose of determining transfer
efficiency)
including the rationale for coating
groupings, the method for determining the analytic
VON content of as applied coatings and the
formulation solvent content of as applied
coatings, and a description of the records of
coating VON content as applied and coating’s usage
which will be kept to demonstrate compliance.
Upon approval of the proposal by the Agency and
USEPA, the compliance demonstration for a coating
line may proceed.
c)
Capture System Efficiency Test Protocols
1)
Applicability
The requirements of subsection
(c) (2)
of this
Section shall apply to all VON emitting processes
emission units employing capture equipment
(e.g.,
hoods, ducts),
except those cases noted below.
A)
If a~source installsemission unit is
equipped with
(or uses)
a permanent total
enclosure
(PTE) that meets Agency and USEPA
specifications,
and which directs all VON to
a control device, then the sourceemission
unit is exempted from the requirements
described in subsection
(c) (2)
of this
Section.
The Agency and USEPA specifications
to determine whether a structure is
considered a PTE are given in Procedure T of
Appendix B of this Part.
In this instance,
the capture efficiency is assumed to be 100
percent and the oourc-cemission unit is still
required to measure control efficiency using
appropriate test methods as specified in
subsection
(d)
of this Section.
B)
If an source usesemission unit is equipped
with
(or uses) uses a control device designed
to collect and recover VON (e.g., carbon
adsorber),
an explicit measurement of capture
efficiency
is not necessary provided that the

163
conditions given below are met.
The overall
control of the system can be determined by
directly comparing the input liquid VOM to
the recovered liquid VON.
The general
procedure for use in this situation is given
in 40 CFR 60.433, incorporated by reference
in Section 218.112 of this Part, with the
following additional restrictions:
1)
The source must be able to equate
solvent usage with solvent recovery on a
24-hour (daily)
basis,
rather than a
30-day weighted average, within
72 hours
following the 24-hour period.
In
addition,
one of the following two
criteria must be met:
Unless otherwise
specified in subsection
(c) (1) (B) (ii)
below, the owner or operator shall
obtain data each operating day for the
solvent usage and solvent recovery to
permit the determination of the solvent
recovery efficiency of the system each
operating day using a 7—day rolling
period.
The recovery efficiency for
each operatin~day is computed as the
ratio of the total recovered solvent for
that day and the most recent prior
6
operating days to the total solvent
usage for the same 7—day period used for
the recovered solvent, rather than a 30—
day weighted average as given in 40 CFR
60.433 incorporated by reference at
Section 218.112 of this Part.
This
ratio shall be expressed as a
percentage.
The ratio shall be computed
within
72 hours following each 7-day
period.
A source that believes that the
7-day rolling period is not appropriate
may use an alternative multi—day rolling
period not to exceed 30 days, with the
approval of the A~encvand USEPA.
In
addition, the criteria in subsection
(C)_(1)
(B) (iii)
or subsection
(c) (1) (B) (iv) below must be met.
jjj..
The owner or operator of the source
en~a~edin printing located at 350 E.
22nd Street, Chicago, Illinois, shall
obtain data each operating day for the
solvent usage and solvent recovery to
permit the determination of the solvent
recovery efficiency of the sYstem each

iii)
i~1
164
-
an
operating day using a 14—day rolling
period.
The recovery efficiency for
each operating day is computed as the
ratio of the total recovered solvent for
that day and the most recent prior 13
operating daYs to the total solvent
usage for the same 14—day period used
for the recovered solvent, rather than a
30-day weighted average as given
in 40
CFR 60.433,
incorporated by reference in
Section 218.112 of this Part.
This
ratio shall be expressed as a
lercentaae.
The ratio shall be computed
within
17 daYs following each 14—day
period.
In addition, the criteria
in
subsection
(c) (1) (B) (iii)
or subsection
(c) (1) (B) (iv) below must be met,
44-)--iii)
The solvent recovery system
(i.e.,
capture and control system) must be
dedicated to a single coating line,
printing line,
or other discrete
activity
i-hM- 1w it~1f
ic
sublect
tr~
a~~1icable
VON
~
s~d~d,
process line (e.g.,
one process line
venting to a carbon adsorber system),
or
If the solvent recovery system controls
more than one coating line, printing
line or other discrete activity that by
itself is subiect to an applicable VON
emission standard, the overall control
(i.e.
the total recovered VON divided by
the sum of liquid VON input from all
lines and other activities venting to
the control system) must meet or exceed
the most stringent standard applicable
to anY line or other discrete activity
venting to the control svstem.multiplc
process lines, then the source must be
able to demonstrate that the overall
control
(i.c.,thc total recovered
solvent VON divided by the sum of liqu~
VON input to all process lines venting
to the control system) meets or exceeds
the most stringent standard applicable
any prnr~r’~
linr~
vr~nti-nci
tn
thc~
2)
Specific Requirements

165
The capture efficiency of a~process lineemissiori
unit shall be measured using one of the four
protocols given below.
Any error margin
associated with a test protocol may not be
incorporated into the results of a capture
efficiency test.
If these techniques are not
suitable for a particular process, then the source
may use an alternative capture efficiency protocol
may be used, provided that the alternative
protocol is approved by the Agency and approved by
the USEPA as a SIP revision.
A)
Gas/gas method using temporary total
enclosure
(TTE).
The Agency and USEPA
specifications to determine whether a
temporary enclosure is considered a TTE are
given in Procedure T of Appendix B of this
Part.
The capture efficiency equation to be
used for this protocol is:
CE
=
Gw/(Gw
+
Fw)
where:
CE
=
çeapture efficiency,
decimal
fraction~
Gw
=
~mass of VOM captured and delivered
to control device using a TTE~
Fw
=
~mass of fugitive VON that escapes
from a TTE.
Procedure G.2 contained in Appendix B of this
Part is used to obtain Gw.
Procedure Fl
in
Appendix B of this Part is used to obtain Fw.
B)
Liquid/gas method using TTE.
The Agency and
USEPA specifications to determine whether a
temporary enclosure
is considered a TTE are
given in Procedure T of Appendix B of this
Part.
The capture efficiency equation to be
used for this protocol is:
CE
=
(L
-
Fw)/L
where:
CE
=
Qeapture efficiency, decimal
fractioni

166
L
=
~mass of liquid VON input to
process emission unit
Fw
=
~mass of fugitive VON that escapes
from a TTE~
Procedure L contained in Appendix B of this
Part
is used to obtain L.
Procedure F.1 in
Appendix B of this Part is used to obtain Fw.
C)
Gas/gas method using the building or room
(building or room enclosure)~in which the
affected coating line, printing line or other
sourceemission unit
is located~as the
enclosure and in which “F” and “G” are
measured while operating only the affected
line or facilityemission unit.
All fans and
blowers
in the building or room must be
operated as they would under normal
production.
The capture efficiency equation
to be used for this protocol
is:
CE
=
G/(G
+
FB)
where:
CE
=
çeapture efficiency, decimal
fraction~
G
=
~mass of VOM captured and delivered
to control device~
FB
=
~mass of fugitive VOM that escapes
from building enclosure~
Procedure G.2 contained in Appendix B of this
Part is used to obtain G.
Procedure F.2 in
Appendix B of this Part is used to obtain FB.
D)
Liquid/gas method using the building or room
(building or room enclosure)~in which the
affected coating line, printing line or other
aourccemission unit is located~as the
enclosure and in which “F” and “L” are
measured while operating only the affected
line
or facilityemission unit.
All fans and
blowers in the building or room must be
operated as they would under normal
production.
The capture efficiency equation
to be used for this protocol
is:

167
CE
=
(L
-
FB)/L
where:
CE
=
~eapture efficiency, decimal
fraction~
L
=
~mass of liquid VON input to
process emission unit
FB
=
~mass of fugitive VOM that escapes
from building enclosure~
Procedure L contained in Appendix B of this
Part is used to obtain
L.
Procedure F.2
in
Appendix B of this Part is used to obtain FB.
3)
Recordkeeping and Reporting
A)
All affected faciliticsowners or operators
affected by this subsection must maintain a
copy of the capture efficiency protocol
submitted to the Agency and the USEPA on
file.
All results of the appropriate test
methods and capture efficiency protocols must
be reported to the Agency within sixty
(60)
days of the test date.
A copy of the results
must be kept on file with the source for a
period of three
(3)
years.
B)
If any changes are made to capture or control
equipment,
then the source is required to
notify the Agency and the USEPA of these
changes and a new test may be required by the
Agency or the USEPA.
C)
The source must notify the Agency 30 days
prior to performing any capture efficiency or
control test.
At that time,
the source must
notify the Agency which capture efficiency
protocol and control device test methods will
be used.
D)
Sources utilizing a PTE must demonstrate that
this enclosure meets the requirement given in
Procedure T
(in Appendix B of this Part)
for
a PTE during any testing of their control
device.

168
E)
Sources utilizing a TTE must demonstrate that
their TTE meets the requirements given in
Procedure T (in Appendix B of this Part)
for
a TTE during testing of their control device.
The source must also provide documentation
that the quality assurance criteria for a TTE
have been achieved.
d)
Control Device Efficiency Testing and Monitoring
1)
The control device efficiency shall be determined
by simultaneously measuring the inlet and outlet
gas phase VON concentrations and gas volumetric
flow rates in accordance with the gas phase test
methods specified in subsection
(f)
of this
Section.
2)
Any owner or operator~
~j
~Ihat uses an afterburner or carbon adsorber
to comply with any Section of this Part
Z~
shall use A~encvand USEPA approved
continuous monitoring equipment which
is
installed,
calibrated, maintained, and
operated according to vendor specifications
at all times the afterburner or carbon
adsorber is in use excePt as provided in
subsection
(d) (3) of this Section.
The
continuous monitoring equipment must monitor
the following parameters:
il
For each afterburner which does not have
a catalyst bed1 the ~combustion chamber
temperature of each afterburner.
s-)-
jjj
For each afterburner which has
a
catalyst bed, commonly known as a
catalytic afterburner, the ~emperature
rise across each catalytic afterburner
bed or VOM concentration of exhaust.
?~)-
iii) For each carbon adsorber, ~the VON
concentration of each carbon adsorption
bed exhaust or the exhaust of the bed
next in sequence to be desorbed.
~J
Of an automobile or light-duty truck Primer
surfacer operation or topcoat operation
•sublect to subsection
(d)(2)(A)
above,
shall
keep a separate record of the following data
for the control devices, unless alternative

169
provisions are set forth in a permit pursuant
to Title V of the Clean Air Act:
~
For thermal afterburners for which
combustion chamber temperature is
monitored, all 3—hour periods of
operation in which the average
combustion temperature was more than
28°C(50°F)below the average combustion
temperature measured during the most
recent performance test that
demonstrated that the operation was in
compliance.
jjj.
For catalytic afterburners for which
temperature rise is monitored.
all
3-hour periods of operation in which the
average gas temperature before the
catalyst bed is more than 28°C(50°F)
below the average gas temperature
immediately before the catalyst bed
measured during the most recent
Performance test that demonstrated that
the operation was in compliance.
iii)
For catalytic afterburners and carbon
adsorbers for which VON concentration is
monitored, all 3—hour periods of
operation during which the average VON
concentration or the reading of organics
in the exhaust gases is more than 20
Percent greater than the average exhaust
gas concentration or reading measured by
the organic monitoring device during the
most recent determination of the
recovery efficiency of a carbon adsorber
or_performance test for a catalytic
afterburner, which determination or test
demonstrated that the operation was in
compliance.
fl
An owner or operator that uses a carbon adsorber
to comply with Section 218.401 of this Part may
oPerate the adsorber during periods of monitoring
equipment malfunction, provided that:
~j
The owner or operator notifies in writing the
A~encvand UCEPA within,
10 daYs after the
conclusion of any
72 hour period during which
the adsorber is operated and the associated
monitoring equipment is not operational, of
such monitoring equipment failure and

170
provides the duration of the malfunction,
a
description of the repairs made to the
equipment, and the total to date of all hours
in_the_calendar year during which the
adsorber was operated and the associated
monitoring equipment was not operational
.~j
During such period of malfunction the
adsorber is operated using timed sequences as
the basis for periodic regeneration of the
adsorber
çj
The period of such adsorber operation does
not exceed 360 hours in any calendar year
without the approval of the Agency and USEPA
and
pj
The total
of all hours
in the calendar year
during which the adsorber was operated and
the associated monitoring equipment was not
operational shall be reported,
in writing, to
the Agency and UCEPA by January 31st of the
following calendar year.
e)
Overall Efficiency
1)
The overall efficiency of the emission control
system shall be determined as the product of the
capture system efficiency and the control device
efficiency or by the liquid/liquid test protocol
as specified in 40 CFR 60.433,
incorporated by
reference in Section 218.112 of this Part,
(and
revised by subsection
(c) (1) (B)
of this Section)
for each solvent recovery system.
In those cases
in which the overall efficiency is being
determined for an entire line, the capture
efficiency used to calculate the product of the
capture and control efficiency is the total
capture efficiency over the entire line.
2)
For coating lines which are both chosen by the
owner or operator to comply with Section
2l8.207~-a-)-jgj, (d),
(e),
(f),
or
(g)
of this Part
by the alternative in Section 218.207(b) (2) g~
this Part and meet the criteria allowing them to
comply with Section 218.207 of this Part instead
of Section 218.204 of this Part,
the overall
efficiency of the capture system and control
device, as determined by the test methods and
procedures specified in subsections
(c),
(d)
and
(e) (1) of this Section, shall be no less than the

171
equivalent overall efficiency which shall be
calculated by the following equation:
E
=
(VOMa
-
VON1
J
/VONa)
x 100
where:
E
=
Equivalent overall efficiency of the
capture system and control device as a
percentage~~j
VOMa
=
Actual VON content of
a coating, or the
daily-weighted average VON content of
two or more coatings
(if more than one
coating is used), as applied to the
subject coating line as determined by
the applicable test methods and
procedures specified in subsection
(a)
of this Section in units of kg VON/i
(lb VON/gal)
of coating solids as
applied,-j.
VON1
=
The VON emission limit specified in
Sections 218.207(a)
or
(b)
218.204 or
218.205 of this Part in units of kg
VON/i
(lb VON/gal)
of coating solids as
applied.
f)
Volatile Organic Material Gas Phase Source Test Methods
The methods in 40 CFR Part 60, Appendix A, incorporated
by reference
in Section 218.112 of this Part delineated
below shall be used to determine control device
efficiencies.
1)
40 CFR Part 60, Appendix A, Method
18,
25 or 25A,
incorporated by reference in Section 218.112 ~
this Part as appropriate to the conditions at the
site,
shall be used to determine VON
concentration.
Method selection shall be based on
consideration of the diversity of organic species
present and their total concentration and on
consideration of the potential presence of
interfering gases.
Except as indicated in
subsections
(f) (1) (A)
and
(B)
below,
the test
shall consist of three separate runs,
each lasting
a minimum of 60 mm, unless the Agency and the
USEPA determine that process variables dictate
shorter sampling times.

172
A)
When
the method is to be used to determine
the efficiency of a carbon adsorption system
with a common exhaust stack for all the
individual adsorber vessels, the test shall
consist of three separate runs, each
coinciding with one or more complete
sequences through the adsorption cycles of
all the individual adsorber vessels.
B)
When the method is to be used to determine
the efficiency of a carbon adsorption system
with individual exhaust stacks for each
adsorber vessel, each adsorber vessel shall
be tested individually.
The test for each
adsorber vessel shall consist of three
separate runs.
Each run shall coincide with
one or more complete adsorption cycles.
2)
40 CFR Part 60, Appendix A, Method
1 or
1A,
incorporated by reference in Section 218.112 g~.
this Part,
shall be used for sample and velocity
traverses.
3)
40 CFR Part
60, Appendix A, Method
2,
2A,
2C or
2D,. incorporated by reference in Section 218.112
of this Part,
shall be used for velocity and
volumetric flow rates.
4)
40 CFR Part 60, Appendix A, Method
3, incorporated
by reference in Section 218.112 of this Part,
shall be used for gas analysis.
5)
40 CFR Part
60, Appendix A, Method 4, incorporated
by reference in Section 218.112 of this Part,
shall be used for stack gas moisture.
6)
40 CFR Part 60, Appendix A, Methods
2,
2A,
2C,
2D,
3 and 4, incorporated by reference in Section
218.112 of this Part,
shall be performed,
as
applicable,
at least twice during each test run.
7)
Use of an adaptation to any of the test methods
specified in subsections
(f) (1),
(2),
(3),
(4),
(5) and
(6) of this Section may not be used unless
approved by the Agency and the USEPA on a case by
case basis.
An owner or operator must submit
sufficient documentation for the Agency and the
USEPA to find that the test methods specified in
subsections
(f)(1),
(2),
(3),
(4),
(5)
and
(6) ~
this Section will yield inaccurate results and
that the proposed adaptation is appropriate.

173
g)
Leak Detection Methods for Volatile Organic Material
Owners or operators required by this Part to carry out
a leak detection monitoring program shall comply with
the following requirements:
1)
Leak Detection Monitoring
A)
Monitoring shall comply with 40 CFR 60,
Appendix A, Method 21, incorporated by
reference in Section 218.112 of this Part.
B)
The detection instrument shall meet the
performance criteria of Method 21.
C)
The instrument shall be calibrated before use
on each day of its use by the methods
specified in Method 21.
D)
Calibration gases shall be:
i)
Zero air
(less than loppm of hydrocarbon
in air); and
ii)
A mixture of methane or n—hexane and air
at a concentration of approximately, but
no less than,
10,000 ppm methane or
n—hexane.
E)
The instrument probe shall be traversed
around all potential leak interfaces as close
to the interface as possible as described in
Method 21.
2)
When equipment
is tested for compliance with no
detectable emissions as required, the test shall
comply with the following requirements:
A)
The requirements of subsections
(g) (1) (A)
through
(g) (1) (E)
of this Section above shall
apply.
B)
The background level shall be determined as
set forth in Method 21.
3)
Leak detection tests shall be performed consistent
with:
A)
“APTI Course SI 417 controlling Volatile
Organic Compound Emissions from Leaking
Process
i1
EPA—450/2—82-0l5,

174
incorporated by reference in Section 218.112
of this Part.
B)
“Portable Instrument User’s Manual for
Monitoring VOC Sources”, EPA—340/1—86-015,
incorporated by reference in Section 218.112
of this Part.
C)
“Protocols for Generating Unit-Specific
Emission Estimates for Equipment Leaks of VOC
and VHAP”,
EPA—450/3-88—010, incorporated by
reference in Section 218.112 of this Part.
D)
“Petroleum Refinery Enforcement Manual”,
EPA-340/l-80-008,
incorporated by reference
in Section 218.122218.112 of this Part.
h)
Bulk Gasoline Delivery System Test Protocol
1)
The method for determining the emissions of
gasoline from
a vapor recovery system are
delineated in 40 CFR 60, Subpart XX, Section
60.503,
incorporated by reference in Section
218.112 of this Part.
2)
Other tests shall be performed consistent with:
A)
“Inspection Manual for Control of Volatile
Organic Emissions from Gasoline Marketing
Operations:
Appendix D”, EPA-340/1-80-012,
incorporated by reference in Section 218.112
of this Part.
B)
“Control of Hydrocarbons from Tank Truck
Gasoline Loading Terminals: Appendix A”,
EPA-450/2-77-026,
incorporated by reference
in
Section 218.112
of this Part.
1)
Notwithstanding other requirements of this Part, upon
request of the Agency where it is necessary to
demonstrate compliance,
an owner or operator of an
emission source unit which is subject to this Part
shall,
at his own expense, conduct tests
in accordance
with the applicable test methods and procedures
specific in this Part.
Nothing in this Section shall
limit the authority of the USEPA pursuant to the Clean
Air Act,
as amended, to require testing.
jI
Stage
II Gasoline Vapor Recovery Test Methods
The methods for determining the acceptable performance
of Stage II Gasoline Vapor Recovery System are

175
delineated in “Technical Guidance-Stage II Vapor
Recovery Systems for Control of Vehicle Refueling
Emissions at Gasoline Dispensing Facilities,” found at
EPA 450/3-91-022b and incorporated by reference in
Section 218.112 of this Part.
Specifically, the test
methods are as follows:
fl
Dynamic Backpressure Test is a test procedure used
to determine the pressure drop
(flow resistance)
throuah balance vapor collection and control
systems
(including nozzles, vapor hoses,
swivels,
dispenser piping and underground piping)
at
prescribed flow rates.
21
Pressure Decay/Leak Test is
a test procedure used
to quantify the vapor tightness of a vapor
collection and control system installed at
gasoline dispensing facilities.
fl
Liquid Blockage Test is
a test procedure used to
detect low points
in any vapor collection and
control system where condensate may accumulate.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.106
Compliance Dates
a)
Compliance with the requirements of all rules
is
required by July,
1991,
or September
1,
1991, for all
sources located in Cook,
DuPage, Kane,
Lake, McHenry or
Will Counties, consistent with the appropriate
provisions of Section 218.103 of this Part.
b)
Compliance with the requirements of this Part is
required by November 15,
1993,
for all sources located
in Aux Sable Township or Goose Lake Township in Grundy
County or in Oswego Township in Kendall County.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.107
Operation of Afterburners
The operation of any natural gas fired afterburner and capture
system used to comply with this Part is not required during the
period of November
1 of any year to April
1 of the following year
provided that the operation of such devices is not required for
purposes of occupational safety or health,
or for the control of
toxic substances,
odor nuisances,
or other regulated pollutants.

176
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.109
Vapor Pressure of Volatile Organic Liquids
a)
If the VOL consists of only
a single compound, the
vapor pressure shall be determined by ASTM Method
D2879—86 (incorporated by reference in Section 218.112
of this Part) or the vapor pressure may be obtained
from a published sourcepublication such as:
Boublik,
T.,
V.
Fried and E. Hala,
“The Vapor Pressure of Pure
Substances,” Elsevier Scientific Publishing
Co.., New
York (1973);
Perry’s Chemical Engineer’s Handbook,
McGraw-Hill Book Company (1984); CRC Handbook of
Chemistry and Physics, Chemical Rubber Publishing
Company
(1986-87); and Lange’s Handbook of Chemistry,
John A.
Dean,
editor, McGraw-Hill Book Company
(1985).
b)
If the VOL is a mixture, the vapor pressure shall be
determined by ASTM Method D2879-86 (incorporated by
reference in Section 218.112)
or by the following
equation:
n
Pvoi
E
Pi X~
i=1
where:
Pvoi
=
Total vapor pressure of the mixtureT~
n
=
Number of components in the mixture-~-j
i
=
Subscript denoting an individual
component-7-~
P1
=
Vapor pressure of a component determined
in accordance with Cubpart A of this
Partsubsection
(a)
of this Section
X1
=
Mole fraction of the component in the
total mixture.
(Source:
Amended at
Ill.
Reg.
_____,
effective
_____________
Section 218.110
Vapor Pressure of Organic Material or Solvent
a)
If the organic material or solvent consists of only a
single compound, the vapor pressure shall be determined
by ASTM Method D2879-86 (incorporated by reference in

177
Section 218.112 of this Part)
or the vapor pressure may
be obtained from a published source publication such
as:
Boublik,
T., V.
Fried and E. Hala,
“The Vapor
Pressure of Pure Substances,” Elsevier Scientific
Publishing Co., New York (1973); Perry’s Chemical
Engineer’s Handbook, McGraw-Hill Book Company
(1984);
CRC Handbook of Chemistry and Physics, Chemical Rubber
Publishing Company (1986-87); and Lange’s Handbook of
Chemistry,
John A. Dean, editor, McGraw-Hill Book
Company (1985).
b)
If the organic material or solvent is in a mixture made
up of both organic material compounds and compounds
which are not organic material, the vapor pressure
shall be determined by the following equation:
n
E
P~ Xj~
Pvom
=
i=l
n
Xj
1=1
where:
~om
=
Total vapor pressure of the portion of
the mixture which is composed of organic
material7j..
n
=
Number of organic material components in
the mixture-rI
i
=
Subscript denoting an individual
component~
Pi.
=
Vapor pressure of an organic material
component determined in accordance with
6-ubpart A of this Part subsection
(a)
of
this Section-rI
Xj~
=
Mole fraction of the organic material
component of the total mixture.
c)
If the organic material or solvent is in a mixture made
up of only organic material compounds, the vapor
pressure shall be determined by ASTM Method D2879-86
(incorporated by reference in Section 218.112 of this
Part)
or by the above equation.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

178
Section 218.111
Vapor Pressure of Volatile Organic Material
a)
If the VOM consists of only a single compound,
the
vapor pressure shall be determined by ASTM Method
D2879—86 (incorporated by reference
in Section 218.112
of this Part)
or the vapor pressure may be obtained
from
a published sourcepublication such as:
Boublik,
T.,
V.
Fried and E.
Hala,
“The Vapor Pressure of Pure
Substances,” Elsevier Scientific Publishing Co., New
York (1973); Perry’s Chemical Engineer’s Handbook,
McGraw-Hill Book Company
(1984); CRC Handbook of
Chemistry and Physics, Chemical Rubber Publishing
Company (1986-87); and Lange’s Handbook of Chemistry,
John A.
Dean,
editor, McGraw-Hill Book Company
(1985).
b)
If the VOM is in a mixture made up of both VOM
compounds and compounds which are not VON, the vapor
pressure shall be determined by the following equation:
n
E
P3
X1
~vom
=
i=l
n
z
x~
i=1
where:
P~
=
Total vapor pressure of the portion of
the mixture which
is composed of VONTI
n
=
Number of VON components in the
mixturel
I
=
Subscript denoting an individual
componentl
P3
=
Vapor pressure of a VON component
determined in accordance with Cubpart A
of this Part subsection
(a)
of this
Sect!on-~-j.
X1
=
Mole fraction of the VON component of
the total mixture.
c)
If the VON is in a mixture made up of only VOM
compounds, the vapor pressure shall be determined by
ASTM Method D2879-86
(incorporated by reference in
Section 218.112 of this Part)
or by the above equation.

179
(Source:
Amended at
Iii. Reg.
______,
effective
Section 218.112
Incorporations by Reference
The following materials are incorporated by reference and do not
contain any subsequent additions or amendments:
a)
American Society for Testing and Materials,
1916 Race
Street, Philadelphia, PA 19103:
1)
ASTN D2879—86
2)
ASTM D323—82
3)
ASTM D86—82
4)
ASTM D—369—69
(1971)
5)
ASTM D—396—69
6)
ASTM D2880—7l
7)
ASTM D—975—68
8)
ASTM D3925—81
(1985)
9)
ASTM E300—86
10)
ASTM D1475—85
11)
ASTM D2369—87
12)
ASTM D3792—86
13)
ASTM D4017—81
(1987)
14)
ASTM D4457—85
15)
ASTN D2697—86
16)
ASTM D3980—87
17)
ASTM El80—85
18)
ASTM D2372—85
19)
ASTM D97—66
20)
ASTM E—168—67
(1977)
21)
ASTM E—169.~i
22)
ASTM E—260~j~.
23)
ASTM D2504—83
24)
ASTM D2382—83
j~1.
ASTM D323-82
(approved 1982)
b)
Standard Industrial Classification Manual, published by
Executive Office of the President,
Office of Management
and Budget, Washington,
D.C.,
1987.
c)
American Petroleum Institute Bulletin 2517,
“Evaporation Loss From Floating Roof Tanks”,
Second
ed., February,
1980.
d)
40 CFR Part
60
(July
1,
19901991) and 40 CFR 60,
Appendix A,
Method 24
(57 FR 30654, July 10,
1992).
e)
40 CFR Part 61
(July
1,
19901991)
f)
40 CFR Part 50
(July
1,
19801991).

180
g)
40 CFR Part 51
(July
1,
19891991).
h)
40 CFR Part 52
(July
1,
19891991).
fl
40 CFR Part 80
(July
1,
1991).
#)-jj~. “A Guide for Surface Coating Calculation”, United
States Environmental Protection Agency, Washington,
D.C.,
EPA—340/1—86—0l6.
~-)-~j“Procedures for Certifying Quantity of Volatile Organic
Compounds Emitted by Paint, Ink and Other Coating”,
(revised June 1986),
United States Environmental
Protection Agency, Washington D.C.,
EPA—450/3—84-0l9.
~-)-fl“A Guide for Graphic Arts Calculations”, August 1988,
United States Environmental Protection Agency,
Washington D.C., EPA—340/1—88—003.
~--~j“Protocol for Determining the Daily Volatile Organic
Compound Emission Rate of Automobile and Light-Duty
Truck Topcoat Operations”, December 1988.
United States
Environmental Protection Agency, Washington D.C.,
EPA—450/3—88—018.
m-)-ifl. “Control of Volatile Organic Emissions from
Manufacturing of Synthesized Pharmaceutical Products”,
United States Environmental Protection Agency,
Washington,
D.C., EPA—450/2—78—029.
-~j“Control of Volatile Organic Compound Leaks from
Gasoline Tank Trucks and Vapor Collection Systems”,
Appendix B, United States Environmental Protection
Agency,
Washington,
D.C.,
EPA—450/2—78—05l.
efpj “Control
of Volatile Organic Compound Emissions from
Large Petroleum Dry Cleaners”, United States
Environmental Protection Agency, Washington, D.C.,
EPA—450/3—82—009.
~
“APTI Course S1417 Controlling Volatile Organic
Compound Emissions from Leaking Process EquiPment”,
United States Environmental Protection Agency,
Washington,
D.C.,
EPA—450/2—82—015.
~
“Portable Instrument User’s Manual for Monitoring VOC
Sources”, United States Environmental Protection
Agency. Washington,
D.C.,
EPA-340/l—86—015.
~j
“Protocols for Generating Unit—Specific Emission
Estimates for Equipment Leaks of VOC and VHAP”,
United

181
States Environmental Protection Agency. Washington,
D.C.
,
EPA—450/3—88—010.
~j
“Petroleum Refinery Enforcement Manual”, United States
Environmental Protection Agency, Washington,
D.C.,
EPA—340/1—80—008.
~j
“Inspection Manual for Control of Volatile Organic
Emissions from Gasoline Marketing Operations:
Appendix
D”, United States Environmental Protection Agency,
Washington,
D.C..
EPA—340/l—80—012.
yj
“Control of Hydrocarbons from Tank Truck Gasoline
Loading Terminals:
Appendix A”, United States
Environmental Protection Agency, Washington,
D.C.,
EPA—450 /2—77—026.
~jj..“Technical Guidance—Stage II Vapor RecoverY Systems for
Control of Vehicle Refueling Emissions at Gasoline
Dispensing Facilities”, United States Environmental
Protection Agency, Washington, D.C., EPA-450/3—91—022b.
~çj
California Air Resources Board,
Compliance Division.
Compliance Assistance Program:
Gasoline Marketing and
Distribution:
Gasoline Facilities Phase
I
& II
(October 1988. rev. March 1991)
(CARB Manual).
(Source:
Amended at
Ill. Reg.
______,
effective
____________
SUBPART
B:
ORGANIC EMISSIONS FROM STORAGE
AND
LOADING OPERATIONS
Section 218.121
Storage Containers
No person shall cause or allow the storage of any VOL with a
vapor pressure of 17.24 kPa
(2.5 psia)
or greater at 294.3~K
(70°F) or any gaseous organic material in any stationary tank,
reservoir or other container of more than 151 cubic meters
(40,000 gal)
capacity unless such tank, reservoir or other
container:
a)
Is a pressure tank capable of withstanding the vapor
pressure of such liquid or the pressure of the gas,
so
as to prevent vapor or gas loss to the atmosphere at
all times;
or,
b)
Is designed and equipped with one of the following
vapor loss control devices:
1)
A floating roof which rests on the surface of the
VOL and is equipped with a closure seal or seals
between the roof edge and the tank wall.
Such

182
floating roof shall not be permitted if the VOL
has a ‘~.rapor pressure of 86.19 kPa (12.5 psia)
or
greater at 294.3°K(70°F). No person shall cause
or allow the emission of air contaminants into the
atmosphere from any gauging or sampling devices
attached to such tanks,
except during sampling or
maintenance operations.
2)
A vapor recovery system consisting of:
A)
A vapor gathering system capable of
collecting 85
or more of the uncontrolled
VON that would be otherwise emitted to the
atmosphere;
and,
B)
A vapor disposal system capable of processing
such VON so as to prevent its emission to the
atmosphere.
No person shall cause or allow
the emission of air contaminants into the
atmosphere from any gauging or sampling
devices attached to such tank, reservoir or
other container except during sampling.
3)
Other equipment or means of equal efficiency
approved by the Agency according to the provisions
of 35 Ill.
Adm. Code 201, and further processed
consistent with Section 218.108.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.122
Loading Operations
a)
No person shall cause or allow the discharge of more
than 3.6 kg/hr
(8 lbs/hr)
of organic material into the
atmosphere during the loading of any organic material
from the aggregate loading pipes of any loading
facility area having through-put of greater than 151
cubic meters per day (40,000 gal/day)
into any railroad
tank car, tank truck or trailer unless such loading
facilityarea is equipped with submerged loading pipes,-
submerged fill or a device that is equally effective in
controlling emissions and is approved by the Agency
according to the provisions of
35
Ill. Adm. Code 201,
and further processed consistent with Section 218.108.
b)
No person shall cause or allow the loading of any
organic material into any stationary tank having a
storage capacity of greater than 946
1
(250 gal),
unless such tank is equipped with a permanent submerged
loading pipe,
submerged fill or an equivalent device
approved by the Agency according to the provisions of

183
35 Ill.
Adm. Code 201,
and further processed consistent
with Section 218.108 of this Part, or unless such tank
is a pressure tank as described in Section 218.121(a)
of this Part or is fitted with a recovery system as
described in Section 218.121(b) (2)
of this Part.
c)
Exception:
If no odor nuisance exists the limitations
of this Section shall only apply to the loading of VOL
with a vapor pressure of 17.24 kPa (2.5 psia)
or
greater at 294.3°K(70°F).
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.123
Petroleum Liquid Storage Tanks
a)
The requirements of subsection
(b)
of this Section
shall not apply to any stationary storage tank:
1)
Equipped before January
1,
1979 with one of the
vapor loss control devices specified in Section
218.121(b)
of this Part, except Section
218.121(b) (1)
of this Part
2)
With a capacity of less than 151.42 cubic meters
(40,000 gal);
3)
With a capacity of less than 1,600 cubic meters
(422,400 gal) and used to store produced crude oil
and condensate prior to custody transfer;
4)
With a capacity of less than 1,430 cubic meters
(378,000 gal) and used to store produced oil or
condensate in crude oil gathering;
5)
Subject to new source performance standards for
storage vessels of petroleum liquid,
35 Ill.
Adm.
Code 230 40 CFR
60, as regulations promulgated by
the U.S. Environmental Protection Agency under
Section 111 of the Clean Air Act
(42 USC 7411), as
amended.
THE PROVISIONS OF SECTION 111 OF THE
CLEAN AIR ACT
...
ARE APPLICABLE IN THIS STATE AND
ARE ENFORCEABLE UNDER
ITHE ENVIRONMENTAL
PROTECTION ACT1
(Ill. Rev.
Stat.
1991,
ch. l11~,
Par.
1009.1(b))
1415 ILCS 5/9.1(b))
6)
In which volatile petroleum liquid is not stored;
or
7)
Which is
a pressure tank as described in Section
218.121(a)
of this Part.

184
b)
Subject to subsection
(a)
of this Section no owner or
operator of a stationary storage tank shall cause or
allow the storage of any volatile petroleum liquid
in
the tank unless:
1)
The tank is equipped with one of the vapor loss
control devices specified in Section 218.121(b) Q~
this Part
2)
There are no visible holes, tears or other defects
in the seal or any seal fabric or material of any
floating roof;
3)
All openings of any floating roof deck, except
stub drains, are equipped with covers,
lids or
seals such that:
A)
The cover,
lid or seal is in the closed
position at all times except when petroleum
liquid is transferred to or from the tank;
B)
Automatic bleeder vents are closed at all
times except when the roof is floated off or
landed on the roof leg supports; and
C)
Rim vents,
if provided, are~setto open when
the roof
is being floated off the roof leg
supports or at the manufacturer’s recommended
setting;
4)
Routine inspections of floating roof seals are
conducted through roof hatches once every six
months;
5)
A complete inspection of the cover and seal of any
floating roof tank is made whenever the tank is
emptied for reasons other than the transfer of
petroleum liquid during the normal operation of
the tank,
or whenever repairs are made as a result
of any semi—annual inspection or incidence of roof
damage or defect; and
6)
A record of the results of each inspection
conducted under subsection
(b) (4)
or
(b) (5) ~
this Section
is maintained.
a)
Owners and operators of petroleum liquid storage
were required to have compliance schedules as
summarized
in Appendix C to 35 Ill Adm. Code 215.
(Source:
Amended at
Ill.
Reg.
______,
effective
______

185
Section 218.124
External Floating Roofs
a)
In addition to meeting the requirements of Section
218.123(b) of this Part, no owner or operator of a
stationary storage tank equipped with an external
floating roof shall cause or allow the storage of any
volatile petroleum liquid in the tank unless:
1)
The tank has been fitted:
~j
w~itha continuous secondary seal extending
from the floating roof to the tank wall
(rim
mounted secondary seal), or
~j
With aAny other device which controls VON
emissions “ith an effectiveness equal to or
greater than
a rim mQunLcu secondary
seal;equipment or means
of egual efficiency
approved by the Agency according to the
provisions of 35
Ill. Adm. Code 201,
and
further processed consistent with Section
218.108 of this Part
2)
Each seal closure device meets the following
requirements:
A)
The seal
is intact and uniformly in place
around the circumference of the floating roof
between the floating roof and tank wall;
and
B)
The accumulated area of gaps exceeding 0.32
centimeter
(1/8 inch)
in width between the
secondary seal and the tank wall shall not
exceed 21.2 square centimeters per meter of
tank diameter
(1.0 square inches per foot of
tank diameter).
Compliance with this
requirement shall be determined by:
fl
Physically measuring the length and
width of all gaps around the entire
circumference of the secondary seal
in
each place where a 0.32 cm (0.125 in.)
uniform diameter Probe passes freely
(without forcing or binding against the
seal)
between the seal and the tank
wall; and
£jJ
Summing the area of the individual gaps.
3)
Emergency roof drains are provided with slotted
membrane fabric covers or equivalent covers across
at least
90 percent of the area of the opening;

186
4)
Openings are equipped with projections into the
tank which remain below the liquid surface at all
times;
5)
Inspections are conducted prior to May
1 of each
year to insure compliance with subsection
(a) ~
this Section
6)
The secondary seal gap is measured prior to May
1
of each yearf and within 30 days of a written
request to demonstrate compliance with subsection
(2) (B)
of this Section
7)
Records of the types of volatile petroleum liquid
stored, the maximum true vapor pressure of the
liquid as stored, the results of the inspections
and the results of the secondary seal gap
measurements are maintained and available to the
Agency, upon verbal or written request,
at any
reasonable time for a minimum of two years after
the date on which the record was made.
b)
Subsection
(a)
above does not apply to any stationary
storage tank equipped with an external floating roof:
1)
Exempted under Section 218.123(a) (2) through
218.123(a) (6)
of this Part
2)
Of welded construction equipped with a metallic
type shoe seal having a secondary seal from the
top of the shoe seal to the tank wall
(shoe—mounted secondary seal);
3)
Of welded construction equipped with a metallic
type shoe seal,
a liquid—mounted foam seal,
a
liquid-mounted liquid-filled-type seal, or other
closure device of equivalent control efficiency
approved by the Agency in which a petroleum liquid
with a true vapor pressure less than 27.6 kPa
(4.0
psia)
at 294.3°K(70°F)
is stored; or
4)
Used to store crude oil with a pour point of 50°F
or higher as determined by ASTM Standard D97-66
incorporated by reference in Section 218.112 ~
this Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
___________
Section 218.125
Compliance Dates
(Repealed)

187
Every owner or operator of ~n cmission source subject to 35 Ill.
Adm. Code 215,
Cubpart B,
as of December 31,
1987 shall have
complied with its standards and limitations by December 31,
1987-i-
(Source:
Repealed at
Ill. Reg.
______,
effective
Section 218.126
Compliance Plan (Repealed)
a)
The owner or operator of an emission source previously
subject to Ceotion 215.125 shall have submitted to the
Agency a compliance plan as required by 35
Ill.
Adm.
Code 201.241, including a project completion schedule
where applicable, no later than April 21,
1983.
b)
Unless the submitted compliance plan or schedule was
disapproved by the Agency, the owner or operator of
a
facility or emission source subject to the rules
specified in subsection
(a) may operate the emission
source according to the plan and schedule as submitted.
r~)
The plan
r~nc~
ht-~tin1r~~-*hn11
mr~r~t
thi~
~rrn1~-r-’mr’
4-
iii.
AWU.
~oae
~Ui.~4i.
including specific interim dates
as required in
35 Ill. Adm. Code 201.242.
—4~
(Source:
Repealed at
Ill. Reg.
______,
effective
________
SUBPART C:
ORGANIC EMISSIONS FROM MISCELLANEOUS EQUIPMENT
Section 218.141
Separation Operations
a)
No person shall use any single or multiple compartment
effluent water separator which receives effluent water
containing 757 1/day
(200 gal/day) or more of organic
material from any equipment processing,
refining,
treating, storing or handling organic material unless
such effluent water separator is equipped with air
pollution control equipment capable of reducing by 85
percent or more the uncontrolled organic material
emitted to the atmosphere.
Exception:
If no odor
nuisance exists the limitations of this subsection
shall not apply if the vapor pressure of the organic
material
is below 17.24 kPa
(2.5 psia)
at 294.3°K
(70°F)
b)
Subsection
(a)
of this Section shall not apply to water
and crude oil separation in the production of Illinois
crude oil,
if the vapor pressure of such crude oil
is
less than 34.5 kPa
(5 psia).

188
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.143
Vapor Blowdown
No person shall cause or allow the emission of organic material
into the atmosphere from any vapor blowdown system or any safety
relief valve,
except such safety relief valves not capable of
causing an excessive release, unless such emission is controlled:
a)
To 10 ppm equivalent methane (molecular weight 16.0)
or
less;
or,
b)
By combustion in a smokeless flare;
or,
C)
By other air pollution control equipment approved by
the Agency according to the provisions of
35 Ill.
Adm.
Code 201,
and further processed consistent with Section
218.108 of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.144
Safety Relief Valves
Section 218.143 of this Part shall not apply to any set of
unregulated safety relief valves capable of causing excessive
releases, provided the owner or operator thereof, by October
1,
1972,
supplied the Agency with the following:
a)
A historical record of each such set
(or,
if such
records were unavailable,
of similar sets which,
by
virtue of operation under similar circumstances, may
reasonably have been presumed to have the same or
greater frequency of excessive releases)
for a three-
year period immediately preceding October
1,
1972,
indicating:
1)
Dates on which excessive releases occurred from
each such set; and
2)
Duration in minutes of each such excessive
release; and
3)
Quantities
(in pounds)
of mercaptans and/or
hydrogen sulfide emitted into the atmosphere
during each such excessive release.
b)
Proof, using such three—year historical records, that
no excessive release is likely to occur from any such
set either alone or
in combination with such excessive
releases from other sets owned or operated by the same

189
person and located within a ten-mile radius from the
center point of any such set, more frequently than
3
times
in any 12 month period;
c)
Accurate maintenance records pursuant to the
requirements of subsection
(a)
of this Section
and,
d)
Proof,
at three—year intervals,
using such three—year
historical records, that such set conforms to the
requirements of subsection
(c)
of this Section.
(Source:
Amended at
Ill.
Reg.
______,
effective
__________
______________________)
SUBPART
E:
SOLVENT CLEANING
Section 218.181
Solvent Cleaning in General
The requirements of this Subpart shall apply to all cold
cleaning, open top vapor degreasing,
and conveyorized degreasing
operations which use volatile organic materials.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
Section 218.182
Cold Cleaning
a)
Operating Procedures:
No person shall operate a cold
cleaning degreaser unless:
1)
Waste solvent is stored in covered containers only
and not disposed of in such a manner that more
than 20
of the waste solvent (by weight)
is
allowed to evaporate into the atmosphere;
2)
The cover of the degreaser is closed when parts
are not being handled; and
3)
Parts are drained until dripping ceases.
b)
Equipment Requirements:
No person shall operate a cold
cleaning degreaser unless:
1)
The degreaser is equipped with a cover which
is
closed whenever parts are not being handled in the
cleaner.
The cover shall be designed to be easily
operated with one hand or with the mechanical
assistance of springs, counter—weights or a
powered system if:

190
A)
The solvent vapor pressure
is greater than 2
kPa
(15
itunHg or 0.3 psi) measured at 38°C
(100°F);
B)
The. solvent is agitated; or
C)
The solvent is heated above ambient room
temperature.
2)
The degreaser is equipped with a facilitydevice
for draining cleaned parts. The drainage facility
device shall be constructed so that parts are
enclosed under the cover while draining unless:
A)
The solvent vapor pressure is less than 4.3
kPa
(32
mmHg
or 0.6 psi) measured at 38°C
(100°F);or
B)
An internal drainage facilitydevice cannot be
fitted into the cleaning system,
in which
case the drainage facilitydevice may be
external.
3)
The degreaser is equipped with one of the
foLlowing control devices
if the vapor pressure of
the solvent is greater than 4.3 kPa
(32
mmHg
or
0.6 psi) measured at 38°C(100°F)or if the
solvent is heated above 50°C(120°F)or its
boiling point:
A)
A freeboard height of 7/10 of the inside
width of the tank or 91 cm
(36 in), whichever
is less; or
B)
Any other equipment or system of equivalent
emission control as approved by the Agency
and further processed consistent with Section
218.108 of this Part.
Such a system may
include a water cover,
refrigerated chiller
or carbon adsorber.
4)
A permanent conspicuous label summarizing the
operating procedure is affixed to the degreaser;
and
5)
If a solvent spray
is used, the degreaser is
equipped with a solid fluid stream spray,
rather
than a fine,
atomized or shower spray.
(Source:
Amended at
Ill. Reg.
______,
effective
__________

191
Section 218.183
Open Top Vapor Degreasing
a)
Operating Requirements: No person shall operate an open
top vapor degreaser unless:
1)
The cover of the degreaser is closed when
workloads are not being processed through the
degreaser;
2)
Solvent carryout emissions are minimized by:
A)
Racking parts to allow complete drainage;
B)
Moving parts
in and out of the degreaser at
less than 3.3 m/min
(11 ft/mm);
C)
Holding the parts
in the vapor zone until
condensation ceases;
D)
Tipping out any pools of solvent on the
cleaned parts before removal from the vapor
zone;
~
E)
Allowing parts to dry within the degreaser
until visually dry.
3)
Porous or absorbent materials,
such as cloth,
leather, wood or rope are not degreased;
4)
Less than half of the degreaser’s open top area is
occupied with a workload;
5)
The degreaser is not loaded to the point where the
vapor level would drop more than 10 cm
(4
in) when
the workload is removed from the vapor zone;
6)
Spraying is done below the vapor level only;
7)
Solvent leaks are repaired immediately;
8)
Waste solvent is stored in covered containers only
and not disposed of in such a manner that more
than 20
of the waste solvent (by weight)
is
allowed to evaporate into the atmosphere;
9)
Water is not visually detectable in solvent
exiting from the water separator; and
10)
Exhaust ventilation exceeding 20 cubic meters per
minute per square meter
(65 cubic feet per minute
per square foot)
of degreaser open area is not

192
used, unless necessary to meet the requirements of
the Occupational Safety and Health Act
(29 U.S.C.
Section 651 et seq.).
b)
Equipment Requirements: No person shall operate an open
top vapor degreaser unless:
1)
The degreaser is equipped with a cover designed to
open and close easily without disturbing the vapor
zone;
2)
The degreaser is equipped with the following
switches:
A)
A dcviceQ~which shuts off the sump heat
source if the amount of condenser coolant
is
not sufficient to maintain the designed vapor
level; and
B)
A dcvice~ which shuts off the spray pump if
the vapor level drops more than 10 cm
(4
in)
below the bottom condenser coil; and
C)
A dcviceQj~which shuts off the sump heat
source when the vapor level exceeds the
design level.
3)
A permanent conspicuous label summarizing the
operating procedure is affixed to the degreaser;
4)
The degreaser is equipped with one of the
following devices:
A)
A freeboard height of 3/4 of the inside width
of the degreaser tank or 91 cm
(36 in),
whichever is
less;
and if the degreaser
opening is greater than
1 square meter
(10.8
square feet),
a powered or mechanically
assisted cover; or
B)
Any other equipment or system of equivalent
emission control as approved by the Agency
and further processed consistent with Section
218.108 of this Part.
Such equipment or
system may include a refrigerated chiller,
an
enclosed design or a carbon adsorption
system.
(Source:
Amended at
Ill. Reg.
______,
effective
____________

193
Section 218.184
Conveyorized Degreasing
a)
Operating Requirements:
No person shall operate
a
conveyorized degreaser unless:
1)
Exhaust ventilation exceeding 20 cubic meters per
minute per square meter
(65 cubic feet per minute
per square foot)
of area of loading and unloading
opening is not used, unless necessary to meet the
requirements of the Occupational Safety and Health
Act
(29 U.S.C. Section 651 et seq.);
2)
Solvent carryout emissions are minimized by:
A)
Racking parts for best drainage; and
B)
Maintaining the vertical conveyor speed
at
less than 3.3 m/min
(11 ft/mm);
3)
Waste solvent is stored in covered containers only
and not disposed of in such a manner that more
than 20
of the waste solvent
(by weight)
is
allowed to evaporate into the atmosphere;
4)
Solvent leaks are repaired immediately;
5)
Water is not visually detectable in solvent
exiting from the water separator;
and
6)
Downtime covers are placed over entrances and
exits of conveyorized degreasers immediately
aftE
the conveyors and exhausts are shut down and not
removed until just before start—up.
b)
Equipment Requirements:
No person shall operate a
conveyorized degreaser unless:
1)
The degreaser is equipped with a drying tunnel,
rotating (tumbling)
basket or other equipment
sufficient to prevent cleaned parts from carrying
out solvent liquid or vapor;
2)
The degreaser is equipped with the following
switches:
A)
A deviceOne which shuts off the sump heat
source if the amount of condenser coolant is
not sufficient to maintain the designed vapor
level;
B)
A dcviccOne which shuts off the spray pump or
the conveyor if the vapor level drops more

194
than 10 cm
(4
in) below the bottom condenser
coil; and
C)
A deviceQfl~which shuts off the sump heat
source when the vapor level exceeds the
design level~~
3)
The degreaser is equipped with openings for
entrances and exits that silhouette workloads so
that the average clearance between the parts and
the edge of the degreaser opening is less than 10
cm
(4
in)
or less than 10 percent of the width of
the opening;
4)
The degreaser
is equipped with downtime covers for
closing off entrances and exits when the degreaser
is shut down; and
5)
The degreaser is equipped with one of the
following control devices,
if the air/vapor
interface
is larger than 2.0 square meters
(21.6
square feet):
A)
A carbon adsorption system with ventilation
greater than or equal to 15 cubic meters per
minute per square meter
(50 cubic feet per
minute per square foot)
of air/vapor area
when downtime covers are open,
and exhausting
less than 25 ppm of solvent by volume
averaged over a complete adsorption cycle; or
B)
Any other equipment or system of equivalent
emission control as approved by the Agency,
and further processed consistent with Section
218.108 of this Part.
Such equipment or
system may include a refrigerated chiller.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.185
Compliance Schedule
(RePealed)
_1_~
I
prcviouslyexcmptfrointhe
rcquircrnentsof
CubpartEof
35
Ill.
Adin.
Code 215
(Cections 215.182 215.184) because it satisfied the
criteria
in either 35
Ill. Adm.
Code 215.181(a)
or
35 Ill.
Adm.
Code 215.181(b),
shall comply with the requirements of this
Cubpart on and after a date consistent with Section 218.106.
A
source which did not satisfy the criteria in either
35
Ill.
Adin.
Code 215.181(a)
or 35 Ill.
Adm. Code 215.181(b)
shall comply with
the requirements of this Cubpart upon adoption.

195
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
Section 218.186
Test Methods
The following test methods shall be used to demonstrate
compliance with this Subpart:
a)
Vapor pressures shall be determined by using the
procedure specified in Section 218.110 of this Part.
b)
Exhaust ventilation rates shall be determined by using
the procedures specified in Section 218.105(f) (3)
of
this Part.
c)
The performance of control devices shall be determined
by using the procedures specified in Section 218.105(f)
of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
SUBPART
F:
COATING OPERATIONS
Section 218.204
Emission Limitations
for
Nanufaoturing Plants
Except as provided
in Sections 218.205, 218.207 and 218.208
of
this Part,
no owner or operator of a coating line shall apply at
any time any coating in which the VON content exceeds the
following emission limitations for the specified coating.
The
following emission limitations are expressed in units
of VOM per
volume of coating (minus water and any compounds which are
specifically exempted from the definition of VON)
as applied at
each coating applicator,
except where noted.
Compounds which are
specifically exempted from the definition of VON should be
treated as water for the purpose of calculating the “less water”
part of the coating composition.
Compliance with this Subpart
must be demonstrated through the applicable coating analysis test
methods and procedures specified in Section 218.105(a) of this
Part and the recordkeeping ahd reporting requirements specified
in Section 218.211(c) of this Part except where noted.
(Note:
The equation presented in Section 218.206 of this Part shall be
used to calculate emission limitations for determining compliance
by add—on controls, credits for transfer efficiency,
emissions
trades and cross-line averaging.)
The emission limitations are
as follows:
a)
Automobile or Light-Duty
kg/l
lb/gal
Truck Coating
1)
Prime coat
0.14
(1.2)

196
2)
Primer surfacer coat
p.341.81
(2-r&l5.1)
(Note:
The priiue~surfacer coat limitation is
based upon a transfer efficiency of 30 percent.
The usc of tran3fcr efficiency credits can be
allowed only if approved by the Agency and
approved by the UCEPA as a SIP revision in units
of kg
(lbs) of VOM Per
1
(aal)
of coating solids
deposited.
Compliance with the limitation shall
be based on the daily—weighted average from an
entire primer surfacer operation.
Compliance
shall be demonstrated in accordance with the
topcoat Protocol referenced in Section 218.105(b)
and the recordkeeping and reporting requirements
specified in Section 218.211(f).
Testing to
demonstrate compliance shall be Performed in
accordance with the topcoat Protocol and a
detailed testing proposal aPProved by the Agency
and USEPA specifying the method of demonstrating
compliance with the protocol. Section 218.205 does
not apply to the primer surfacer limitation.)
kg/l
lb/gal
3)
Topcoat
1.81
(15.1)
(Note:
The topcoat 1imitation~is in units of kg
(lbs)
of VON per
1
(gal)
of coating solids
deposited.
Compliance with the limitation shall
be based on the daily-weighted average VON content
from #~e~entire topcoat operation (all topcoat
spray booths,
flash—off areas and bake ovens)-.
Compliance shall be demonstrated in accordance
with the topcoat protocol for automobiles and
light-duty trucks referenced in Section 218.105(b)
of this Part and the recordkeeping and reporting
requirements specified in Section 218.211(f).
Testing to demonstrate compliance shall be
Performed in accordance with the topcoat Protocol
Section 218.205 does not apply to the topcoat
limitation.)
At least 180 days prior to the
initial compliance date,
the owner or operator of
a coating line subject to the topcoat limitation
shall have submitted to the UCEPA a detailed
testing proposal approved by the Agency and USEPA
specifying the method of demonstrating compliance
with the protocol.
The proposal shall have
included,
at a minimum,
a comprehensive plan
-(including a rationale)
for determining the
transfár efficiency at each booth through the use
of in-plant,
or pilot testing;
the selection of
coatings to be tested
(for the purposc of
determining transfer efficiency)
including
th-e

197
rationale for coating groupings; and the method
for determining the analytic VON content of ac
applied coatings and the formulation solvent
~.
~
coatings.
Upon approval of
the protocol by the UCEPA,
the souroc may proceed
t7ith the
ciomniianoc?
demonstration.
Section
apply to the topcoat
218.205 of thi~Part
ir~~
nnt~
limitation.)
kg/i
1)
Sheet basecoat and
overvarnish
0.34
2)
Exterior basecoat and
overvarnish
0.34
3)
Interior body spray coat 0.51
(4.2)
4)
Exterior end coat
0.51
5)
Side seam spray coat
0.66
6)
End sealing compound coato.44
(3.7)
c)
Paper Coating
(Note:
The paper coating limitation shall not apply to
any owner or operator of any paper coating line on
which printing is performed if the paper coating line
complies with the emissions limitations in Subpart H:
Printing and Publishing,
Sectione 218.401 of this Part
through 218.404.)
d)
Coil Coating
0.35
0.45
g)
Metal Furniture Coating
0.36
h)
Large Appliance Coating
0.34
(Note:
The limitation shall not apply to the use of
quick-drying lacquers for repair of scratches and nicks
that occur during assembly, provided that the volume of
4)
Final repair coat
b)
Can Coating
kg/1
0.58
lb/gal
(4.8)
lb/gal
(2.8)
(2.8)
(4.2)
(5.5)
kg/1
0.35
lb/gal
(2.9)
e)
Fabric Coating
f)
Vinyl Coating
kg/i
0.31
lb/gal
(2.6)
(2.9)
(3.8)
(3.0)
(2.8)

198
coating does not exceed 0.9~
i
~i
quarc~ in any one
roiling eight-hour period.)
kg/i
lb/gal
i)
Magnet Wire Coating
0.20
(1.7)
j)
Miscellaneous Metal Parts and
Products Coating
1)
Clear coating
0.52
(4.3)
2)
Air-dried coating
0.42
(3.5)
3)
Extreme performance
0.42
(3.5)
coating
~j
Steel pail and drum
(0.52)
(4.3)
interior coating
4~)
All
other coatings
0.36
(3.0)
kg/1
lb/gal
k)
Heavy
Off-Highway Vehicle
Products Coating
1)
Extreme performance
0.42
(3.5)
prime coat
2)
Extreme performance top- 0.42
(3.5)
coat
(air dried)
3)
Final repair coat
0.42
(3.5)
(air dried)
4)
All other coatings are subject to the emission
limitations for miscellaneous metal parts and
products coatings in subsection
(j)
above.
1)
Wood Furniture Coating
kg/i
lb/gal
1)
Clear topcoat
0.67
(5.6)
2)
Opaque stain
0.56
(4.7)
3)
Pigmented coat
0.60
(5.0)
4)
Repair coat
0.67
(5.6)
5)
Sealer
0.67
(5.6)
6)
Semi—transparent stain
0.79
(6.6)

199
7)
Wash coat
0.73
(6.1)
(Note:
An owner or operator of a wood furniture
coating operation subject to this Section shall
apply all coatings, with the exception of no more
than 37.8
1
(10 gal)
of coating per day used for
touch—up and repair operations, using one or more
of the following application systems:
airless
spray application system, air—assisted airless
spray application system, electrostatic spray
application system, electrostatic bell or disc
spray application system, heated airless spray
application system, roller coating, brush or wipe
coating application system, e~dip coating
application system or high volume low pressure
(HVLP)
application system.)
m)
Existing Diesel—Electric Locomotive Coating Lines
in
Cook County
kg/i
lb/gal
1)
Extreme performance prime
coat
0.42
(3.5)
2)
Extreme performance top-
coat (air dried)
0.42
(3.5)
3)
Final repair coat
(air dried)
0.42
(3.5)
4)
High-temperature aluminum
coating
0.72
(6.0)
5)
All other coatings
0.36
(3.0)
(Source:
Amended at
Ill. Reg.
______,
effective
__________
Section 218.205
Daily-Weighted Average Limitations
No owner or operator of a coating line subject to the limitations
of Section 218.204 of this Part and complying by means of this
Section shall operate the subject coating line unless the owner
or operator has demonstrated compliance with subsection
(a),
(b),
(c),
(d),
(e)
or
(f)
of this Section
(depending upon the source
category of coating) through the applicable coating analysis test
methods and procedures specified in Section 218.105(a)
of this
Part and the recordkeeping and reporting requirements specified
in Section 218.211(d)
of this Part:

200
a)
No owner or operator of a coating line subject to only
one of the limitations from among Section
218.204 (a) (1),
(ci)
(2),
(a) (4),
(C),
(d)
,
(e)
,
(f)
,
(g)
,
(h), or
(i)
of this Part shall apply coatings on any
such coating line,
during any day, whose daily-weighted
average VON content exceeds the emission limitation to
which the coatings are subject.
b)
No owner or operator of a miscellaneous metal parts and
products coating line subject to the limitations of
Section 218.204(j)
of this Part shall apply coatings to
miscellaneous metal parts or products on the subject
coating line unless the requirements in subsection
(b) (1)
or
(b) (2) below are met.
1)
For each coating line which applies multiple
coatings,
all of which are subject to the same
numerical emission limitation within Section
218.204(j)
during the same day (e.g.,
all coatings
used on the line are subject to 0.42 kg/i
3.5
lbs/gal),
the daily-weighted average VON content
shall not exceed the coating VON content limit
corresponding to the category of coating used,
or
2)
For each coating linewhich applies coatings
subject to more than one numerical emission
limitation from more than one of the four coating
categories in Section 218.204(j)
above, during the
same day, the owner or operator shall have a
site-specific proposal approved by the Agency and
approved by the USEPA as a SIP revision.
To
receive approval, the requirements of USEPA’s
Emissions Trading Policy Statement (and related
policy)
51 Fed.
Reg. 43814
(December 4,
1986),
must be satisfied.
c)
No owner or operator of a can coating faciiityline
subject to the limitations of Section
~j,~.204(b) g~
this Part shall operate the subject coating f-a-cility
line using a coating with a VON content in excess of
the limitations specified in Section 24-&2J,~.204(b)
this Part unless all of the following requirements are
met:
1)
An alternative daily emission limitation shall be
determined for the can coating operation,
i.e.
for
all of the can coating lines at the source,
according to subsection
(c) (2)
below.
Actual
daily emissions shall never exceed the alternative
daily emission limitation and shall be calculated
by use of the following equation.

201
n
Ed
=
E
V1
C,
i=1
where:
Ed
=
Actual VON emissions for the day
in
units of kg/day
(lbs/day),-j.
i
=
Subscript denoting a specific
coating applied,-j
n
=
Total number of coatings applied in
the can coating operation,
i.e.
all
can coating lines at the source
V1
=
Volume of each coating applied for
the day in units of 1/day
(gal/day)
of coating
(minus water and any
compounds which are specifically
exempted from the definition of
VOM)~
C1
=
The VON content of each coating as
applied in units of kg VOM/1
(lbs
VON/gal)
of coating (minus water
and any compounds which are
specifically exempted from the
definition of VOM).
2)
The alternative daily emission limitation
(Ad)
shall be determined for the can coating operation,
i.e.
for all of the can coating lines at the
source,
on a daily basis as follows:
n
Ad=
E
V1
~
-C1j
i=1
(D1
L1)
where:
Ad
=
The VOM emissions allowed for the
day in units of kg/day (ibs/day),-~
i
=
Subscript denoting a specific
coating applied,-~
n
=
Total number of surface coatings
applied in the can coating
operation,-j.

202
C1
=
The VON content of each surface
coating as applied in units
of kg
VON/i
(lbs VON/gal)
of coating
(minus water and any compounds
which are specifically exempted
from the definition of VON),-~
=
The density of VON in each coating
applied.
For the purposes of
calculating +Ad, the density is
0.882 kg VON/i VON
(7.36 lbs
VON/gal VON),-~
V1
=
Volume of each surface coating
applied for the day in units
of
1
(gal)
of coating
(minus water and
any compounds which are
specifically exempted from the
definition of VOM),-~
L1
=
The VOM emission limitation for
each surface coating applied as
specified in Section 218.204(b)
~i
this Part in units of kg VOM/i
(lbs
VOM/gal)
of coating
(minus water
and any compounds which are
specifically exempted from the
definition of VON).
d)
No owner or operator of a
heavy
off—highway vehicle
products coating line subject to the limitations of
Section 218.204(k)
of this Part shall apply coatings to
heavy off-highway vehicle products on the subject
coating line unless the requirements of subsection
(ci) (1)
or
(d) (2) below are met.
1)
For each coating line which applies multiple
coatings, all of which are subject to the same
numerical emission limitation within Section
218.204(k)
above, during the same day (e.g., all
coatings used on the line are subject to 0.42 kg/l
3.5
lbs/gal)),
the daily-weighted average VON
content shall not exceed the coating VON content
limit corresponding to the category of coating
used,
or
2)
For each coating line which applies coatings
subject to more than one numerical emission
limitation in Section 218.204(k)
above,
during the
same day, the owner or operator shall have a site
specific proposal approved by the Agency and

203
approved by the USEPA as a SIP revision.
To
receive approval, the requirements of USEPA’s
Emissions Trading Policy Statement (and related
policy)
51 Fed. Reg.
43814
(December 4,
19861,
must be satisfied.
e)
No owner or operator of a wood furniture coating line
subject to the limitations of Section 218.204(1)
~
this Part shall apply coatings to wood furniture on the
subject coating line unless the requirements of
subsection
(e) (1)
or subsection
(e) (2)
below,
in
addition to the requirements specified in the note to
Section 218.204(1)
of this Part,
are met.
1)
For each coating line which applies multiple
coatings, all of which are subject to the same
numerical emission limitation within Section
218.204(1)
above, during the same day
(e.g.,
all
coatings used on the line are subject to 0.67 kg/i
5.6
lbs/gal),
the daily-weighted average VON
content shall not exceed the coating VON content
limit corresponding to the category of coating
used,
or
2)
For each coating line which applies coatings
subject to more than one numerical emission
limitation in Section 218.204(1)
above, during the
same day, the owner or operator shall have a site
specific proposal approved by the Agency and
approved by the USEPA as a SIP revision.
To
receive approval, the requirements of USEPA’s
Emissions Trading Policy Statement (and related
policy)
51 Fed.
Req.
43814
(December 4,
1986),
must be satisfied.
f)
No owner or operator of an existing diesel—electric
locomotive coating line in Cook County,
subject to the
limitations of Section 218.204(m)
of this Part shall
apply coatings to diesel-electric locomotives on the
subject coating line unless the requirements of
subsection
(b) (1) (f) (1)
or
-(~b)(2) (f) (2)
of this Section
are met.
1)
For each coating line which applies multiple
coatings, all of which are subject to the same
numerical emission limitation within Section
218.204(m) above,
during the same day
(e.g.,
all
coatings used on the line are subject to 0.42 kg/i
3.5
lbs/gal),
the daily-weighted average VON
content shall not exceed the coating VON content
limit corresponding to the category of coating
used,
or

204
2)
For each coating line which applies coatings
subject to more than one numerical emission
limitation in Section 218.204(m)
above,
during the
same day,
the owner or operator shall have a site
specific proposal approved by the Agency and
approved by the USEPA as a SIP revision.
To
receive approval, the requirements of USEPA’s
Emissions Trading Policy Statement (and related
policy) must be satisfied.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.206
Solids Basis Calculation
Limitations
in terms of kg
(ibs)
of VON emissions per
1
(gal)
of
solids as applied at each coating applicator shall be determined
by the following equation:
S
=
C
1
(C/D)
where:
S
=
The limitation on VON emissions in terms of
kg VON/i
(lbs VON/gal)
of soiids,-~
C
=
The limitation on VON emissions in terms of
kg/i
(lbs/gal)
of coating (minus water and
any compounds which are specifically excluded
from the definition of VON) specified in
Section 218.204,- of this Part
D
=
The density of VON in the coating.
For the
purposes of calculating 5, the density is
0.882 kg VOM/l VON (7.36 lbs VOM/gal VON).
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.207
Alternative Emission Limitations
a)
Any owner or operator of a coating line subject to
Section 218.204 of this Part may comply with this
Section, rather than with Section 218.204 of this Part,
if a capture system and control device are operated at
all times the coating line is
in operation and the
owner or operator demonstrates compliance with
subsections
(c),
(d),
(e),
(f),
(g)
or
(h)
of this
Section (depending upon the source category) through
the applicable coating analysis and capture system and
control device efficiency test methods and procedures

205
specified in Section 218.105 of this Part and the
recordkeeping and reporting requirements specified in
Section 218.211(e)
of this Part and the control device
is equipped with the applicable monitoring equipment
specified in Section 218.105(d)
of this Part and the
monitoring equipment is
installed, calibrated, operated
and maintained according to vendor specifications at
all times the control device
is in use.
A capture
system and control device, which does not demonstrate
compliance with subsection
(c),
(d),
(e),
(f),
(g)
or
(h)
of this Section may be used as an alternative to
compliance with Section 218.204 of this Part only if
the alternative is approved by the Agency and approved
by the USEPA as
a SIP revision.
b)
Alternative Add-On Control Methodologies
1)
The coating line is equipped with a capture system
and control device that provides 81 percent
reduction in the overall emissions of VON from the
coating line and the control device has a 90
percent efficiency,
or
2)
The system used to control VON from the coating
line is demonstrated to have an overall efficiency
sufficient to limit VON emissions to no more than
what is allowed under Section 218.204 of this
Part.
Use of any control system other than an
afterburner, carbon adsorption,
condensation, or
absorption scrubber system can be allowed only if
approved by the Agency and approved by the USEPA
as a SIP revision.
The use of transfer efficiency
credits can be allowed only if approved by the
Agency and approved by the USEPA as a SIP
revision.
Baseline transfer efficiencies and
transfer efficiency test methods must be approved
by the Agency and the USEPA.
Such overall efficiency
is to be determined as
follows:
A)
eObtain
the emission limitation from the
appropriate subsection in Section 218.204 of
this Part~-~
B)
eCalculate US” according to the equation in
Section 218.206 of this Part,-~
C)
ecalculate the overall efficiency required
according to Section 218.105(e)
of this
Part.
For the purposes of calculating this value,
according to the equation in Section

206
218.105(e) (2)
of this Part,
VON1 is equal to
the value of “5” as determined above
in
subsection
(b) (2) (B) of this Section.
c)
No owner or operator of a coating line subject to only
one of the emission limitations from among Section
218.204 (a) (1),
-(-a) (2),
(a) (4),
(C),
(d)
,
(e)
,
(f)
,
(g)
(h)
or
(i)
of this Part and equipped with a capture
system and control device shall operate the subject
coating line unless the requirements in subsection
(b) (1)
or
(b) (2)
above are met.
No owner or operator
of a coating line subject to Section 218.204(a) (2)
or
218.204(a) (3)
and equipped with a capture system and
control device shall operate the coating line unless
the owner or operator demonstrates compliance with ~e
topcoat such limitation in accordance with the topcoat
protocol for automobile or light—duty trucks referenced
in Section 218.105(b).
ci)
No owner or operator of a miscellaneous metal parts and
products coating line which applies one or more
coatings during the same day, all of which are subject
to the same numerical emission limitation within
Section 218.204(j)
of this Part (e.g.,
all coatings
used on the line are subject to 0.42 kg/l
3.5
lbs/gal)), and which is equipped with a capture system
and control device shall operate the subject coating
line unless the requirements in subsection
(b) (1)
or
(b) (2)
above are met.
e)
No owner or operator of a heavy off—highway vehicle
products coating line which applies one or more
coatings during the same day, all of which are subject
to the same numerical emission limitation within
Section 218.204(k)
of this Part
(e.g., all coatings
used on the line are subject to 0.42 kg/i
3.5
lbs/gal),
and which is equipped with a capture system
and control device shall operate the subject coating
line unless the requirements in subsection
(b) (1)
or
(b) (2)
above are met.
f)
No owner or operator of an existing diesel—electric
locomotive coating line in Cook County which applies
one or more coatings during the same day, all of which
are subject to the same numerical emission limitation
within Section 218.204(m)
of this Part (e.g.,
all
coatings used on the line are subject to 0.42 kg/i
3.5
lbs/gal),
and which is equipped with a capture system
and control device shall operate the subject coating
line unless the requirements in subsection
(b) (1)
or
(b) (2)
above are met.

207
g)
No owner or operator of a wood furniture coating line
which applies one or more coatings during the same day,
all of which are subject to the same numerical emission
limitation within Section 218.204(1)
of this Part
(e.g., all coatings used on the line are subject to
0.67 kg/i
5.6
lbs/gal)),
and which is equipped with a
capture system and control device shall operate the
subject coating line unless the requirements in
subsection
(b) (1)
or
(b) (2)
of this Section are met.
If compliance is achieved by meeting the requirements
in subsection
(b) (2)
of this Part, then the provisions
in the note to Section 218.204(1)
of this Part must
also be met.
h)
No owner or operator of
a can coating facilityline end
which
is equipped with a capture system and control
device shall operate the subject coating facilityline
unless the requirements in subsection
(h) (1)
or
(h) (2)
below are met.
1)
An alternative daily emission limitation shall be
determined for the can coating operation,
i.e.
for
all of the can coating lines at the source,
according to Section 218.205(c) (2)
of this Part.
Act~ialdaily emissions shall never exceed the
alternative daily emission limitation and shall be
calculated by use of the following equation:
n
Ed
=
E
V1
C.
(1—F1
)
i=i
where:
Ed
=
Actual VOM emissions for the day in
units
of kg/day
(lbs/day),-j.
i
=
Subscript denoting the specific
coating applied,-~
n
=
Total number of surface coatings as
applied in the can coating
operation,-~
VI
=
Volume of each coating as applied
for the day in units of 1/day
(gal/day)
of coating
(minus water
and any compounds which are
specifically exempted from the
definition of VOM)-~-~

208
C1
=
The VON content of each coating as
applied in units of kg VON/i
(lbs
VON/gal)
of coating (minus water
and any compounds which are
specifically exempted from the
definition of VON) and
F1
=
Fraction, by weight,
of VON
emissions from the surface coating,
reduced or prevented from being
emitted to the ambient air. This is
the overall efficiency of the
capture system and control device~
2)
The coating line
is equipped with a capture system
and control device that provide 75 percent
reduction in the overall emissions of VON from the
coating line and the control device has a 90
percent efficiency.
(Source:
Amended at
Iii. Reg.
______,
effective
____________
Section 218.208
Exemptions From Emission Limitations
a)
Exemptions for all sourcccoating categories except wood
furniture coating.
The limitations Of this Subpart
shall not apply to coating lines within a facility
source, that otherwise would be subject to the same
subsection of Section 218.204
(because they belong to
the same sourcecoating category,
e.g. can coating)
provided that combined actual emissions of VON from all
lines at the fcicilitysource subject to that subsection
never exceed 6.8 kg/day
(15 lbs/day) before the
application of capture systems and control devices.
(For example, can coating lines within a plcintsource
would not be subject to the limitations of Section
218.204(b)
of this Part if the combined actual
emissions of VON from the can coating lines never
exceed 6.8 kg/day
(15 lbs/day) before the application
of capture systems and control devices.)
Volatile
organic material emissions from heavy off—highway
vehicle products coating lines must be combined with
VON emissions from miscellaneous metal parts and
products coating lines to determine applicability.
Any
owner or operator of a coating facilitysource shall
comply with the applicable coating analysis test
methods and procedures specified in Section 218.105(a)
of this Part and the recordkeeping and reporting
requirements specified in Section 218.211(a)
of this
Part if total VON emissions from the subject coating

209
lines are always less than or equal to 6.8 kg/day
(15 lbs/day) before the application of capture systems
and control devices and,
therefore, are not subject to
the limitations of Section 218.204 of this Part.
Once
a category of coating lines at a facilitysource is
subject to the limitations in Section 218.204,
of this
Part the coating lines are always subject to the
limitations in Section 218.204 of this Part.
b)
Applicability for wood furniture coating
1)
The limitations of this Subpart shall apply to a
plant’osource’s wood furniture coating lines if
the piantsource contains process emission sources
units,
not regulated by Subparts B,
E,
F
(excluding Section 218.204(1)
of this Part),
H
(excluding Section 218.405),
Q,
R,
5,
T
(excluding
Section 218.486 of this Part),V,
X,
Y, e~Z or BB
of this Part, which as a group both:
A)
ll1~avemaximum theoretical emissions of 91 Mg
(100 tons) or more per calendar year of VON
if no air pollution control equipment were
used,
and
B)
Aere not limited to less than 91 Mg
(100 tons)
of VOM per calendar year if no
air pollution control equipment were used,
through production or capacity limitations
contained in a federally enforceable
construction permit or SIP revision.
2)
If
a piantsource ceases to fulfill the criteria of
subsection
(b) (1)
of this Section, the limitations
of Section 218.204(1) of this Part shall continue
to apply to any wood furniture coating line which
was ever subject to the limitations of Section
218.204(1)
of this Part.
3)
For the purposes of subsection
(b)
of this
Section,
an emission sourceunit shall be
considered regulated by
a Subpart if it is subject
to the limitations of that Subpart.
An emission
sourccunit is not considered regulated by a
Subpart
if it is not sublect to the limits of that
Subpart, e.g., the emission unit is covered by an
exemption in the Subpart or the appplicabiiity
criteria of the Subpart are not met.
its emissions
are below the applicability cutoff level or if the
source
is covered by an exemption.

~~LV
4)
Any owner or operator of a wood furniture coating
line to which the limitations of this Subpart are
not applicable due to the criteria in subsection
(b)
of this Section shall, upon request by the
Agency or the USEPA,
submit records to the Agency
and the USEPA within 30 calendar days from the
date of the request that document that the coating
line is exempt from the limitations of this
Subpart.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.209
Exemption From General Rule on Use of Organic
Material
No owner or operator of a coating line subject to the limitations
of Section 218.204 of this Part is required to meet the
limitations of Subpart G (Section 218.301 or 218.302)
of this
Part,
after the date by which the coating line is required to
meet Section 218.204 of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.210
Compliance Schedule
Every owner or operator of a coating line
(of a type included
within Section 218.204)
of this Part shall comply with the
requirements of Section 218.204,
218.205, 218.207 or 218.208 and
Section 218.211 of this Part in accordance with the appropriate
compliance schedule as specified in subsection
(a),
(b),
(c)
or
(d)
below:
a)
No owner or operator of a coating line which is exempt
from the limitations of Section 218.204 of this Part
because of the criteria in Section 218.208(a)
of this
Part shah
operate said coating line on or after a date
consistent with Section 218.106 of this Part, unless
the owner or operator has complied with, and continues
to comply with,
Section 218.211(b)
of this Part.
Wood
furniture coating lines are not subject to Section
218.211(b)
of this Part.
b)
No owner or operator of a coating line complying by
means of Section 218.204 of this Part shall operate
said coating line on or after a date consistent with
Section 218.106 of this Part,
unless the owner or
operator has complied with,
and continues to comply
with,
Sections 218.204 and 218.211(c)
of this Part.

211
c)
No owner or operator of a coating line complying by
means of Section 218.205 of this Part shall operate
said coating line on or after a date consistent with
Section 218.106 of this Part, unless the owner or
operator has complied with,
and continues to comply
with,
Sections 218.205 and 218.211(d) of this Part.
d)
No owner or operator of a coating line complying by
means of Section 218.207 of this Part shall operate
said coating line on or after a date consistent with
Section 218.106 of this Part, unless the owner or
operator has complied with, and continues to comply
with,
Sections 218.207 and 218.211(e) of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
_________
Section 218.211
Recordkeeping and Reporting
a)
The VON content of each coating and the efficiency of
each capture system and control device shall be
determined by the applicable test methods and
procedures specified in Section 218.105 of this Part to
establish the records required under this Section.
b)
Any owner or operator of a coating line which
is
exempted from the limitations of Section 218.204 ~
this Part because of Section 218.208(a)
of this Part
shall comply with the following:
1)
By a date consistent with Section 218.106 of this
Part, the owner or operator of a fcicihitycoating
line or a group of coating lines referenced in
this subsection(b)
of this Section shall certify
to the Agency that the facilitycoating line or
group of coating lines
is exempt under the
provisions of Section 218.108(a)
of this Part.
Such certification shall include:
A)
A declaration that the facihitycoating line
or group of coating lines is exempt from the
limitations of Section 218.204 of this Part
because of Section 218.208(a)
of this Part
and
B)
Calculations which demonstrate that the
combined VOM emissions from ~
coating
lines at the faciiity~group of coating
lines never exceed 6.8 kg
(15
lbs) per day
before the application of capture systems and
control devices.
The following equation

212
shall be used to calculate total VON
emissions:
m
n
~
=
E
(A~ B1)~
j=1
i=1
where:
T~-,
=
Total VOM emissions from coating
lines
cit
a facility each day before
the application of capture systems
and control devices in units of
kg/day
(lbs/day),-j.
m
=
Number of coating lines at the
facility source that otherwise
would be sublect to the same
subsection of Section 218.104 of
this Part (because they beion~to
the same category, e.g.,
can
coating),-~
j
=
Subscript denoting an individual
coating
line,-.L
n
=
Number of different coatings as
applied each day on each coating
line at the facility,~
i
=
Subscript denoting an individual
coating,-j
A1
=
Weight of VON per volume of each
coating (minus water and any
compounds which are specifically
exempted from the definition of
VON)
as applied each day on each
coating line at the facility in
units of kg VON/i
(lbs VON/gal)~
and
B,
=
Volume of each coating (minus watem
and any compounds which are
specifically exempted from the
definition of VON)
as applied each
day on each coating line at the
facility in units
of 1/day
(gal/day).
The instrument or
method by which the owner or
operator accurately measured or

213
calculated the volume of each
coating as applied on each coating
line each day shall be described in
the certification to the Agency.
2)
On and after a date consistent with Section
218.106 of this Part, the owner or operator of
a
facility coating line or group of coating lines
referenced in this subsection shall collect and
record all of the following information each day
for each coating line and maintain the information
at the facilitysource for a period of three years:
A)
The name and identification number of each
coating as applied on each coating line.
B)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating line.
3)
On and after a date consistent with Section
2l8.106of this Part, the owneror operator of a
facility coating line or group of coating lines
exempted from the limitations of Section 218.204
of this Part because of Section 218.2O8~a)of this
Part shall notify the Agency of any record showing
that total VON emissions from the coating
faciiityiine or group of coating lines exceed 6.8
kg
(15 ibs)
in any day before the application of
capture systems and control devices by sending a
copy of such record to the Agency within 30 days
after the exceedance occurs.
c)
Any owner or operator of a coating line subject to the
limitations of Section 218.204 of this Part other than
Section 218.204(a) (2)
or
(a)(3)
and complying by means
of Section 218.204 of this Part shall comply with the
following:
1)
By a date consistent with Section 218.106 of this
Part,
or upon initial start—up of a new coating
line, or upon changing the method of compliance
from an existing subject coating line from Section
218.205 or Section 218.207 of this Part to Section
218.204 of this Part
the owner or operator of a
subject coating line shall certify to the Agency
that the coating line will be in compliance with
Section 218.204 of this Part on and after a date
~~-~t-
t.~4-h
~
~1R
106
of
this Part.
or

214
on and after the initial start-up date.
Such
certification shall
include:
A)
The name and identification number of each
coating
as
applied
on
each
coating
line.
B)
The weight of VON per volume of each coating
(minus water and any compounds which are
specifically
exempted from the definition of
VON)
as
applied
each
day
on each coating
line.
ern)-
For
coating
lines
subject
to
Section
218.204(a~
(1)
certification
shall
include:
.........
name and identification number of
each coating 218.204(a) (3),
44-)-
The name and identification numDer o~
each coating as applied on
line,
iii) Thc weight of VON per
VO.LUmC
or
eacn
coating
as
~r~r~licd
On
ecion
r~r~mr1ntT
.Lj~C
nstrumcnt
or
method
by
which
the
owner or operator will accurately
measure
or
calculate
the
volume
of
each
coat~inrias applied each day on each
coating
iinc,
The method by
operator
will
which
create
the
and
owner or
maintain
r~r~rird~i
~r~h
d~..r
~
i—~rin
i
rr~t-~
I
ri
suosccti~..
(c)(2)
below
for
coating
lines
subject
to
Section
218.204(a)
(3)
,
An
example
format
in
-which
the
records
required
in
subsection
(a)
(2)
below
for
V
-
-
I r,n
~bjec~
t~
218.204
(ci)
(3).
2)
On
and
after
a
date
consistent
with
Section
218.106
of
this
Part,
or
on
and
after
the
initial
start—up
date,
the
owner
or
operator
of
a
sublect
coating line subject to the limitations of
Cecti-eri
218.204 and complying by means of Section
218.2-04
shall collect and record all of the following
information each day for each coating line and
maintain the information at the facility source
for a period of three years:

215
A)
The name and identification number of each
coating
as
applied
on
each
coating
line.
B)
The
weight
of
VON
per
volume
of
each
coating
(minus
water
and
any
compounds
which
are
specifically
exempted
from
the
definition
of
VON)
as
applied
each
day
on
each
coating
line.
For
coating
lines
218.204 (a)
(3)
the
owner
or
operator
shall
maintain
all
records
necessary
to
calculate
the
daily-weighted
average
VON
content
from
the
coating
line
in
accordance
with the
proposal
submitted,
and
proved
by
the
UCEPA,
pursuant
to
Section
218.204
(a)
(3).
3)
On
and
after
a date consistent with Section
218.106
of
this
Part, the owner or operator of a
subject coating line shall notify the Agency in
the following instances:
A)
Any
record
showing
violation
of
Section
218.204
of
this
Part
shall
be
reported
by
sending
a
copy
of
such
record
to
the
Agency
within
30
days
following
the
occurrence
of
the
violation,
except
that
any
record
showing
a
violation
of
Section
218.204(a)
(3)
shall
be
reported
by
sending
a
copy
of
such
record
to
the
Agency
within
15
days
from
the
end
of
the
month
in
which
the
violation
occurred.
B)
At
least
30
calendar days before changing the
method
of
compliance
with
Section
218.204
from Section 218.204 of this Part to Section
218.205 or Section 218.207 of this Part, the
owner or operator shall comply with all
requirements of subsection
(d) (1)
or
(e) (1)
of this Section below, respectively.
Upon
changing the method of compliance with
Section 218.204 from Section 218.204
of this
Part to Section 218.205 of this Part or
Section 218.207 of this Part, the owner or
operator shall comply with all requirements
of subsection
(d) or
(e)
of this Section,
respectively.
?-)-
For coating lines subject to Section
218.204
(a)
(3)
the
owner
or
operator
shall
notify the Agcncy or
~
cnangc
cc
cne
topcoating operation at least 30 days before
the
change
is
effected.
The
Agency
shall

216
rocertif.~~,jp~
i.t.~tiny i~
required, then the owner or operator shall
submit
a
proposal
to
the
Agency
within
to
test
30
days
of
I
d)
Any owner or operator of a coating line subject to the
limitations of Section 218.204 of this Part and
complying by means of Section 218.205 of this Part
shall comply with the following:
1)
By a date consistent with Section 218.106 of this
Part, or upon initial start—up of a new coating
line, or upon changing the method of compliance
for an existing subject coating line from Section
218.204 or Section 218.207 of this Part to Section
218.205 of this Part the owner or operator of the
subject coating line shall certify to the Agency
that the coating line will be in compliance with
Section 218.205 of this Part on and after a date
consistent with Section 218.106 of this Part, or
on and after the initial start-up date.
Such
certification shall include:
A)
The name and identification number of each
coating line which will comply by means of
Section 218.205 of this Part.
B)
The name and identification number of each
coating as applied on each coating line.
C)
The weight of VON per volume and the volume
of each coating (minus water and any
compounds
which
are
specifically
exempted
from the definition of VON)
as applied each
day on each coating line.
D)
The
instrument
or
method
by
which
the
owner
or operator will accurately measure or
calculate the volume of each coating as
applied each day on each coating line.
E)
The method by which the owner or operator
will create and maintain records each day as
required in subsection
(d) (2)
of this
Section.
F)
An
example
of
the
format
in
which
the
records
required
in
subsection
(d)
(2)
of
this
Section
will
be
kept.
determine whether or not recertification
testing is required.
If the Agency
I..._~I
~
within 30
d~.1... and retest
the
Agency’s
approval
of
the
ppu~u.,..

217
2)
On and after
a date consistent with Section
218.106 of this Part, or on and after the initial
start—up date, the owner or operator of
a subiect
coating line subject to the limitations of Section
218.204 and complying by means of Section 218.205
shall
collect
and
record
all
of
the
following
information each day for each coating line and
maintain the information at the facility source
for a period of three years:
A)
The name and identification number of each
coating as applied on each coating line.
B)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating line.
C)
The daily-weighted average VON content of all
coatings as applied on each coating line as
defined in Section 218.104 of this Part.
3)
On and after a date consistent with Section
218.106 of this Part, the owner or operator of a
subject coating line shall notify the Agency in
the following instances:
A)
Any record showing violation of Section
218.205 of this Part shall be reported by
sending a copy of such record to the Agency
within 30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with this subpart from
Section 218.205 of this Part to Section
218.204 or Section 218.207 of this Part, the
owner or operator shall comply with all
requirements of subsection
(c) (1) or
(e) (1)
of this Section, respectively.
Upon changing
the method of compliance with this subpart
from Section 218.205 to Section 218.204 or
Section 218.207 of this Part,
the owner or
operator shall comply with all requirements
of subsection
(c) or
(e)
of this Section,
respectively.
e)
Any owner or operator of a coating line subject to the
limitations of Section 218.207 of this Part and
complying by means of Section 218.207(c),
(d),
(e),

218
(f),
(g) or
(h)
of this Part shall comply with the
following:
1)
By
a date consistent with Section 218.106 of this
Part, or upon initial start—up of a new coating
line, or upon changing the method of compliance
for
an
existing
coating
line
from
Section
218.204
or
Section
218.205
of
this
Part
to
Section
218.207
of this Part, the owner or operator of the subject
coating line shall perform all tests and submit to
the Agency the results of all tests and
calculations necessary to demonstrate that the
subject coating line will be in compliance with
Section 218.207 of this Part on and after a date
consistent with Section 218.106 of this Part,
or
on and after the initial start-up date.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date, the owner or operator of a sublect
coating line subject to the limitations of Section
218.207 and complying by means of Section
218.207(c),
(d)
,
(C)
,
(f)
,
(g)
,
or
(h)
shall
collect and record all of the following
information each day for each coating line and
maintain the information at the facilitysource for
a period of three years:
A)
The weight of VON per volume of coating
solids as applied each day on each coating
line,
if complying pursuant to Section
218.207(b) (2)
of this Part.
B)
Control device monitoring data.
C)
A log of operating time for the capture
system,
control device, monitoring equipment
and the associated coating line.
D)
A maintenance log for the capture system,
control device and monitoring equipment
detailing all routine and non—routine
maintenance performed including dates and
duration of any outages.
3)
On and after a date consistent with Section
218.106 of this Part,
the owner or operator of a
subject coating line shall notify the Agency in
the following instances:
A)
Any record showing violation of Section
‘r~~7
r,F
4-hIc~
P~-t ~h~11
b~?reoorted by

219
sending a copy of such record to the Agency
within 30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with this Subpart from
Section 218.207 of this Part to Section
218.204 or Section 218.205 of this Part, the
owner
or
operator
shall
comply
with
all
requirements
of
subsection
(c)
(1)
or
(d)
(1)
of
this
Section,
respectively.
Upon
changing
the
method
of
compliance
with
this
subpart
from Section 218.207 of this Part to Section
218.204
or
Section
218.205
of this Part, the
owner or operator shall comply with all
requirements of subsection
(c)
or
(d)
of this
Section, respectively.
il
AnY owner or oPerator of
a primer surfacer operation or
topcoat operation subiect to the limitations of Section
218.204(a) (2)
or
(a)(3)
of this Part shall comply with
the following:
fl
By a date consistent with Section 218.106 of this
Part, or upon initial start-up of a new coating
operation, the owner or operator of a sublect
coating operation shall certify to the A~encvthat
the operation will be
in compliance with Section
218.204 of this Part on and after a date
consistent with Section 218.106 of this Part,
or
on and after the initial start-up date.
Such
certification shall include:
~j
The name and identification number of each
coating operation which will comply by means
of Section 218.204(a) (2) and
(a)(3)
of this
Part and the name and identification number
of each coating line in each coatip,g
operation.
~
The name and identification number of each
coating as applied on each coating line
in
the coating operation.
ci
_______________________
Q1
__________________
The weight of VON ~er volume of each coatiflg
(minus water and any compounds which are
specifically exempted from the definition of
VOM)
as applied each day on each coating
line.
The transfer efficiency and control
efficiency measured for each coating line.

220
~j
Test reports,
including raw data and
calculations documenting the testing
performed to measure transfer efficiency and
control efficiency.
fi
The instrument or method by which the owner
or operator will accurately measure or
calculate the volume of each coating as
applied each day on each coating line.
ci
The method by which the owner or operator
will create and maintain records each day as
required in subsection
(f) (2) below.
JiL.
An exam~ieformat for presenting the records
required
in subsection
(f) (2) below.
21
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date,
the owner or operator of
a subiect
coating operation shall collect and record all of
the following information each day for each
operation and maintain the information at the
source for a period of three years:
~j
All information necessary to calculate the
daily-weighted average VON emissions from the
coating operations in kg
(lbs)
per
1
(gal)
of
coating solids deposited in accordance with
the proposal submitted,
and approved pursuant
to Section 218.204 (a) (2) or
(a) (3)
of this
Part including:
LL
The name and identification number of
each coating as applied on each coating
operation.
£jJ.
The weight of VOM per volume of each
coating
(minus
water
and
any
compounds
which are specifically exempted from the
definition of VOM)
as applied each day
on each coating operation.
~j
If a control device(s)
is used to control VON
emissions,
control device monitoring data;
a
log of operating time for the capture system,
control device, monitoring equipment and the
associated coating operation; and a
maintenance log for the capture system,
control device and monitoring equipment,
detailing all routine and non-routine

221
maintenance performed including dates and
duration of any outages.
~j.
On
and
after
a date consistent with Section
218.106
of
this
Part
or
on
and
after the initial
start—up
date,
the
owner
or
operator
of
a subiect
coating operation shall determine and record the
daily VON emissions in kg
(ibs)
per
1
(gal)
of
coating solids deposited in accordance with the
proposal submitted and a~~rovedPursuant to
Section 218.204(a) (2)
or
(a)(3)
of this Part
within 10 days from the end of the month and
maintain this information at the source for a
period
of
three
years.
On
and after a date consistent with Section
218.106 of this Part, the owner or operator of a
sublect coating operation shall notify the Agency
in the following instances:
~j
Any record showing a violation of Section
218.204(a) (2)
or
(a)(3) of this Part shall be
reported by sending a copy of such record to
the Agency within 15 days from the end of the
month in which the violation occurred.
~j
The owner or operator shall notify the Agency
of any change to the operation at least
30
days before the change
is effected.
The
Agency shall determine whether or not
compliance testing is reguired.
If the
A~encvdetermines that compliance testing is
reguired, then the owner or operator shall
submit_a testing proposal to the Agency
within 30 days and test within 30 days of the
approval of the proposal by the Agency and
USEPA.
(Source:
Amended at
Iii.
Reg.
______,
effective
____________
SUBPART
G:
USE OF ORGANIC MATERIAL
Section 218.301
Use of Organic Material
No person shall cause or allow the discharge of more than 3.6
kg/hr
(8 lbs/hr)
of organic material into the atmosphere from any
emission sourceunit,
except as provided in Sections 218.302,
218.303, 218.304 of this Part and the following exception:
If no
odor nuisance exists the limitation of this Subpart shall apply
only to photochemicaily reactive material.

222
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.302
Alternative Standard
Emissions of organic material
in excess of those permitted by
Section 218.301 of this Part are allowable if such emissions are
controlled by one of the following methods:
a)
Flame,
thermal or catalytic incineration so as either
to reduce such emissions to 10 ppm equivalent methane
(molecular weight
16)
or less,
or to convert 85 percent
of the hydrocarbons to carbon dioxide and water;
or,
b)
A vapor recovery system which adsorbs and/or condenses
at least 85 percent of the total uncontrolled organic
material that would otherwise be emitted to the
atmosphere;
or,
c)
Any other air pollution control equipment approved by
the Agency and approved by the USEPA as a SIP revision
capable of reducing by 85 percent or more the
uncontrolled organic material that would be otherwise
emitted to the atmosphere.
(Source:
Amended at
Ill. Reg.
_____,
effective
___________
Section 218.303
Fuel Combustion Emission CourccsUnits
The provisions of Sections 218.301 and 218.302
of this Part shall
not apply to fuel combustion emission sourcesunits.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
Section 218.304
Operations with Compliance Program
The provisions of Sections 218.301 and 218.302 of this Part shall
not appiy to any owner,
operator, user or manufacturer of paint,
varnish,
lacquer, coatings or printing ink whose compliance
program and project completion schedule,
as required by
35 Ill.
Adm. Code 201, provided for the reduction of organic material
used in such process to 20 percent or less of total volume by Nay
30,
1977.
(Source:
Amended at
Ill. Reg.
______,
effective
____________

223
SUBPART H:
PRINTING AND PUBLISHING
Section 218.401
Fiexographic and Rotogravure Printing
a)
No owner or operator of a subject flexographic,
packaging rotogravure or publication rotogravure
printing line shall apply at any time any coating or
ink unless the VON content does not exceed the
limitation specified
in
either subsection
(a) (1) or
(a) (2) below.
Comphi~ncewith this Section must be
demonstrated through the applicable coating or ink
analysis test methods and procedures specified in
Section 218.105(a) of this Part and the recordkeeping
and reporting requirements specified in Section
218.404(c)
of this Part.
As an alternative to
compliance with this subsection,
a subject printing
line may meet the requirements of subsection
(b) or
(c)
below.
1)
Forty percent VOM by volume of the coating and ink
(minus water and any compounds which are
specifically exemptedfrom the definition of VON),
or
2)
Twenty-five
percent
VON
by
volume
of the volatile
content in the coating and ink.
b)
No owner or operator of a subject flexographic,
packaging rotogravure or publication rotogravure
printing line shall apply coatings or inks on the
subject printing line unless the weighted average,
by
volume, VON content of all coatings and inks as applied
each day on the subject printing line does not exceed
the limitation specified in either subsection
(a) (1)
(as determined by subsection
(b) (i)j or subsection
(a)(4~)) (as determined by subsection
(b)(2)1.
Compliance with this subsection must be demonstrated
through the applicable coating or ink analysis test
methods and procedures specified in Section 218.105(a)
of this Part and the recordkeeping and reporting
requirements specified in Section 218.404(d)
of this
Part.
1)
The following equation shall be used to determine
if the weighted average VON content of all
coatings and inks as applied each day on the
subject printing line exceeds the limitation
specified in subsection
(a) (1)
of this Section.

224
n
E
C1
L
(V54~
+
Vv~M~)
VOM(~)(A)
=
i1
n
Z
L~
(V31
+
V~0~
1=41
Where:
VOM(~)(A)
=
The weighted average VON content in
units
of
percent
VOM
by
volume
of
all coatings and inks
(minus water
and any compounds which are
specifically exempted from the
definition of VOM) used each day-rj.
I
=
Subscript denoting a specific
coating or ink as applied~~
n
=
The number of different coatings
and/or inks as applied each day on
a printing line,-~
C1
=
The VON content in units of percent
VON by vOlume of each coating or
ink as applied
(minus water and any
compounds which are specifically
exempted from the definition of
VOM)Tj.
=
The liquid volume of each coating
or ink as applied in units of
1
(gal)-r~
V~
=
The volume fraction of solids
in
each coating or ink as applied and
V4i~
=
The volume fraction of VOM in each
coating or ink as applied.
2)
The following equation shall be used to determine
if the weighted average VOM content of all
coatings and inks as applied each day on the
subject printing line exceeds the limitation
specified in subsection
(a) (2)
of this Section.

225
n
E
C1
L1
VVM4II~
VOM(~)~)
=
1=1
n
E
L1 V~
1=1
where:
VOM(~)
=
The weighted average VOM content in
units of percent VON by volume of
the volatile content of all
coatings and inks used each day~~
I
=
Subscript denoting a specific
coating or ink as applied,-~
n
=
The number of different coatings
and/or inks as applied each day on
each printing lineT~
C
=
The VON content in units of percent
VON by volume of the volatile
matter in each coating or ink as
apphied-~j.
L1
=
The liquid volume of each coating
or ink as applied in units of
1
(gal)
and
VVM-iM~
=
The volume fraction of
volatile matter in each
coating or ink as applied.
c)
No owner or operator of a subject flexographic,
packaging rotogravure or publication rotogravure
printing line equipped with a capture system and
control device shall operate the subject printing line
unless the owner or operator meets the requirements in
subsection
(c) (1),
(c) (2), or
(c) (3) and subsections
(c) (4)
,
(c) (5)
and
(c) (6)
below.
1)
A carbon adsorption system is used which reduces
the captured VOM emissions by at least 90 percent
by weight,
or
2)
An incineration system is used which reduces the
captured VON emissions by at least 90 percent by
weight,
or

226
3)
An alternative VON emission reduction system is
used which is demonstrated to have at least a
90 percent control device efficiency, approved by
the Agency and approved by USEPA as a SIP
revision,
and
4)
The printing line is equipped with a capture
system and control device that provides an overall
reduction in VON emissions of at least:
A)
75 percent where a publication rotogravure
printing line is employed,
or
B)
65 percent where a packaging rotogravure
printing line
is employed,
or
C)
60 percent where a flexographic printing line
is employed,
and
5)
The control device
is equipped with the applicable
monitoring equipment specified in Section
218.105(d) (2) of this Part andT except as provided
in Section 218.105(d) (3) of this Part, the
monitoring equipment is installed, calibrated,
operated and maintained according to vendor
specifications at all times the control device is
in use, and
6)
The capture system and control device are operated
at all times when the subject printing line is in
operation.
The owner or operator shall
demonstrate compliance with this subsection by
using the applicable capture system and control
device test methods and procedures specified in
Section 218.105(c)
through Section 218.105(f)
~f
this Part and by complying with the recordkeeping
and reporting requirements specified in Section
218.404(e)
of this Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.402
Applicability
a)
The limitations of Section 218.401 of this Part apply
to all flexographic and rotogravure printing lines at a
subject facilitysource.
All f-aciiitiessources with
flexographic and/or rotogravure printing lines are
subject facilitiessources unless:
1)
Total maximum theoretical emissions of VOM from
all flexographic and rotogravure printing line(s)

227
(including solvents used for cleanup operations
associated with flexographic and rotogravure
printing line(s))
at the facilitysource never
exceed 90.7 Mg (100 tons)
per calendar year before
the application of capture systems and control
devices,
or
2)
A federally enforceable construction permit or SIP
revision for all flexographic and rotogravure
printing line(s) at a facilitysource requires the
owner or operator to limit production or capacity
of these printing line(s)
to reduce total VOM
emissions from all flexographic and rotogravure
printing line(s) to 90.7 Mg (100 tons)
or less per
calendar year before the application of capture
systems and control devices.
b)
Upon achieving compliance with this Subpart,
the
omission source is flexographic and rotogravure
printing lines are not required to meet Subpart G
(Sections 218.301 or -24-&218.38~02of this Part).
Emission sources Flexographic and rotogravure printing
lines exempt from this Subpart are subject to Subpart G
(Sections 218.301 or
~.3~02
~f
this Part).
Rotogravure or flexographic equipment used for both
roll printing and paper coating is subject to this
Subpart.
c)
Once subject to the limitations of Section 218.401,
a
flexographic or rotogravure printing line
is always
subject to the limitations of Section 218.401 of this
Part.
d)
Any owner or operator of any flexographic or
rotogravure printing line that is exempt from the
limitations of Section 218.401 of this Part because of
the criteria in this Section
is subject to the
recordkeeping and reporting requirements specified in
Section 218.404(b)
of this Part.
(Source:
Amended at
Iii. Reg.
______,
effective
____________
Section 218.403
Compliance Schedule
Every owner or operator of a fiexographic and/or rotogravure
printing line shall comply with the applicable requirements of
Section 218.401 and Section 218.404 of this Part in accordance
with the applicable compliance schedule specified in subsection
(a),
(b),
(c)
or
(d) below:

228
a)
No owner or operator of a flexographic or rotogravure
printing line which
is exempt from the limitations of
Section 218.401 of this Part because of the criteria in
Section 218.402 of this Part shall operate said
printing line on or after a date consistent with
Section 218.106 of this Part, unless the owner
or
operator has complied with,
and continues to comply
with,
Section 218.404(b) of this Part.
b)
No owner or operator of a fiexographic or rotogravure
printing line complying by means of Section 218.401(a)
of this Part shall operate said printing line on or
after
a date consistent with Section 218.106 of this
Part, unless the owner or operator has complied with,
and continues to comply with,
Section 218.401(a)
and
Section 218.404(c)
of this Part.
c)
No owner or operator of a flexographic or rotogravure
printing line complying by means of Section 218.401(b)
of this Part shall operate said printing line on or
after a date consistent with Section 218.106
of this
Part, unless the owner or operator has complied with,
and continues to comply with,
Section 218.401(b)
and
Section
218.404(d)
of
this
Part.
d)
No
owner
or
operator
of
a
flexographic
or
rotogravure
printing line complying by means of Section 218.401(c)
of this Part shall operate said printing line on or
after a date consistent with Section 218.106 of this
Part,
unless the owner or operator has complied with,
and continues to comply with,
Section 218.401(c)
and
Section 218.404(e)
of this Part.
(Source:
Amended at
Iii.
Reg.
______,
effective
____________
Section 218.404
Recordkeeping and Reporting
a)
The VON content of each coating and ink and the
efficiency of each capture system and control device
shall be determined by the applicable test methods and
procedures specified in Section 218.105 of this Part to
establish the records required under this Section.
b)
Any owner or operator of a printing line which is
exempted from the limitations of Section 218.401 g~
this Part because of the criteria in Section 218.402 of
this Part shall comply with the following:
1)
By a date consistent with Section 218.106 of
this
Part,
the owner or operator of a facility

229
flexographic and rotogravure printing line to
which this subsection is applicable shall certify
to the Agency that the facility flexographic and
rotogravure printing line is exempt under the
provisions of Section 218.402 of this Part.
Such
certification shall include:
A)
A declaration that the facilityfiexographic
and rotogravure printing line
is
exempt
from
the limitations of the criteria in Section
218.401
of
this
Part
because of Section
218.402 of this Part, and
B)
Calculations which demonstrate that total
maximum theoretical emissions of VOM from all
flexographic and rotogravure printing lines
at the faciiitysource never exceed 90.7 Mg
(100 tons) per calendar year before the
application of capture systems and control
devices.
Total maximum theoretical emissions
of VON for a flexographic or rotogravure
printing facilitysource is the sum of maximum
theoretical emissions of VON from each
flexographic and rotogravure printing line at
the
facilitysource.
The
following equation
shall be used to calculate total maximum
theoretical emissions of VON per calendar
year before the application of capture
systems and control devices for each
flexographic and rotogravure printing line at
the facilitysource:
E~=AxB+
1095 (CxDxF)
where:
=
Total maximum theoretical emissions
of VOM from one flexographic or
rotogravure printing line in units
of kg/year (ibs/year),-~
A
=
Weight of VON per volume of solids
of the coating or ink with the
highest VON content as applied each
year on the printing line in units
of kg VON/i
(lbs VON/gal)
of
coating or ink soiids~~
~4
B
=
Total volume of solids for all
coatings and inks that can
potentially be applied each year on

230
the printing line
in units of
1/year
(gal/year).
The instrument
and/or method by which the owner or
operator accurately measured or
calculated the volume of each
coating and ink as applied and the
amount that can potentially be
applied each year on the printing
line shall be described in the
certification to the Agency-~
C
=
Weight of VON per volume of
material for the cleanup material
or solvent with the highest VON
content as used each year on the
printing line in units of Kg/i
(lbs
VOM/gal)
of such material
D
=
The greatest volume of cleanup
material or solvent used in any
8-hour period and
F
=
The highest fraction of cleanup
material
or
solvent
which
is
not
recycled
or
recovered
for offsite
disposal during any 8-hour period.
2)
On
and
after
a
date
consistent
with
Section
218.106 of this Part,
the owner or operator of
a
facility flexographic and rotogravure printing
line referenced
in this subsection
shall
collect
and record all of the following information each
year for each printing line and maintain the
information at the facilitysource for a period of
three years:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VOM content and the volume of each
coating and ink as applied each year on each
printing line.
3)
On and after a date consistent with Section
218.106 of this Part,
the owner or operator of a
facility flexographic and rotogravure printing
line exempted from the limitations of Section
218.401 of this Part because of the criteria in
Section 218.402
of this Part shall notify the
Agency of any record showing that total maximum
theoretical emissions of VOM from all printing

231
lines exceed 90.7 Mg
(100 tons)
in any calendar
year before the application of capture systems and
control
devices
by
sending
a
copy
of
such
record
to the Agency within
30 days after the exceedance
occurs.
c)
Any owner or operator of a printing line subject to the
limitations of Section 218.401 of this Part and
complying by means of Section 218.401(a)
of this Part
shall comply with the following:
1)
By a date consistent with Section 218.106 of this
Part,
or upon initial start-up of a new printing
line,
or upon changing the method of compliance
from an existing subject printing line from
Section 218.401(b)
or Section 218.401(c)
of this
Part to Section 218.401(a)
of this Part,
the owner
or operator of a subject printing line shall
certify to the Agency that the printing line will
be in compliance with Section 218.401(a)
of this
Part on and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date.
Such certification shall include:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content of each coating and ink as
applied each day on each printing line.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date,
the owner or operator of a printing
line subject to the limitations of Section 218.401
of this Part and complying by means of Section
218.401(a)
of this Part shall collect and record
all of the following information each day for each
coating line and maintain the information at the
facilitysource for a period of three years:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content of each coating and ink as
applied each day on each printing line.
3)
On and after a date consistent with Section
218.106 of this Part, the owner or operator of a
subject printing line shall notify the Agency in
the following instances:

232
A)
Any record showing violation of Section
218.401(a)
of this Part shall be reported by
sending
a
copy
of
such
record
to
the
Agency
within 30 days following the occurrence of
the
violation.
B)
At least 30 calendar days before changing the
method of compliance with Section 218.401 Q~
this Part from Section 218.401(a) of this
Part to Section 218.401(b)
or
(c) of this
Part,
the
owner
or
operator shall comply with
all requirements of subsection
(b) (1) or
(c) (1) (d) (1) or
(e) (1)
of this Section,
respectively.
Upon changing the method of
compliance with Section 218.401 of this Part
from Section 218.401(a)
of this Part to
Section 218.401(b)
or
(c)
of this Part,
the
owner or operator shall comply with all
requirements of subsection -3-jç~j.or
-(-e-)-~~j
of this Section, respectively.
d)
Any owner or operator of a printing line subject to the
limitations of Section 218.401 of this Part and
complying by means of Section 218.401(b)
shall comply
with the following:
1)
By
a
date
consistent
with
Section
218.106
of
this
Part,
or
upon
initial
start-up
of
a
new
printing
line,
or upon changing the method of compliance
for an existing subject printing line from Section
218.401(a)
or
(c)
of this Part to Section
218.401(b)
of this Part, the owner or operator of
the subject printing line shall certify to the
Agency that the printing line will be in
compliance with Section 218.401(b)
of this Part on
and after a date consistent with Section 218.106
of this Part,
or on and after the initial start-up
date.
Such certification shall include:
A)
The name and identification number of each
printing line which will comply by means of
Section 218.401(b)
of this Part.
B)
The name and identification number of each
coating and ink available for use on each
printing line.
C)
The VON content of each coating and ink as
applied each day on each printing line.
D)
The instrument or method by which the owner
or operator will accurately measure or

233
calculate the volume of each coating and ink
as
applied
each
day
on
each
printing
line.
E)
The method by which the owner or operator
will create and maintain records each day as
required in subsection
-)-.~j(2) of this
Section.
F)
An example
of
the format in which the records
required
in subsection -(-~3-j~j(2)of this
Section will be kept.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start-up date, the owner or operator of a printing
line subject to the limitations of Section 218.401
of this Part and complying by means of Section
218.401(b)
of this Part shall collect and record
all of the following information each day for each
printing line and maintain the information at the
facilitysource for a period of three years:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content and the volume of each
coating
and
ink
as
applied
each
day
on
each
printing line.
C)
The daily-weighted average VOM content of all
coatings and inks as applied on each printing
line.
3)
On and after a date consistent with Section
218.106 of this Part, the owner or operator of a
subject printing line shall notify the Agency in
the following instances:
A)
Any record showing violation of Section
218.401(b)
of this Part shall be reported by
sending a copy of such record to the Agency
within
30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with Section 218.401
~f
this Part from Section 218.401(b)
of this
Part to Section 218.401(a)
or 218.401(c)
~f
this Part,
the owner or operator shall comply
with all requirements of subsection
(c)(1)
or
(e) (1) of this Section,
respectively.
Upon

234
changing the method of compliance with
Section 218.401 of this Part from Section
218.401(b)
of this Part to Section 218.401(a)
or
(c)
of this Part, the owner or operator
shall comply with all requirements of
subsection
(c)
or
(e)
of this Section,
respectively.
e)
Any owner or operator of a printing line subject to the
limitations of Section 218.401 of this Part and
complying by means of Section 218.401(c)
of this Part
shall comply with the following:
1)
By
a date consistent with Section 218.106 of this
Part, or upon initial start-up of a new printing
line, or upon changing the method of compliance
for an existing printing line from Section
218.401(a)
or
(b)
of this Part to Section
218.401(c)
of this Part,
the owner or operator of
the subject printing line shall perform all tests
and submit to the Agency the results of all tests
and calcuiations necessary to demonstrate that the
subject printing line will be in compliance with
Section 218.401(c)
of this Part on and after a
date consistent with Section 218.106 of this Part,
or on and after the initial start-up date.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date,
the owner or operator of a printing
line subject to the limitations of Section 218.401
of this Part and complying by means of Section
218.401(c)
of this Part shall collect and record
all of the following information each day for each
printing line and maintain the information at the
facility for a period of three years:
A)
Control device monitoring data.
B)
A log of operating time for the capture
system,
control device, monitoring equipment
and the associated printing line.
C)
A maintenance log for the capture system,
control device and monitoring equipment
detailing all routine and non-routine
maintenance performed including dates and
duration of any outages.
3)
On and after a date consistent with Section
218.106 of this Part,
the owner or operator of
a

235
subject printing line shall notify the Agency in
the following instances:
A)
Any record showing violation of Section
218.401(c)
of
this
Part,
shall
be
reported
by
sending
a
copy
of
such
record
to
the
Agency
within
30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with Section 218.401 Qf.
this Part from Section 218.401(c)
of this
Part to Section 218.401(a)
or
(b)
of this
Part,
the
owner
or
operator
shall
comply
with
all requirements of subsection
(c) (1)
or
(d) (1)
of this Section, respectively.
Upon
changing the method of compliance with
Section 218.401 of this Part from Section
218.401(c)
of this Part to Section 218.401(a)
or
(b)
of this Part, the owner or operator
shall comply with all requirements of
subsection
(c)
or
(d) of this Section,
respectively.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.405
Heatset-Web—OffsCt Lithographic Printing
a)
Applicability
1)
The limitations
of subsection
(b)
below apply to
all heatset-web—offset lithographic printing lines
(including solvents used for cleanup operations
associated with the heatset—web-offset
lithographic printing line(s))
at a subject
faciiitysource.
All facilities sources with
heatset-web-offset lithographic printing lines are
subject facilitiessources unless:
A)
Total maximum theoretical emissions of VON
from all heatset—web-offset lithographic
printing lines (including solvents used for
cleanup operations associated with the
heatset-web-offset lithographic printing
line(s))
at the facilitysource never exceed
90.7 Mg
(100 tons)
per calendar year in the
absence of air pollution control equipment,
or

236
B)
A federally enforceable oonstruotion permit
or SIP revision for all heatset-web-offset
lithographic printing line(s)
at
a facility
source requires the owner or operator to
limit production or capacity of these
printing line(s)
to reduce total VON
emissions from all heatset—web—offset
lithographic
printing
line(s)
to
90.7
Mg
(100 tons)
per calendar year or less
in the
absence of air pollution control equipment,
and
2)
Any owner or operator of any heatset—web—offset
lithographic printing line that is exempt from the
limitations in subsection
(b)
of this Section
because of the criteria in subsection
(a) (1)
of
this Section shall be subject to the recordkeeping
and reporting requirements in subsection
(c) (1)
~f
this Section.
b)
Specific Provisions.
No owner or operator of a subject
heatset-web-offset printing line may cause or allow the
operation of the subject heatset-web-offset printing
line unless the owner or operator meets the
requirements in subsection
(b) (1)
or
(b) (2) and the
requirements in subsections
(b) (3)
and
(b) (4)
below.
1)
An afterburner system is installed and operated
that reduces 90 percent of the VON emissions from
the dryer exhaust,
or
2)
The fountain solution contains no more than
8 percent, by weight,
of VON and a condensation
recovery system is installed and operated that
removes at least 75 percent of the non—isopropyl
alcohol organic materials from the dryer exhaust,
and
3)
The control device is equipped with the applicable
monitoring equipment specified in Section
218.105(d) (2)
of this Part and the monitoring
equipment is installed, calibrated,
operated and
maintained according to vendor specifications at
all times the control device
is in use, and
4)
The control device is operated at all times when
the subject printing line is in operation.
The
owner or operator shall demonstrate compliance
with this Section by using the applicable test
methods and procedures specified in Section
218.105(a),
(d), and
(f)
of this Part and by

237
complying with the recordkeeping and reporting
requirements specified in subsection
(c) below.
C)
Recordkeeping and Reporting.
The VON content of each
fountain solution and ink and the efficiency of each
Control device shall be determined by the applicable
test methods and procedures specified in Section
2~8.105of this Part to establish the records required
Under this subsection.
1)
Any owner or operator of a printing line which is
exempted from the limitations of subsection
(b) Q~.
this Section because of the criteria in subsection
(a)
of this Section shall comply with the
following:
A)
By a date consistent with Section 218.106 2f
this Part,
the owner or operator of a
facility
heatset- web-offset lithographic
printing line to which subsection
(c) (1)~f
this Section is applicable shall certify to
the Agency that the facility heatset-web-
offset lithographic printing line is exempt
under the provisions of subsection
(a)
~f
this Section.
Such certification shall
include:
i)
A declaration that the facility heatset-
web—offset lithographic printing line is
exempt from the limitations of
subsection
(b)
of this Section because
of the criteria in subsection
(a)
~f
this Section,
and
ii)
Calculations which demonstrate that
total maximum theoretical emissions of
VON from all heatset-web—offset
lithographic printing lines at the
facilitysource never exceed 90.7 Mg
(100 tons)
per calendar year before the
application of air pollution control
equipment.
Total maximum theoretical
emissions of VOM for a heatset—web—
offset lithographic printing facility
source is the sum of maximum theoretical
emissions of VON from each heatset—web-
offset lithographic printing line at the
facilitysource.
The following equation
shall be used to calculate total maximum
theoretical emissions of VON per
calendar year in the absence of air
pollution control equipment for each

238
heatset-web-offset lithographic printing
line at the
facilitysource.
E~=(Ax
B) +(CxD)+1095
(FxGxHI
100
where:
Total
maximum
theoretical
emissions of VOM from one
heatset-web-offset printing
line in units of kg/year
(lbs/year),-.~
A
=
Weight of VON per volume of
solids of ink with the highest
VON content as applied each
year on the printing line in
units of kg VON/i
(lbs
VON/gal)
of solids-~-—and~
B
=
Total volume of solids for all
inks that can potentially be
applied
each
year
on
the
printing line in units of
1/year (gal/year). The
instrument or method by which
the owner or operator
accurately measured or
calculated the volume of each
ink as applied and the amount
that can potentially be
applied
each
year
on
the
printing line shall be
described in the certification
to the Agency-~
C
=
The weight percent VOM of the
fountain solution with the
highest VON content-~
D
=
The total volume of fountain
solution that can potentially
be used each year on the
printing line
in units of
1/year
(gal/year).
The
instrument and/or method by
which the owner or operator
accurately measured or
calculated the volume of eaci
fountain solution used and t~

239
amount that can potentially be
used each year on the printing
line shall be described in the
certification to the Agency-a
Weight of VON per volume of
material for the cleanup
material or solvent with the
highest VON content as used
each year on the printing line
in units
of Kg/i
(lbs VON/gal)
of such material;
The greatest volume of cleanup
material or solvent used in
any 8-hour period and
The highest fraction of
cleanup material or solvent
which is not recycled or
recovered for offsite disposal
during any 8—hour period.
B)
On and after a date consistent with Section
218.106 of this Part, the owner or operator
of a facilityheatset-web-offset lithographic
printing line to which subsection
(C)
(1)
of
this Section is applicable shall collect and
record
all
of
the
following
information
each
year for each printing line and maintain the
information at the facilitysource for
a
period of three years:
i)
The name and identification of each
fountain solution and ink as applied on
each printing line.
ii)
The VON content and the volume of each
fountain solution and ink as applied
each year on each printing line.
C)
On and after a date consistent with Section
218.106 of this Part,
the owner or operator
of a facilitysource exempted from the
limitations of subsection
(b)
of this Section
because of the criteria in subsection
(a)
of
this Section shall notify the Agency of any
record showing that total maximum theoretical
emissions of VON from all printing lines
exceed 90.7 Mg
(100 tons)
in any calendar
year in the absence of air pollution control
equipment by sending a copy of such record to

240
the
Agency
within
30
days
after
the
exceedance occurs.
2)
Any owner or operator of a printing line subject
to the limitations of subsection
(b)
of this
Section and complying by means of subsection
(b) (1)
of this Section shall comply with the
following:
A)
By
a date consistent with Section 218.106
~i
this Part, or upon initial start-up of a new
printing line,
or upon changing the method of
compliance for an existing printing line from
subsection
(b) (2)
to subsection
(b) (1) ~
this Section the owner or operator of the
subject printing line shall perform all tests
and submit to the Agency the results of all
tests and calculations necessary to
demonstrate that the subject printing line
will be in compliance with subsection
(b) (1)
of this Section on and after a date
consistent with Section 218.106 of this Part,
or on and after the initial start-up date.
B)
-
On and after a date consistent with Section
218.106 of this Part,
or on and after the
initial start-up date, the owner or operator
of a printing line subject to the limitations
of subsection
(b) of this Section and
complying by means of subsection
(b) (1)
~f
this Section shall collect and record the
following information each day for each
printing line and maintain the information at
the faciiitysource for a period of three
years:
i)
Control device monitoring data.
ii)
A log of operating time for the control
device, monitoring equipment and the
associated printing line..
iii) A maintenance log for the control device
and monitoring equipment detailing all
routine and nonroutine maintenance
performed including dates and duration
of any outages.
C)
On and after a date consistent with Section
218.106 of this Part,
the owner or operator
of a subject printing line shall notify the
Agency
in the following instances:

241
i)
Any record showing violation of
subsection
(b) (1)
of this Section shall
be reported by sending a copy of such
record to the Agency within 30 days
following the occurrence of the
violation.
ii)
At
least
30
calendar
days
before
changing the method of compliance with
subsection
(b)
of this Section from
subsection
(b) (1) to
(b) (2)
of this
Section, the owner or operator shall
comply with all requirements of
subsection
(C)
(3) (A)
of this Section.
Upon changing the method of compliance
with subsection
(b)
of this Section from
subsection
(b) (1) to
(b) (2)
of this
Section, the owner or operator shall
comply with all requirements of
subsection
(c) (3)
of this Section.
3)
Any owner or operator of a printing line subject
to the limitations of subsection
(b)
of this
Section and complying by means of subsection
(b) (2)
of this Section shall comply with the
following:
A)
By a date consistent with Section 218.106 p1
this Part, or upon initial start-up of a new
printing line,
or upon changing the method of
compliance for an existing printing line from
subsection
(b) (1) to
(b) (2)
of this Section
the owner or operator of the subject printing
line shall perform all tests and submit to
the Agency and the USEPA the results of all
tests and calculations necessary to
demonstrate that the subject printing line
will be in compliance with subsection
(b) (2)
of this Section on and after a date
consistent with Section 218.106 of this Part,
or on and after the initial start-up date.
B)
On and after a date consistent with Section
218.106 of this Part,
or on and after the
initial start—up date,
the owner or operator
of
a printing line subject to the limitations
of subsection
(b)
of this Section and
complying by means of subsection
(b)(2)
p1
this Section shall collect and record the
following information each day for each
printing line and maintain the information at

242
the facilitysource for a period of
three years:
1)
The VON content of the fountain solution
used each day on each printing line.
ii)
A log of operating time for the control
device and the associated printing line.
iii) A maintenance log for the control device
detailing all routine and non-routine
maintenance performed including dates
and duration of any outages.
C)
On and after a date consistent with Section
218.106 of this Part, the owner or operator
of a subject printing line shall notify the
Agency in the following instances:
i)
Any record showing violation of
subsection
(b) (2)
shall be reported by
sending a copy of such record to the
Agency within 30 days following the
occurrence
of
the
violation.
ii)
At least 30 calendar days before
changing the method of compliance with
subsection
(b)
of this Section from
subsection
(b) (2)
to
(b) (1)
of
this
Section,
the owner or operator shall
comply with all requirements of
subsection
(c) (2) (A)
of this Section.
Upon changing the method of compliance
with subsection
(b)
of this Section from
subsection
(b) (2)
to
(b)
(1)
of this
Section, the owner or operator shall
comply with all requirements of
subsection
(c) (2)
of this Section.
d)
Compliance Schedule.
Every owner or operator of
a
heatset-web-offset lithographic printing line shall
comply with the applicable requirements of subsections
(b) and
(c)
of this Section in accordance with the
applicable compliance schedule specified in subsection
(d) (1),
(d) (2),
or
(d) (3)
below:
1)
No owner or operator of a heatset—web—offset
lithographic printing line which
is exempt from
the limitations of subsection
(b)
of this Section
because of the criteria in subsection
(a)
of this
Section shall operate said printing line on or
after a date consistent with Section 218.106
p1

243
this Part, unless the owner or operator has
complied with,
and continues to comply with,
subsection -(-~)-j.~j(1)and
(c) (1)
of this Part.
2)
No owner or operator of a heatset—web—offset
lithographic printing line complying by means of
subsection
(b) (1)
of this Section shall operate
said printing line on or after a date consistent
with Section 218.106 of this Part, unless the
owner or operator has complied with,
and continues
to comply with,
subsection
(b) (2)
(b) (1)~ (b) (3),
fb) (4)
and
(c) (2)
of this Section.
3)
No
owner
or
operator
of
a
heatset—web—offset
lithographic printing line complying by means of
subsection
(b) (2) of this Section shall operate
said printing line on or after a date consistent
with Section 218.106 of this Part, unless the
owner or operator has complied with,
and continues
to comply with,
subsection
(b) (2),
(b) (3).
(b) (4)
and
(c) (3)
of this Section.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
_________________________ )
SUBPART
Q:
LEANS
FROM SYNTHETIC ORGANIC CHEMICAL AND POLYMER
MANUFACTURING EQUIPMENT PLANT
Section
218.421
General
Requirements
The owner or operator of a plant which processes more than 3660
mg/yr
(4033 tons/year)
gaseous and light liquid VON, and whose
components are used to manufacture the synthetic organic
chemicals or polymers listed in Appendix A,
shall comply with
this Subpart.
The provisions of this Subpart are applicable to
components containing 10 percent or more by weight VON as
determined by ASTM method E-i68,
E-i69 and E-260,
incorporated by
reference in Section 218.112 of this Part.
Those components that
are not process unit components are exempt from this Subpart.
A
component shall be considered to be leaking
if the VON is equal
to,
or is greater than 10,000 ppmv as methane or hexane as
determined by USEPA Reference Method 21,
as specified at 40 CFR
60, Appendix A,
incorporated by reference in Section 218.112
p1
this
Part,
indication
of
liquids
dripping,
or
indication
by
a
sensor that a seal or barrier fluid system has failed.
The
provisions of this Subpart are not applicable if the equipment
components are used to produce heavy liquid chemicals only from
heavy
liquid feed or raw materials.
(Source:
Amended at
Ill. Reg.
______,
effective
____________

244
Section 218.422
Inspection Program Plan for Leaks
The owner or operator of a synthetic organic chemical or polymer
manufacturing plant subject to Section 218.421 of this Part shall
prepare an inspection program plan which contains,
at a minimum:
a)
An identification of all components and the period in
which each will be monitored pursuant to Section
218.423 of this Part.
b)
The format for the monitoring log required by Section
218.425 of this Part.
c)
A description of the monitoring equipment to be used
when complying with Section 218.423 of this Part;
and
d)
A description of the methods to be used to identify all
pipeline valves, pressure relief valves
in gaseous
service,
all leaking components, and components
exempted under Section
218.423-(4)-Lfl.. of this Part such
that they are obvious and can be located by both plant
personnel performing monitoring and Agency personnel
performing inspections.
(Source:
Amended
at
Iii. Reg.
,
effective
)
Section 218.423
Inspection Program for Leaks
The owner or operator of a synthetic organic chemical or polymer
manufacturing plant subject to this e~ubpartshall, for the
purposes of detecting leaks, conduct a component inspection
program using the test methods specified in Method 21,
40 CFR 60,
Appendix
A
(1986),
incorporated
by
reference
in
Section
218.112
of this Part,
consistent with the following provisions:
a)
Test annually those components operated near extreme
temperature or pressure such that they would be unsafe
to routinely monitor and those components which would
require the elevation of monitoring personnel higher
than two meters above permanent worker access
structures or surfaces.
b)
Test quarterly all other pressure relief valves in gas
service, pumps in light liquid service, valves in light
liquid service and in gas service, and compressors.
c)
If less than or equal to 2 percent of the valves in
light liquid service and in gas service tested pursuant
to subsection
(b)
of this Section are found
fi9~
to leak
for five consecutive quarters,
no leak tests shall be
required for three consecutive quarters.
Thereafter,
leak tests shall resume for the next quarter.
If that

245
test shows less than or equal to
2 percent of the
valves in light liquid service and in gas service are
leaking, then no tests are required for the next
three quarters.
If more than
2 percent are leaking,
then tests are required for the next five quarters.
d)
Observe visually all pump seals weekly.
e)
Test immediately any pump seal from which liquids are
observed dripping.
f)
Test any relief valve within 24 hours after it has
vented to the atmosphere.
g)
Routine instrument monitoring of valves which are not
externally regulated, flanges, and equipment in heavy
liquid service,
is not required.
However,
any valve
which is not externally regulated,
flange or piece of
equipment in heavy liquid service that is found to be
leaking on the basis of sight, smell or sound shall be
repaired as soon as practicable but no later than
30 days after the leak is found.
h)
Test immediately after repair any component that was
found
leaking.
.
1)
Within one hour of its detection,
a weatherproof,
readily visible tag,
in bright colors such as red or
yellow, bearing an identification number and the date
on which the leak was detected must be affixed on the
leaking component and remain in place until the leaking
component is repaired.
j)
The following components are exempt from the monitoring
requirements in this Section:
1)
Any component that is in vacuum service, and
2)
Any pressure relief valve that is connected to an
operating flare header or vapor recovery device.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.424
Repairing Leaks
All leaking components must be repaired and retested as soon as
practicable but no later than 15 days after the leak is found
unless the leaking component cannot be repaired until the process
unit is shut down.
Records of repairing and retesting must be
maintained in accordance with Section 218.425 and 218.426 of this
Part.

246
(Source:
Amended
at
Ill.
Reg.
______,
effective
____________
Section
218.425
Recordkeeping
for
Leaks
a)
The
owner
or
operator
of
a
synthetic
organic
chemical
or polymer manufacturing plant shall maintain a leaking
components monitoring log which shall contain, at a
minimum, the following information:
1)
The name of the process unit where the component
is located;
2)
The type of component
(e.g., valve,
seal);
3)
The identification number of the component;
4)
The date on which a leaking component is
discovered;
5)
The date on which
a leaking component is repaired;
6)
The date and instrument reading of the recheck
procedure after a leaking component is repaired;
7)
A record of the calibration of the monitoring
instrument;
8)
The identification number of leaking components
which cannot be repaired until process unit
shutdown; and
9)
The total number of valves in light liquid service
and
in gas service inspected; the total number and
the percentage of these valves found leaking
during the monitoring period.
b)
Copies of the monitoring log shall be retained by the
owner or operator for a minimum of two years after the
date on which the record was made or the report was
prepared.
c)
Copies of the monitoring log shall be made available to
the Agency~upon verbal or written request~prior to or
at the time of inspection pursuant to Section 4(d)
of
the Environmental Protection Act
(Act)
(Ill.
Rev.
Stat.
~
ch.
lii 1/2, pars.
1001 et seq.)
1415 ILCS 5/1
et seg.1 at any reasonable time.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

247
Section
218.426
Report
for
Leaks
The owner or operator of a synthetic organic chemical or polymer
manufacturing plant subject to Section 218.421 through 218.430
p1
this Part shall:
a)
Submit quarterly reports to the Agency on or before
March 31, June 30, September 30, and December
31 of
each year,
listing al~leaking components identified
pursuant to Section 218.423 of this Part but not
repaired within
15 days,
all leaking components
awaiting process unit shutdown, the total number of
components inspected,
the type of components inspected,
and the total number of components found leaking, the
total number of valves in light liquid service and in
gas service inspected and the number and percentage of
valves in light liquid service and in gas service found
leaking.
b)
Submit a signed statement with the report attesting
that all monitoring and repairs were performed as
required under Section 218.421 through 218.427 of this
Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.427
Alternative Program for Leaks
The Agency shall approve an alternative program of monitoring,
recordkeeping,
or reporting to that prescribed in this Subpart
upon
a demonstration by the owner or operator of such plant that
the alternative program will provide piantsource personnel and
Agency personnel with an equivalent ability to identify and
repair leaking components.
Any alternative program can be
allowed if approved by the Agency and approved by the USEPA as a
SIP revision.
(Source:
Amended at
Iii.
Reg.
______,
effective
___________
Section 218.428
Open-Ended Valves
a)
Each open-ended valve shall be equipped with a cap,
blind flange,
plug, or a second valve, except during
operations requiring fluid flow through the open-ended
valve.

248
b)
Each open—ended valve equipped with
a
second
valve
shall be operated in a manner such that the valve on
the process fluid end is closed before the second valve
is closed.
c)
Components which are open—ended valves and which serve
as a sampling connection shall be controlled such that
they com~ivwith subsection(c) (1),
(c) (2)
or
(c) (3)
below.
This requirement does not a~~lv
to in—situ
sampling svstems.÷
1)
A closed purge system or closed vent system shall
return purged process fluid to the process line
with no detectable VON emissions to the
atmosphere, or
2)
A closed purge system or closed vent system shall
collect and recycle purged process fluid to the
process line with no detectable VOM emissions to
the atmosphere,
or
3)
Purged process fluid shall be transported to a
control device that complies with the requirements
of Section 218.429 of this Part.
If a container is
used to transPort purged process fluid to the
control device, the container shall be a closed
container designed and used to reduce the VON
emissions vented from purged process fluid after
transfer to no detectable VON emissions as
determined by USEPA Reference Method 21,
as
specified in
40 CER 60, Appendix A (1990 or 1991)
incorporated by reference in Section 218.112 of
this Part.
For purposes of this Section, the
phrase “after transfer” shall refer to the time at
which the entire amount of purged process fluid
resulting from a flushing or cleaning of the
sample line enters the container,
provided,
however, that ~ur~ed process fluid maY be
transferred from the initial container to another
closed container prior to disposal, e.g.,
to a
bulk waste storage container.
a-)-
In-situ
samr~1ir~r’
—‘~-~-‘-~‘--
exempt
~~sec~
(c).
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.429
Standards for Control Devices
Control devices used to comply with Section 218.428(c)
of this
Part shall comply with the following:

249
a)
If the control device
is a vapor recovery system (for
example, condensers and adsorbers),
it shall be
designed and operated to recover the VOM emissions
vented to it with an efficiency of 95 percent or
greater.
b)
If the control device
is an enclosed combustion device,
it shall be designed and operated to reduce the VON
emissions
vented
to
it
with
an
efficiency
of
95
percent
or greater,
or to provide a minimum residence..time of
0.75 seconds at a minimum temperature of 816°C.
c)
If the control device is a flare,
it shall:
1)
Be designed for and operated with no visible
emissions as determined by USEPA Reference Method
22,
40 CFR 60, Appendix A
(1986),
incorporated by
reference in Section 218.112, except for periods
not to exceed a total of
5 minutes during any 2
consecutive hours.
2)
Be operated with a pilot flame present at all
times and shall be monitored with a thermocouple
or
any
other
equivalent
device
to
detect
the
presence
of
the
pilot
flame.
3)
Be steam—assisted,
air assisted, or nonassisted.
4)
Be used only with the net heating value of the gas
being combusted being 11.2 NJ/scm
(300 Btu/scf)
or
greater if the flare
is steam—assisted or
air-assisted; or with the net heating value of the
gas being combusted being 7.45 NJ/scm or greater
if the flare is nonassisted.
The net heating
value of the gas being combusted shall be
calculated using the following equation:
n
Hr
=
K
E
C1
H1
i=l
Where:
Hr
=
Net heating value of the sample in
NJ/scm;
where the net enthalpy per
mole of offgas
is based on
combustion at 25°Cand 760 mm Hg,
but the standard temperature for
determining the volume
corresponding to one mole
is
2O°C-~j

250
d)
K
=
Constant,
1.740 x
(1/ppm) (g—mole/scm) (NJ/Kcal)
where
standard temperature for
(g-moie/scm)
is
Cl
=
Concentration of sample component
1,
in ppm, as measured by USEPA
Reference Method 18, 40 CFR 60,
Appendix A
(1986), and ASTM D
2504-83, both incorporated by
reference in Section 218.112-u.
H
=
Net heat of combustion of sample
component
i, kcal/g mole.
The
heats of combustion may be
determined using ASTN D 2382-83,
incorporated by reference in
Section 218.112 of this Part,
if
published values are not available
or cannot be calculated.
5)
Steam—assisted and nonassisted flares shall be
designed and operated with an exit velocity, as
determined by dividing the volumetric flowrate
(in
units of standard temperature and pressure),
as
determined by USEPA Reference Method
2 or
2A,
40
CFR 60, Appendix A
(1986)
incorporated by
reference in Section 218.112 of this Part,
as
appropriate; by the unobstructed
(free)
cross
sectional area of the flare tip, less than 18
m/sec
(60 ft/sec).
6)
Air-assisted flares shall be designed and operated
with an exit velocity less than the maximum
permitted velocity, V~, as determined by the
following equation:
~~max
=
8.706
+ 0~7084(Hr)~L
V~
=
Maximum permitted velocity, m/see.j
8.706
=
Constant-~L
0.7084
=
Constant-~j
=
The net heating value as determined
in subsection
(c) (4)
of this
section.
If the control device is a closed container,
it shall
be designed and operated to reduce the VON emissions,
vented from purged process fluid after transfer, to—ne

251
-
-
-
~S
t~- -
H
~“Appcndi~
erence
in
~
Cection
218.
112.
A
(1986),
~
by
ref
For purposes of this Ccction, -the ~
transfer” shall refer to the time at which the entire
amount of purged process fluid resulting from a
flushing or cleaning of the sample line enters the
closed container or containers including the final
container(s) prior to disposal.
The following
information pertaining to closed vent systems and
control devices subiect to Section 218.429 shall be
maintained bY the owner or operator.
These records
shall be updated as necessary to describe current
operation and eciuipment.
The records shall be retained
at
a readily accessible location at the source for a
minimum of two Years after the control device
is
permanently shutdown.
fl
Detailed schematics,
design specifications,
and
piping and instrumentation diagrams
21
The dates and description of any changes in design
specifications;
A description of the parameter or Parameters
monitored and recorded as reguired in subsection
(f) (1) to ensure that the control devices are
operated and maintained in conformance with their
design and an explanation why that Parameter
(or
Parameters) was selected for monitoring.
a control device shall monite~
~.L...L..
~L
~
.~
tnc
ConLEpi. acvioe
to cn~urc
LUUL
.LL
.L~3
Upt.LU1..eU
UJ1U
maintained in conformance
specifications,
modified
with
to the
the
pa
manufacturer’s
rticular process
design.
~)
The control device shall be operated at all times when
emissions may be vented to it.
~j
Owners and oPerators
of control devices used to comply
with this Subpart shall monitor each control device to
ensure that the control device is onerated and
maintained in conformance with its designs at all times
that emissions may be vented to it.
This monitoring
shall be conducted in accordance with Section
218.429(d) (3). The records prepared as Part of this
monitoring activity shall include the dates of startup
and shutdown of control devices and identify periods
when the devices are not operated as designed,
including periods when a flare pilot light does not
have a flame.

252
gj..
The requirements of subsections
(d),
(e)
and
(f)
shall
not aP~iYto a combustion device located at the source
used for disposal of purged process fluid which is
subject to the Burning of Hazardous Waste
in Boilers
and Industrials Furnaces
(BIF) rules, 40 CFR Parts 260,
261,
264.
265, 266, and 270, or which is subiect to the
Resource Conservation and Recovery Act
(RCRA)
rules,
35
Ill. Mm.
Code Parts 703,
720, 721,
724k 725, and 726.
The owner or oPerator of such combustion device shall
satisfy applicable provisions of the RCRA or BIF rules.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.430
Compliance Date
(Repealed)
The owner or operator of a synthetic organic chemical or polymer
manufacturing plant subject to 35
Ill. Adm. Code 215.430 through
215.438 as of December
31,
1987 shall have complied with the
standards and limitations of those Cections no later than
D-eccnwcr
3i,
~
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
SUBPART
R:
PETROLEUM REFINING AND RELATED INDUSTRIES;
ASPHALT MATERIALS
Section 218.441
Petroleum Refinery Waste Gas Disposal
a)
Except as provided in subsection
(b)
or
(c)
of this
Section,
no person shall cause or allow the discharge
of organic materials in excess of 100 ppm equivalent
methane
(molecular weight
16.0)
into the atmosphere
from:
1)
Any catalyst regenerator of a petroleum cracking
system; or
2)
Any petroleum fluid coker;
or
3)
Any other waste gas stream from any petroleum or
petrochemical manufacturing process.
b)
Exception.
Existing sources subject to subsection
(a) (3)
of this Section may, alternatively, at their
election, comply with the organic material emission
limitations imposed by 35 Ill. Adm. Code 21~.301or
2i~.302;provided, however, that there shall be no
increase in emissions from such sources above the level
of emissions in existence on May 3,
1979.

253
c)
New Sources.
Sources subject to subsection
(a) (3)
p1
this Section, construction of which commenced on or
after January
1,
1977, may,
at their election,
comply
with the following emission limitations:
1)
A maximum of eight pounds per hour of organic
materiai;
or
2)
Emission of organic material in excess of the
limitation of suk’section
(c) (1)
of this Section is
allowable if such emissions are controlled by air
pollution control methods or equipment approved by
the Agency capable of reducing by 85 percent or
more the uncontrolled organic material that would
otherwise be emitted to the atmosphere.
Such
methods or equipment must be approved by the
Agency and approved by the USEPA as a SIP
revision.
(Source:
Amended at
Ill. Reg.
,
effective
____________
Section 218.443
Wastewater
(Oil/Water) Separator
No owner or operator of a petroleum refinery shall operate any
wastewater
(oil/water) separator at a petroleum refinery unless
the separator is equipped with air pollution control equipment
capable of reducing by 85 percent or more the uncontrolled
organic material emitted to the atmosphere.
If no odor nuisance
exists, the limitation of this Section shall not apply if the
vapor pressure of the organic material
is below 10.34 kPa
(1.5
psia)
at 29~4.3°K(70°F) at all times.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section
218.445
Leaks:
General Requirements
a3-The owner or operator of a petroleum refinery shall:
~)
Develop a monitoring program plan consistent with the
provisions of Section 218.446;
~)
Conduct a monitoring program consistent with the
provisions of Section 218.447;
~3p) Record all leaking components which have a volatile
organic material concentration exceeding 10,000 ppm
consistent with the provisions of Section 218.448;
4~)
Identify each component consistent with the monitoring
program plan submitted pursuant to Section 218.446;

254
~)
Repair
and retest the leaking components as soon as
possible within 22 days after the leak is found,
but no
later than June
1 for the purposes of Section
218.447(a) (1), unless the leaking components cannot be
repaired until the unit is shut down for turnaround;
and
6~) Report to the Agency consistent with the provisions of
Section 218.449.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.446
Monitoring Program Plan for Leaks
The owner or operator of a petroleum refinery shall prepare a
monitoring program plan which contains,
at a minimum:
a)
An identification of all refinery components and the
period in which each will be monitored pursuant to
Section 218.447 of this part
b)
The format for the monitoring log required by Section
218.448 of this part
c)
A description of the monitoring equipment to be used
pursuant to Section 218.447 of this part and
d)
A description of the methods to be used to identify all
pipeline valves, pressure relief valves in gaseous
service and all leaking components such that they are
obvious to both refinery personnel performing
monitoring and Agency personnel performing inspections.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.447
Monitoring Program for Leaks
a)
The owner or operator of a petroleum refinery subject
to Section 218.445 of this Part shall,
for the purpose
of detecting leaks, conduct a component monitoring
program consistent with the following provisions:
1)
Test once between March
1 and June
1 of each year,
by methods referenced in Section 218.105(g)
p1
this Part,
all pump seals, pipeline valves
in
liquid service and process drains--j
2)
Test once each quarter of each calendar year,
by
methods referenced in Section 218.105(g)
of this
Part,
all pressure relief valves in gaseous

255
service, pipeline valves
in gaseous service and
compressor seals--j
3)
Inaccessible valves may be tested once each
calendar year instead of once each quarter of each
calendar
year~-.~
4)
Observe
visually
all
pump
seals
weekly.~j
5)
Test immediately any pump seal from which liquids
are observed dripping~~
6)
Test any relief valve within 24 hours after it has
vented to the atmosphere-a and
7)
Test immediately after repair any component that
was found leaking.
b)
Storage tank valves and pressure relief devices
connected to an operating flare header or vapor
recovery device are exempt from the monitoring
requirements in subsection
(a)
of this Section.
C)
The Agency or the USEPA may require more frequent
monitoring than would otherwise be required by
subsection
(a)
for components which are demonstrated to
have a history of leaking.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.449
Reporting for Leaks
The owner or operator of a petroleum refinery shall:
a)
Submit a report to the Agency prior to the 1st day of
both July and September listing all leaking components
identified pursuant to Section 218.447 of this Part but
not repaired within 22 days, all leaking components
awaiting unit turnaround,
the total number of
components inspected and the total number of components
found leaking;
b)
Submit a signed statement with the report attesting
that all monitoring and repairs were performed as
required under Sections 218.445 through 218.448 of this
Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

256
Section 218.450
Alternative Program for Leaks
The Agency may approve an alternative program of monitoring,
recordkeeping or reporting to that prescribed in Sections 218.446
through 218.449 of this Part upon a demonstration by the owner or
operator of a petroleum refinery that the alternative program
will provide refinery, Agency and USEPA personnel with an
equivalent ability to identify and repair leaking components.
Any alternative program can be allowed only if approved by the
USEPA as a SIP revision.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.452
Compliance Schedule for Leaks
The owner or operator of
a petroleum refinery shall adhere to the
increments of progress contained in the following schedule:
a)
Have submitted to the UCEPAAgency a monitoring program
consistent with Section 218.446 of this Part prior to
September
1,
1990.
b)
Have submitted to the IJCEPAAgency the first monitoring
report pursuant to Section 218.449 of this Part prior
to October
1,
1990.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
______
)
Section 218.453
Compliance Dates
(Repealed)
Every
owner
or
operator
of
a petroleum refinery subject to 35
‘‘
Code
215,
Subp~:-~
~
1987 shall
1~IJ~
.1
r
L
It
.TI
~
ti!
~
.)
f
I
._1
V t~
oompiieu
WILU
i~
~unaarus
and limitation~i
uy
ucue~wcr
.~i,
i.s87.
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
SUBPART 5:
RUBBER
AND MISCELLANEOUS PLASTIC PRODUCTS
Section 218.461
Manufacture of pneumatic Rubber Tires
The owner or operator of an undertread cementing, treadend
cementing or bead dipping operation at a pneumatic rubber tire
manufacturing facilitysource shall install and operate:
a)
A capture system, with minimum capture efficiency of 65
percent by weight of VON for treadend cementing or bead
dipping operations and a capture system with a minimum
capture efficiency of 55.5 percent by weight of VOM for
undertread cementing;
and

257
b)
A control device that meets the requirements of one of
the following:
1)
A carbon adsorption system designed and operated
in a manner such that there is at least
a 90
percent removal of VON by weight from the gases
ducted to the control device;
2)
An
afterburning
system
that
oxidizes
at
least
90
percent of the captured nonmethane VOMs
(VON
measured as total combustible carbon) to carbon
dioxide
and
water;
and
3)
An alternative VON emission reduction system
demonstrated to have at least a 90 percent overall
reduction efficiency and approved by the Agency
and approved by the USEPA as a SIP revision.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.462
Green Tire Spraying Operations
The owner or operator of a green tire spraying operation at
a
pneumatic rubber tire manufacturing facilitysource shall:
a)
Install and operate:
1)
A capture system with a minimum capture efficiency
of 90 percent by weight of VOM; and
2)
A control device that meets the requirements of
one of the following:
A)
A
carbon adsorption system designed and
operated in
a manner such that there
is at
least 90 percent removal of VOM by weight
from the basesgases ducted to the control
device;
B)
An afterburning system that oxidizes at least
90 percent of the captured nonmethane VOM
(measured as total combustible carbon)
to
carbon dioxide and water; or
C)
An alternative VON emission reduction system
demonstrated to have at least a 90 percent
overall reduction efficiency and approved by
the Agency and approved by the USEPA as a SIP
revision.

258
b)
Substitute for the normal solvent—based mold release
compound water-based sprays containing:
1)
No more than five percent by volume of VOM as
applied for the inside of tires;
2)
No
more
than
ten
percent
by
volume
of
VON
as
applied for the outside of tires.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________ )
Section 218.463
Alternative Emission Reduction Systems
In lieu of complying with Section 218.461 or 218.462 of this
Part, the owner or operator of an emission source may utilize an
alternative volatile organic emission reduction system,
including
an alternative production process, which
is demonstrated to be
equivalent to Section 218.461 or 218.462 of this Part on
the basis of emissions of volatile organic mattcrmaterial.
A
treadend cementing operation shall be considered equivalent to
Section 218.461 or 218.462 of this Part for the purposes of this
Section if the total volatile organic emission from such
operation is 10 grams or less per tire.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.464
Testing and HonitoringEmission Testing
a)
Upon a reasonable request by the Agency, the owner or
operator of a VON emission source required to comply
with a limit of Sections 218.461 through 218.464
p1
this Part shall conduct emissions testing, at such
person’s own expense,
to demonstrate compliance.
b)
A
person planning to conduct a VON emission test to
demonstrate compliance shall notify the Agency of that
intent not less than 30 days before the planned
initiation of the tests so the Agency may observe the
test.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.465
Compliance Dates
(Repealed)
Every
owner—or operator of an emission source subject to
35 Ill.
A4m.
Code
215,
Subpart
6,
as of December 31,
1987 shall have
eemplicd with its standards and limitations by December 31,
1937.

259
(Source:
Repealed at
Ill. Reg.
______,
effective
___________
Section 218.466
Compliance Plan fRepealed)
a-)-
The owner or operator of an emission source shall have
submitted
to
the
Agency
a
compliance
plan,
pursuant
to
35 Ill. Adm. Code 201, Subpart H,
including a project
completion schedule where applicable,
no later than
April
21,
1983.
b.)-
Unless the submitted compliance plan or schedule was
disapproved
by
the-Agency,
the
owner
or
operator
of
a
facility or emission source may operate the emission
source according to the plan and schedule as submitted.
a.)-
The plan and schedule shall meet the requirements of 35
Ill. Adm. Code 201, Subpart H, including specific
interim
dates
~
rc~rmircd
in
35
Ill. Adm. Code 201.242.
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
SUBPART T:
PHARMACEUTICAL MANUFACTURING
Section 218.480
Applicability
a)
The rules of this Subpart, except for Sections 218.483
through 218.485 of this Part, apply to all emission
sourcesunits of VON, including but not limited to
reactors, distillation units, dryers, storage tanks -for
VOL, equipment for the transfer of VOL, filters,
crystallizers, washers,
laboratory hoods,
pharmaceutical
coating
operations,
mixing
operations
and centrifuges used in manufacturing,
including
packaging,
of pharmaceuticals,
and emitting more than
6.8 kg/day
(15 lbs/day)
and more than 2,268 kg/year
(2.5 tons/year)
of VON.
If such an emission sourceunit
emits less than 2,268 kg/year
(2.5 tons/year)
of VON,
the requirements of this Subpart still apply to the
emission sourceunit if VON emissions from the emission
sourceunit exceed 45.4 kg/day
(100 lbs/day).
b)
Notwithstanding subsection
(a)
of this Section, the air
suspension coater/dryer, fluid bed dryers, tunnel
dryers, and Accelacotas located in Libertyville
Township, Lake County,
Illinois shall be exempt from
the rules of this Subpart, except for Sections 218.483
through 218.485,
if emissions of VON not vented to air
pollution control equipment do not exceed the following
levels:

260
1)
~or
the air suspension coater/dryer:
2,268
kg/year
(2.5
tons/year);
2)
~or
each
fluid
bed
dryer:
4,535
kg/year
(5.0 tons/year);
3)
~or
each tunnel dryer:
6,803
kg/year
(7.5
tons/year)~and
4)
~or
each Accelacota:
6,803 kg/year
(7.5 tons/year).
c)
Sections 218.483 through 218.485 of this Part apply to
a plantsource having one or more emission sourccsunits
that:
1)
Are used to manufacture pharmaceuticals,
and
2)
Emit more than 6.8 kg/day
(15 lbs/day)
of VON and
more than 2,268 kg/year (2.5 tons/year)
of VON,
or,
if less than 2,268 kg/year
(2.5 tons/year),
these Sections still apply if emissions from one
or more sources exceed 45.4 kg/day
(100 lbs/day).
d)
No owner or operator shall violate any condition in a
permit when the condition results in exclusion of an
emission sourccunit from this Subpart.
e)
Any
pharmaceutical
manufacturing
source
that
becomes
subject to the provisions of this Subpart
a-t any time
shall remain subject to the provisions of this Subpart
at all times.
f)
Emissions subject to this Subpart shall be controlled
at all times consistent with the requirements set forth
in this Subpart.
g)
Any control device required pursuant to this Subpart
shall be operated at all times when the source it is
controlling is operated.
h)
Determinations of daily and annual emissions for
purposes of this Section shall be made using both data
on the hourly emission rate
(or the emissions per unit
of throughput)
and appropriate daily and annual data
from records of emission sourceunit operation (or
material throughput or material consumption data).
In
the absence of representative test data pursuant to
Section 218.487 of this Part for the hourly emission
rate
(or the emissions per unit of throughput), such
items shall be calculated using engineering
calculations,
including the methods described in

261
-
Appendix B of “Control of Volatile Organic Emissions
from Manufacturing of Synthesized Pharmaceutical
Products”
(EPA-450/ 2-78-029),
incorporated by
reference in Section 218.112 of this Part.
(This
subsection shall not affect the Agency’s or the USEPA’s
authority to require emission tests to be performed
pursuant to Section 218.487 of this Part.)
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.481
Control of Reactors, Distillation Units,
Crystallizers, Centrifuges and Vacuum Dryers
a)
The owner or operator shall equip all reactors,
distillation units,
crystallizers, centrifuges and
vacuum dryers that are used to manufacture
pharmaceuticals with surface condensers or other air
pollution control equipment listed in subsection
(b)
p1
this Section.
If a surface condenser is used,
it shall
be operated such that the condenser outlet gas
temperature does not exceed:
1)
248.2°K(-13°F)when condensing VON of vapor
pressure greater than 40.0 kPa (5.8 psi)
at
294.3°K(70°F),or
2)
258.2°K(5°F)when condensing VON of vapor
pressure greater than 20.0 kPa (2.9 psi)
at
294.3°K(70°F),or
3)
273.2°K(32°F)when condensing VONof vapor
pressure greater than 10.0 kPa
(1.5 psi)
at
294.3°K(70°F), or
4)
283.2°K(50°F)when condensing VOM of vapor
pressure greater than 7.0 kPa
(1.0 psi)
at 294.3°K
(70°F)
,
or
5)
298.2°K(77°F)when condensing VON of vapor
pressure greater than 3.45 kPa
(0.5 psi)
at
294.3°K(70°F).
b)
If a scrubber, carbon adsorber, thermal afterburner,
catalytic afterburner,
or other air pollution control
equipment other than a surface condenser is used,
such
equipment shall provide a reduction in the emissions of
VON of 90 percent or more.
c)
The owner or operator shall enclose all centrifuges
used to manufacture pharmaceuticals and that have an
exposed VOL surface, where the VON in the VOL has a

262
vapor pressure of 3.45 kPa
(0.5 psi)
or more at 294.3°K
(70°F),except as production,
sampling, maintenance, or
inspection procedures require operator access.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
______________________)
Section 218.482
Control of Air Dryers, Production Equipment
Exhaust Systems and Filters
a)
The owner or operator of an air dryer or production
equipment exhaust system used to manufacture
pharmaceuticals shall control the emissions of VON from
such emission sourcesunit by air pollution control
equipment which reduces by 90 percent or more the VON
that would otherwise be emitted into the atmosphere.
b)
The owner or operator shall enclose all rotary vacuum
filters and other filters used to manufacture
pharmaceuticals and that have an exposed VOL surface,
where the VON in the VOL has a vapor pressure of 3.45
kPa
(0.5 psi)
or more at 294~°K(70°F),except as
production,
sampling, maintenance,
or inspection
procedures
require
operator
access.
(Source:
Amended
at
Ill. Reg.
______,
effective
____________
Section 218.483
Material Storage and Transfer
The owner or operator of
a pharmaceutical manufacturing
plantsource shall:
a)
Provide a vapor balance system that is at least
90 percent effective in reducing VON emissions from
truck or railcar deliveries to storage tanks with
capacities equal to or greater than 7.57
m3
(2,000 gal)
that store VOL with vapor pressures greater than
28.0 kPa (4.1 psi)
at 294.3°K(70°F),and
b)
Install,
operate, and maintain pressure/vacuum
conservation vents set at 0.2 kPa
(0.03
psi)
or greater
on all storage tanks that store VOL with vapor
pressures greater than 10 kPa
(1.5 psi)
at 294.3°K
(70°F)
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.485
Leaks

263
The owner or operator of a pharmaceutical manufacturing
plantsource shall repair any component from which a leak of VOL
can be observed.
The repair shall be completed as soon as
practicable but no later than 15 days after the leak is found.
If the leaking component cannot be repaired until the process
unit is shut down, the leaking component must then be repaired
before the unit is restarted.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.486
Other Emission Sources Units
The owner or operator of a washer,
laboratory hood, tablet
coating operation, mixing operation or any other process emission
sourceunit not subject to Sections 218.481 through 218.485
p1
this Part,
and used to manufacture pharmaceuticals shall control
the emissions of VON from such emission sourcesunits by:
a)
Air pollution control equipment which reduces by
81 percent or more the VON that would otherwise be
emitted to the atmosphere,
or
b)
A surface condenser which captures all the VON which
would otherwise be emitted to the atmosphere and which
meets the requirements of Section 218.481(a)
of this
Part and
(b).
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.487
Testing
a)
Upon request by the Agency or the USEPA,
the owner or
operator of any VON emission source subject to this
Subpart or exempt from this Subpart by virtue of the
provisions of Section 218.480 of this Part shall,
at
his own expense, demonstrate compliance to the Agency
and the USEPA by the methods or procedures listed in
Section 218.105(f) (1)
of this Part.
b)
A person planning to conduct a VON emissions test to
demonstrate compliance with this Subpart shall notify
the Agency and the USEPA of that intent not less than
30 calendar days before the planned initiation of the
test.
(Source:
Amended at
Ill. Reg.
______,
effective
____________

264
Section 218.489
Recordkeeping for Air Pollution Control
Equipment
a)
The owner or operator of a pharmaceutical manufacturing
facility source shall maintain the following records:
1)
Parameters listed in Section 218.488(a)-(4-)- of this
Part shall be recorded.
2)
For sourocoemission units subject to Section
218.481, of this Part,
the vapor pressure of VON
being controlled shall be recorded for every
process.
b)
For any leak subject to Section 218.485 of this Part
which cannot be readily repaired within one hour after
detection,
the following records shall be kept:
1)
The name of the leaking equipment,
2)
The date and time the leak is detected,
3)
The action taken to repair the leak,
and
4)
The dat~aand time the leak
is repaired.
c)
The following records shall be kept for emission
sourccsunits subject to Section 218.484 of this Part
which contain VOL:
1)
For maintenance and inspection:
A)
The date and time each cover is opened,
B)
The length of time the cover remains open,
and
C)
The reason why the cover
is opened.
2)
For production and sampling, detailed written
procedures or manufacturing directions specifying
the circumstances under which covers may be opened
and the procedures for opening covers.
d)
For each emission sourceunit used in the manufacture of
pharmaceuticals for which the owner or operator of a
pharmaceutical manufacturing plantsource claims
emission standards are not applicable, because the
emissions are below the applicability cutoffs in
Section 218.480(a)
or 218.480(b)
of this Part, the
owner or operator shall:

265
1)
Maintain
a demonstration including detailed
engineering calculations of the maximum daily and
annual emissions for each such emission sourceunit
showing that the emissions are below the
applicability cutoffs in Section 218.480(a)
or
218.480(b)
of this Part, as appropriate,
for the
current and prior calendar years;
2)
Maintain appropriate operating records for each
such emission source to identify whether the
applicability cutoffs in Section 218.480(a)
or
218.480(b)
of this Part, as appropriate, are ever
exceeded; and
3)
Provide written notification to the Agency and the
USEPA within 30 days of a determination that such
an emission sourceunit has exceeded the
applicability cutoffs in Section 218.480(a)
or
218.480(b) pf this Part,
as appropriate.
e)
Records required under subsection
(a)
of this Section
shall be maintained by the owner or operator for a
minimum of two years after the date on which they are
made.
f)
Copies of the records shall be made available to the
Agency or the USEPA upon verbal or written request.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
SUBPART
V:
AIR OXIDATION PROCESSES
Section 218.521
Definitions
(Repealed)
In addition to the definitions
of
35
Ill.
Adm. Code 211, Section
218.104 cnc Loiiow~1r1definitions
~r~r~1~:
to this Subpart:
“Air Oxidation Process”:
any unit process including
and o::::~i:~
:~ie~
~Jfflfl1(J~
ILI.J
LI
(ill
..~I_H1
I
lU
I
Fl.
L. I (Jfl
~.II
-
u~eL~
U.LL
UL
U
combination of air and oxygen as an oxidant in combination
with one or more organic reactants to produce one or more
organic compounds.
“Cost Effectiveness”:
the annual expense for cost of
control of
a given process stream divided by the reduction
in emissions of
organic
material of that stream.
(F)”.
Vent str
temperature of 20°C.
-c~.m
fi
r~it~
(scm/mm)
at a standard

266
“Full Operating
the facility.
~z1_..
__.-c
“Hourly
Emissions
(E)”:
Hourly
omissions
reported
in
kg/hr
measured at full operating flowratc.
“Net Heating Value (H)”~ Vent stream not heating value
(NJ/scm), where the net cnthalpy per mole of offgas is based
on combustion at 25°Cand 760 mm Hg, but the standard
temperature
for
determining
the
volume
corresponding
to
one
mole is 20°C, as in the definition of “Flow.”
“~-occssVent Stream”:
An emission stream resulting from an
air
oxidation
process.
•1
t~____.____
-ntC_..S!
----i---
(TRE)”
~---~-
~~~2
oxidetionproocesdividcdby
and methods sot forth in this
~i6OO/Hg, ucing the criteria
Subpart and Appendices C and
(Source:
Repealed at
)
Section 218.525
Ill. Reg.
______,
effective
Emission Limitations for Air Oxidation
Processes
a)
No
person
shall
cause
or
allow
the
emission of VON from
any process vent stream unless the process vent stream
is vented to a combustion device which is designed and
operated either:
1)
To reduce the volatile organic emissions vented to
it with an efficiency of at least ninety eight
percent
(98)
by weight; or
2)
To emit VOM at a concentration less than twenty
parts per million by volume, dry basis.
b)
Aj~Aairoxidation facilitiesprocess vent stream for
which an existing combustion device is employed to
control process VON emissions a-~-ej~
not required to
meet the
98 percent emissions limit until the
combustion device is replaced for other reasons, which
shall be considered to include, but not be limited to,
normal maintenance, malfunction, accident,
and
obsolescence. The combustion device is considered to be
replaced when:
1)
All of the device is replaced; or

267
2)
When the cost of the repair of the device or the
cost of replacement of part of the device exceeds
50
of the cost of replacing the entire device
with a device which complies.
c)
The limitations of subsection
(a)
above do not apply to
any process vent stream or combination of process vent
streams which has a Total Resource Effectiveness Index
(TRE)
greater than 1.0,
as determined by the following
methods:
1)
If an air oxidation process has more than one
process vent stream, TRE shall be based upon a
combination of the process vent streams.
2)
TRE of a process vent stream shall be determined
according to the following equation:
TRE
=
E1
a
+
bF°
+
cF
+
dFH
+
e(FH)’1
+
fF°-5
where:
n
=
O.88~
TRE
=
Total resource effectiveness
index-~
F
=
Vent stream flowrate (scm/mm),
at
a standard temperature of 20°C-~
E
=
Hourly measured emissions in
kg/hr-~j
H
=
Net heating value of vent stream
(NJ/scm), where the net enthalpy
per mole of offgas
is based on
combustion at 25°Cand 760 mm Hg,
but the standard temperature for
determining the volume
corresponding to one mole is 20°C,
as in the definition of
“Flow”--;
a,b,
c,
d,
e
and f=
Coefficients obtained by use of
Appendix
~.
3)
For nonchlorinated process vent streams,
if the
net heating value,
H,
is greater than 3.6 MJ/scm,
F shall
be replaced by
~! ~
for purposes of
calculating
TRE.
~! F’
is computed as follows:

268
=
FH
/
3.6
where F and H are as defined in subsection
(c) (2)
of this Section.
4)
The actual numerical values used in the equation
described in subsection
(c) (2)
above shall be
determined as follows:
A)
All
reference methods and procedures for
determining the flow,
(F), hourly emissions,
(E), and net heating,
(H), value shall be in
accordance with Appendix C.
B)
All
coefficients described in subsection
(c)
(2)
of this Section shall be in accordance
with Appendix
D.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
_________________________ )
Section 218.527
Compliance Date
(Repealed)
Each owner or opera
Adm.
Code 215, Subp
tor of an
art V,
as
cmi
of
ssion source
December 31,
subj
1987
oat to
shall
35 Ill.
have
complied with the standards and limitations of 35 Ill. Adm.
Code
215, Cubpart V,
by December
31,
1987.
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
SUBPART W:
AGRICULTURE
Section 218.541
Pesticide Exception
The provisions of Sections 218.301 and 218.302 of this Part shall
not apply to the spraying or use of insecticides, herbicides or
other pesticides.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
)
SUBPART
X:
CONSTRUCTION
Section 218.562
Paving Operations
The provisions of Sections 218.301 and 218.302 of this Part shall
not apply to the application of paving asphalt and pavement
marking paint from sunrise to sunset.

269
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
SUBPART Y:
GASOLINE DISTRIBUTION
Section 218.581
Bulk Gasoline Plants
a)
Subject to ~ubsection
(e)
of this Section, no person
may cause or allow the transfer of gasoline from a
delivery vessel into
a stationary storage tank located
at a bulk gasoline plant unless:
1)
The delivery vessel and the stationary storage
tank are each equipped with a vapor collection
system that meets the requirements of subsection
(d) (4)
of this Section~j..
2)
Each vapor collection system
is operating-~-j
3)
The delivery vessel displays the appropriate
sticker pursuant to the requirements of Sections
-218.584
(b)
or
(d) of this Part~j~
4)
The pressure relief valve(s) on the stationary
storage tank and the delivery vessel are set to
release at no less than 0.7 psi or the highest
pressure allowed by state or local fire codes or
the guidelines of the National Fire Prevention
Association7~and
5)
The stationary storage tank is equipped with a
submerged loading pipe.
b)
Subject to subsection
(f)
of this Section, no person
may cause or allow the transfer of gasoline from a
stationary storage tank located at a bulk gasoline
plant into a delivery vessel unless:
1)
The requirements set forth in subsections
(a) (1)
through
(a) (4)
of this Section are met~~and
2)
Equipment
is available at the bulk gasoline plant
to provide for the submerged filling of the
delivery vessel or the delivery vessel
is equipped
for bottom loading.
c)
Subject to subsection
(e)
of this Section, each owner
of a stationary storage tank located at a bulk gasoline
plant shall:
1)
Equip each stationary storage tank with a vapor
control system that meets the requirements of

270
subsection
(a)
or
(b)
of this Section, whichever
is applicable~~
2)
Provide instructions to the operator of the bulk
gasoline plant describing necessary maintenance
operations and procedures for prompt notification
of the owner in case of any malfunction of a
vapor control systemT~and
3)
Repair, replace or modify any worn out or
malfunctioning component or element of design.
d)
Subject to subsection
(e)
of this Section, each
operator of a bulk gasoline plant shall:
1)
Maintain and operate each vapor control system in
accordance with the owner’s instructions7~
2)
Promptly notify the owner of any scheduled
maintenance or malfunction requiring replacement
or repair of a major component of a vapor control
system~~and
3)
Maintain gauges, meters or other specified testing
devices
in
proper working order7~
4)
Operate the bulk plant vapor collection system and
gasoline
loading equipment in a manner that
prevents:
A)
Gauge pressure from exceeding 45.7 cm
(18
in.)
of water and vacuum from exceeding 15.2
cm
(6
in.)
of water,
as measured as close as
possible to the vapor hose connectionT~and
B)
A reading equal to or greater than
100
percent of the lower explosive limit
(LEL
measured as propane) when tested in
accordance with the procedure described in
“Control of Volatile Organic Compound Leaks
from Gasoline Tank Trucks and Vapor
Collection Systems”, Appendix B,
EPA
450/2-78-051,
(incorporated by reference
in Section 218.112)
of this Part,-j and
C)
Avoidable leaks of liquid during loading or
unloading operations.
5)
Provide a pressure tap or equivalent on the bulk
plant vapor collection system in order to allow
the determination of compliance with subsection
(d) (4) (A)
of this Section-n and

271
6)
Within
15 business days after discovery of any
leak by the owner, the operator, the Agency or the
USEPA, repair and retest a vapor collection system
which exceeds the limits of subsection
(d) (4) (A)
or
(B)
of this Section.
e)
The requirements of subsections
(a),
(c) and
(d)
p1
this Section shall not apply to:
1)
Any stationary starage tank with a capacity of
less than 2,177
1
(575 gal),-j or
2)
Any bulk gasoline plant whose daily gasoline
throughput
is less than 15,140
1
(4,000 gal/day)
on a thirty-day rolling average.
f)
The requirements of subsection
(b)
of this Section
shall apply only to bulk gasoline plants whose daily
gasoline throughput is greater than or equal to 15,140
1
(4,000 gal/day)
on a thirty-day rolling average.
g)
Any bulk gasoline plant which is ever subject to
subsections
(a),
(b),
(c), or
(d)
shall always be
subject to these paragraphs.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.582
Bulk Gasoline Terminals
a)
No person shall cause or allow the transfer of gasoline
into any delivery vessel from any bulk gasoline
terminal unless:
1)
The bulk gasoline terminal is equipped with a
vapor control system that limits emission of
VON
to
80 mg/l
(0.00067
lbs/gal)
of gasoline loaded;
2)
The vapor control system
is operating and all
vapors displaced in the loading of gasoline to the
delivery vessel are vented only to the vapor
control system;
3)
There
is no liquid drainage from the loading
device when it is not in use;
4)
All
loading and vapor return lines are equipped
with fittings which are vapor tight;
and
5)
The delivery
vessel displays the appropriate
sticker pursuant to the requirements of Section
218.584(b) or
(d)
of this Part
or,
if the

272
terminal is driver—loaded, the terminal owner or
operator shall be deemed to be in compliance with
this Section when terminal access authorization is
limited to those owners and/or operators of
delivery vessels who have provided a current
certification as required by Section 218.584(c) (3)
of this Part.
-h)-
Bulk gasolinc tcrminal3 were required to take
UCLLUJ.fl
UL~L.LUI1~
sununari~cdin 35
LU
UULILCVC
Ill.
Adni.
compi.Lanoc
Code 215.
which arc
Appendix C.
ek)
The operator of
a bulk gasoline terminal shall:
1)
Operate the terminal vapor collection system and
gasoline loading equipment in a manner that
prevents:
A)
Gauge pressure from exceeding 18 inches of
water and vacuum from exceeding
6 inches of
water as measured as close as possible to the
vapor hose connection; and
B)
A reading equal to or greater than 100
-
percent
of
the lower explosive limit
(LEL
measured as propane) when tested in
accordance with the procedure described in
EPA 450/2-78-051 Appendix B~incorporated by
reference
in
Section
218.112
of
this
Part
and
C)
Avoidable leaks of liquid during loading or
unloading operations.
2)
Provide a pressure tap or equivalent on the
terminal vapor collection system in order to allow
the determination of compliance with Section
218.582(d) (1) (A)
of this Part
and
3)
Within 15 business days after discovery of the
leak by the owner,
operator,
or the Agency repair
and retest a vapor collection system which exceeds
the limits of subsection
(c) (1) (A)
or
(B)
of this
Section.
(Source:
Amended at
Ill. Reg.
______,
effective
)

273
-
-
Section 218.583
Gasoline Dispensing Facilities
-
Storage Tank
Filling Operations
a)
Subject to subsection
(b) below,
no person shall cause
or allow the transfer of gasoline from any delivery
vessel
into any stationary storage tank at a gasoline
dispensing facilityoperation unless:
1)
The tank is equipped with a submerged loading
pipe; and
2)
The vapors displaced from the storage tank during
filling are processed by a vapor control system
that includes one or more of the following:
A)
A vapor collection system that meets the
requirements of subsection
(d) (4)
below;
or
B)
A refrigeration—condensation system or any
other system approved by the Agency and
approved by the USEPA as a SIP revision, that
recovers at least 90 percent by weight of all
vaporized organic material from the equipment
being controlled; and
C)
The delivery vessel displays the appropriate
sticker pursuant to the requirements of
Section 218.584(-b)
or
(d)
of this Part.
b)
The requirements of subsection
(a) (2)
above shall not
apply to transfers of gasoline to a stationary storage
tank at a gasoline dispensing facilityoperation if:
1)
The tank is equipped with a floating roof, or
other system of equal or better emission control
approved by the Agency and approved by the USEPA
as a SIP revision;
2)
The tank has a capacity of less than 2000 gallons
and was in place and operating before January
1,
1979; or
3)
The tank has a capacity of less than 575 gallons.
c)
Subject to subsection
(b)
above, each owner of
a
gasoline dispensing facilityoperation shall:
1)
Install all control systems and make all process
modifications required by subsection
(a)
above;
2)
Provide instructions to the operator of the
gasoline dispensing facilityoperation describing

274
necessary maintenance operations and procedures
for prompt notification of the owner in case of
any malfunction of
a vapor control system; and
3)
Repair, replace or modify any worn out or
malfunctioning component or element of design.
d)
Subject to subsection
(b)
above, each operator of a
gasoline dispensing facilityoperation shall:
1)
Maintain and operate each vapor control system in
accordance with the owner’s instructions;
2)
Promptly notify the owner of any scheduled
maintenance or malfunction requiring replacement
or repair of a major component of a vapor control
system;
3)
Maintain gauges, meters or other specified testing
devices in proper working order;
4)
Operate the vapor collection system and delivery
vessel unloading points in a manner that prevents:
A)
A reading equal to or greater than 100
percent
of
the
lower
explosive
limit
(LEL
measured
as
propane)
when
tested
in
accordance
with
the
procedure described in
EPA 450/2-78-051 Appendix B, and
B)
Avoidable leaks of liquid during the filling
of storage tanks; and
5)
Within 15 business days after discovery of the
leak by the owner, operator, or the Agency, repair
and retest a vapor collection system which exceeds
the limits of subsection
(d) (4) (A)
above.
a)-
Gasoline dispensing facilities were required to take
certain actions
summarized
in 35
to achieve
Ill. Adm.
compliance which arc
Code 215, Appendix C.
(Source:
Amended at
Ill.
Reg.
______,
effective
3ection 218.584
Gasoline Delivery Vessels
a)
Any delivery vessel equipped for vapor control by use
of vapor collection equipment:
1)
Shall have a vapor space connection that is
equipped with fittings which are vapor tight;
)

275
2)
Shall have its hatches closed at all times during
loading or unloading operations,
unless a top
loading vapor recovery system is used;
3)
Shall not internally exceed a gauge pressure of 18
inches of water or a vacuum of
6 inches of water;
4)
Shall be designed a~dmaintained to be vapor tight
at all times during normal operations;
5)
Shall not be refilled in Illinois at other than:
A)
A bulk gasoline terminal that complies with
the
requirements
of Section 218.582 of this
Part
or
B)
A bulk gasoline plant that complies with the
requirements of Section 218.581(b)
of this
Part.
6)
Shall be tested annually in accordance with Method
27,
40 CFR 60, Appendix A, incorporated by
reference in Section 218.105.
Each vessel must be
repaired and retested within
15 business days
after
discovery
of
the
leak
by
the
owner,
operator,
or the Agency, when it fails to sustain:
A)
A
pressure drop of no more than three inches
of water in five minutes; and
B)
A vacuum drop of no more than three inches of
water in five minutes.
b)
Any delivery vessel meeting the requirements of
subsection
(a)
of this Section shall have a sticker
affixed to the tank adjacent to the tank manufacturer’s
data plate which contains the tester’s name,
the tank
identification number and the date of the test.
The
sticker shall be in a form prescribed by the Agency,
and,
for those delivery vessels subject to 35 Ill.
Adni.
Code 215 as of December 31,
1987 shall have been
displayed no later than December
31,
1987.
c)
The owner or operator of a delivery vessel shall:
1)
Maintain copies of any test required under
subsection
(a) (6)
of this Section for a period of
3 years;
2)
Provide copies of these tests to the Agency upon
request; and

276
3)
Provide annual test result certification to bulk
gasoline plants and terminals where the delivery
vessel is loaded.
d)
Any delivery vessel which has undergone and passed a
test in another state which has a USEPA-approved leak
testing and certification program will satisfy the
requirements of subsection
(a)
of this Section.
Delivery vessels must display a sticker, decal or
stencil approved by the state where tested or comply
with the requirements of subsection
(b)
of this
Section.
All such stickers, decals or stencils shall
have been displayed no later than December 31,
1987,
for delivery vessels subject to 35 Ill.
Adm. Code
215
as of December 31,
1987.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.585
Gasoline Volatility Standards
a)
No person shall sell, offer for sale,
dispense, supply,
offer for supply,
or transport for use in Illinois
gasoline whose Reid vapor pressure exceeds the
applicable limitations set forth in subsections
(b)
and
(c)
of this Section during the regulatory control
periods, which shall be July~y 1 to August 31
September 15 for retail outlets, wholesale
purchaser—consumer,
facilities operations,
and all
other facilities operations.
b)
The Reid vapor pressure of gasoline,
a measure of its
volatility,
shall not exceed 9.4Q psi
(65.5 62.07
kPa)
during the regulatory control period in 1990 and each
year thereafter.
c)
The Reid vapor pressure of ethanol blend gasolines
shall
not
exceed
the
limitations
for gasoline set forth
in
subsection
(b)
of this Section by more than 1.0 psi
(6.9 kPa).
Notwithstanding this limitation, blenders
of ethanol blend gasolines whose Reid vapor pressure is
less than 1.0 psi above the base stock gasoline
immediately after blending with ethanol are prohibited
from adding butane
or- any product that will increase
the Reid vapor pressure of the blended gasoline.
d)
All sampling of gasoline required pursuant to the
provisions of this Section shall be conducted by one or
more of the following approved methods or procedures
which are incorporated by reference in Section 215.105.
1)
For manual sampling, ASTN D4057;

277
2)
For automatic sampling, ASTM D4177;
3)
Sampling procedures for Fuel Volatility,
40 CFR 80
Appendix
D.
e)
The Reid vapor pressure of gasoline shall be measured
in
accordance
with
either
test
method
ASTM
D323
or
a
modification of ASTM D323 known as the “dry method” as
set forth in 40 CFR 80, Appendix E, incorporated by
reference in 35 Ill.
Adm. Code ~442~.4
of this
Part.
For gasoline
oxygenate
blends
which
contain
water—extractable
oxygenates,
the
Reid
vapor
pressure
shall be measured using the dry method test.
f)
The ethanol content of ethanol blend gasolines shall be
determined by use of one of the approved testing
methodologies specified in 40 CFR 80, Appendix F,
incorporated by reference in 35
Ill.
Adm.
Code
-24-~2~.
~
of this Part.
g)
Any alternate to the sampling or testing methods or
procedures contained in subsections
(d),
(e), and
(f)
of this Section must be approved b~the Agency, which
shall consider data comparing the performance of the
proposed alternative to the performance of one or more
approved test methods or procedures.
Such data shall
accompany any request for Agency approval of any
alternate
test procedure.
-
If the Agency determines
that such data demonstrates that the proposed
alternative will achieve results equivalent to the
approved test methods or procedures, the Agency shall
approve the proposed alternative.
h)
Each refiner or supplier that distributes gasoline or
ethanol blends shall:
1)
During the regulatory control period,
state that
the Reid vapor pressure of all gasoline or ethanol
blends leaving the refinery or distribution
facility operation for use in Illinois complies
with the Reid vapor pressure limitations set forth
in
35 Ill.
Adm. Code
-~j~.585(b)and
(c).
Any
facilityoperation receiving this gasoline shall be
provided with a copy of an invoice, bill of
lading, or other documentation used in normal
business practice stating that the Reid vapor
pressure of the gasoline complies with the State
Reid vapor pressure standard.
2)
Maintain records for a period of one year on the
Reid vapor pressure, quantity shipped and date of
delivery of any gasoline or ethanol blends leaving

278
the refinery or distribution facility operation
for use in Illinois.
The Agency shall be provided
with copies of such records if requested.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________)
Section 218.586
Gasoline Dispensing Facilities Operations
-
Motor
Vehicle
Fueling
Operations
a)
For the purposes of this Section, the following
definitions apply.
1)
Average Mzi~onth1y~,Ryolume÷means tThe amount of
motor vehicle fuel dispensed per month from a
gasoline dispensing facility operation based upon
a monthly average for the 2—year period of
November,
1990 through October,
1992 or,
if not
available, the monthly average for the most recent
twelve calendar months.
Monthly averages are to
include only those months when the facility
operation was operating.
-
2)
Certified÷means aAny vapor collection and control
system
which
has
been
tested
and
approved
by
CARB
as having
a vapor recovery and removal efficiency
of at least 95
(by weight)
shall constitute a
certified vapor collection and control system.
CARB testing and approval is pursuant to the CARB
manual,
hereby
incorporated
by
reference
~
218.112 of this Part ~California Air Resources
Board,
Compliance Division, Compliance Assistance
Program:
1~aciliticsPhase
I ~ II
(October 1988,
rev. March 1991
CARS
Manual)).
This incorporation
includes no later additions or amendments.
3)
Completion of installation+ means t~1hesuccessful
passing of one or more of the following tests
applicable to the installed vapor collection and
control system:
Dynamic Backpressure Test,
Pressure Decay/Leak Test,
and Liquid Blockage
Test~(United States Environmental Protection
Agency, Washington D.C.,
EPA-450-3-91-002b).
These tests arc hereby incorporated by reference
at 218.112 of this Part.
This incorporation
includes no later additions or amendments.
4)
Constructed+ means f~abricated,erected or
installed; refers to any facility, emission source
or air pollution control equipment.

279
5)
CARB÷means California Air Resources Board, P.O.
Box 2815,
Sacramento, CA 95812.
6)
Employee÷means aAny person who performs work for
an employer.
7)
FacilityOperation÷means aAny building, structure,
installation, operation or combination thereof
located on contiguous properties and under common
ownership that provides for the dispensing of
motor vehicle fuel.
8)
Gasoline ~ispensing
Facility operation÷ means
~Any facilityoperation where motor vehicle fuel is
dispensed into motor vehicle fuel tanks or
portable containers from a storage tank with a
capacity of 2176 liters
(575 gallons)
or more.
9)
Modification÷means aAny change, removal or
addition,
other than an identical replacement,
of
any component contained within the vapor
collection and control system.
10)
Motor Vyehicle÷means aAny self-propelled vehicle
powered by an internal combustion engine
including, but not limited to, automobiles and
trucks.
Specifically excluded from this
definition are watercraft and aircraft.
11)
Motor
‘~ehicle~uel+
means aAny petroleum
distillate having a Reid vapor pressure of more
than 27.6 kilopascals
(kPa)
(four pounds per
square inch)
and which is used to power motor
vehicles.
12)
Owner or 99perator÷means aAny person who owns,
leases,
operates, manages, supervises or controls
(directly or indirectly)
a gasoline dispensing
facilityoperation.
13)
Reid ~yapor Ppressure÷f-for gasoline, 4~shall be
measured in accordance with either the method ASTM
D323 or a modification of ASTM D323 known as the
“dry method” as set forth in 40 CFR 80, Appendix
E, incorporated by references
in 35
Ill. Adm. Code
215.105218.112 of this Part.
14)
Vapor ~ollection
and Gcontrol ~ystem÷
means aAny
system certified
by CARB
which limits the
discharge to the atmosphere of motor vehicle fuel
vapors displaced during the dispensing of motor
vehicle fuel into motor vehicle fuel tanks.

-
280
b)
The provisions of subsection
(c)
below shall apply to
any gasoline dispensing facility operation which
dispenses an average monthly volume of more than 10,000
gallons of motor vehicle fuel per month. Compliance
shall be demonstrated in accordance with the schedule
provided in subsection
(d)
below.
c)
No owner or operator of a gasoline dispensing facil-ity
operation subject to the requirements of subsection
(b)
above shall cause or allow the dispensing of motor
vehicle fuel at any time from a motor fuel dispenser
unless the dispenser is equipped with and utilizes a
vapor collection and control system which is properly
installed and operated as provided below:
1)
Any vapor collection and control system installed,
used or maintained has been
CARB
certified.
2)
Any vapor collection and control system utilized
is maintained in accordance with the
manufacturer’s specifications and the
certification.
3)
No elements or components of a vapor collection
and control system are modified,
removed, replaced
or otherwise rendered inoperative in a manner
which prevents the system from performing in
accordance
with
its
certification
and
design
specifications.
4)
A vapor collection and control system has no
defective, malfunctioning or missing components.
5)
Operators and employees of the gasoline dispensing
facility operation are trained and instructed in
the proper operation and maintenance of a vapor
collection and control system.
6)
Instructions are posted in a conspicuous and
visible place within the motor fuel dispensing
area and describe the proper method of dispensing
motor vehicle fuel with the use of the vapor
collection and control system.
d)
In conjunction with the compliance provisions of
Section 218.105 of this Part,
facilitiesoperations
subject to the requirements of subsection
(c)
above
shall demonstrate compliance according to the
fl—li
•~
(1t.T1
~~•~l-f

281
-
1)
FaciliticsOperations that commenced construction
after November
1,
1990, must comply by May 1,
1993.
-
2)
FaciliticsOperations
that
commenced
construction
before November
1,
1990,
and dispense an average
monthly volume of more than 100,000 gallons of
motor fuel per month must comply by November 1,
1993.
3)
FaciliticsOperations that commenced construction
before November
1,
1990,
and dispense an average
monthly volume of less than 100,000 gallons of
motor fuel per month must comply by November 1,
1994.
4)
New facilitiesoperations constructed after the
adoption of this Section shall comply with the
requirements of subsection
(c)
above upon startup
of the facilityoperation.
5)
Existing facilitiesoperations previously exempted
from but which become subject to the requirements
of subsection
(c)
above after Nay 1,
1993 shall
comply
with
the
requirements
of
subsection
(c)
above within six calendar months of the date from
-
which the facilityoperation becomes subject.
e)
Any gasoline dispensing facility operation that becomes
subject to the provisions of subsection
(c)
above at
any time shall remain subject to the provisions of
subsection
(c)
above at all times.
f)
Upon request by the Agency, the owner or operator of a
gasoline dispensing facilityoperation which claims to
be exempt from the requirements of this Section shall
submit records to the Agency within 30 calendar days
from the date of the request which demonstrate that thE
gasoline dispensing facilityoperation is in fact
exempt.
g)
Recordkeeping and reporting:
1)
Any gasoline dispensing facilityoperation subject
to subsection
(c)
above shall retain at the
facility operation copies of the registration
information required at subsection
(h)
below.
2)
Records and reports required pursuant to this
subsection shall be made available to the Agency
upon request.
Records apd reports which shall be
maintained by the owner or operator of the

282
gasoline dispensing facilityoperation shall
clearly demonstrate:
A)
That a certified vapor collection and control
system has been installed and tested to
verify its performance according to its
specifications.
B)
That proper maintenance has been conducted in
accordance with the manufacturer’s
specifications
and
requirements.
C)
The time period and duration of all
malfunctions of-the vapor collection and
control system.
D)
The motor vehicle fuel throughput of the
facilityoperation for each calendar month of
the previous year.
E)
That operators and employees are trained and
instructed in the proper operation and
maintenance of the vapor collection and
control system and informed as to the
potential penalties associated with the
violation of any provision of this Section.
h)
Any gasoline dispensing facilityoperation subject to
subsection
(c)
above
shall
be
exempt
from
the
permit
requirements specified under 35 Ill.
Adm. Code 201.142,
201.143 and 201.144 for its vapor collection and
control systems, provided that:
1)
Upon the installation of a vapor collection and
control system, the owner or operator of the
gasoline dispensing facilityoperation submits to
the Agency a registration which provides at
minimum the facility operation name and address,
signature of the owner or operator,
the CARB
Executive Order Number for the vapor collection
and control system to be utilized, the number of
nozzles
(excluding diesel or kerosene) used for
motor vehicle refueling,
the monthly average
volume of motor vehicle fuel dispensed, the
location (including contact person’s name,
address, and telephone number)
of records and
reports required by this Section, and the date of
completion of installation of the vapor collection
and control system.
2)
The registration
is submitted to the Agency within
30 days of completion
of’ such installation.

283
3)
A copy of the registration information is
maintained at the gasoline dispensing facility
operation.
4)
Upon the modification of an existing vapor
collection and control system, the owner or
operator of the gasoline dispensing facility
operation submits to the Agency a registration
that details the changes to the information
provided in the previous registration of the vapor
collection and control system and which includes
-
the signature of the owner or operator. The
registration must be submitted to the Agency
within 30 days of completion of such modification.
(Source:
Amended at
______
Ill. Reg.
________,
effective_______
SUBPART
Z:
DRY CLEANERS
Section
218.601
Perchloroethylene Dry Cleaners
The owner or operator of a dry cleaning faoilityoperation which
uses perchloroethylene shall:
a)
Vent the entire dryer exhaust through a properly
designed
and
functioning
carbon
adsorption
system
or
equally
effective
control
device;
and
b)
Emit no more than 100 ppmv of VOM from the dryer
control
device
before
dilution,
or
achieve
a
90
percent
average reduction before dilution; and
c)
Immediately repair all components found to be leaking
liquid VON; and
d)
Cook or treat all diatomaceous earth filters so that
the residue contains
25 kg
(55
lb)
or less of VON per
100 kg
(220
lb)
of wet waste material; and
e)
Reduce the VON from all solvent stills to 60 kg (132
lb)
or less per 100 kg
(220
lb)
of wet waste material;
and
f)
Drain all filtration cartridges in the filter housing
or other sealed container for at least 24 hours before
discarding the cartridges;
and
g)
Dry all drained filtration cartridges in equipment
connected to an emission reduction system or in a
manner that will eliminate emission of VON to the
atmosphere.

(Source:
Amended at
_________________________ )
Section 218.602
284
Ill.
Reg.
______,
effective
Exemptiens
The provisions of Section 218.601 of this Part are not applicable
to perchloroethylene dry cleaning operations which are
coin—operated or to dry cleaning facilitiesoperations consuming
less than 30 gal per month
(360 gal per year)
of
perchloroethylene.
-
(Source:
Amended at
Ill. Reg.
______,
effective
)
Section
218.603
Leaks
The presence of leaks shall be determined for purposes of Section
218.601(c)
of this Part by a visual inspection of the following:
hose connections, unions, couplings and valves; machine door
gaskets and seatings; filter head gasket and seating; pumps; base
tanks and storage containers; water separators;
filter sludge
recovery; distillation unit;
diverter valves; saturated lint from
lint baskets; and cartridge filters.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.604
Compliance Dates
(Reoealed)
~,-et
fL~. in 35 Ill.
Adm. Code 215.60-.
(Source:
Repealed at
Ill.
Reg.
______,
effective
Section
218.605
Compliance Plan
(Repealed)
a-)-
..‘-.
.
compliance plan, pursuant to 35 Ill.
Adm. Code
201,
Subpart H,
including a project completion schedule
where
applicable,
no
later
than,
for
Section
2l8.60l(a-)-
and
(b), April 21,
1983.
Unless
the submitted compliance plan or schedule was
disapproved by the Agency, the owner or operator of—a
facility or emission source may operate the omission
source according to the plan and schedule as submitte4--
Every owner or operator of an emission source previously subject
to 35 Ill.
Adni. Code 215, Subpart
Z,
shall have complied with its
standards and limitations in accordance with the
applicable
dates

285
e-)-
The plan and schedule shall meet the requirements of 35
Ill. Mm.
Code 201, Subpart H,
including specific
in-ccrun sates
as required in
35
Ill. Adm.
Coae
~
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
Section 218.606
Exception to Compliance Plan (Repealed)
Coin
operated
dry
cleaning
operations
and
dry
cleaning
facilities
consuming
loss
than
30
gal
per
menth
(360
gal
per
year)
of
pcrohlorocthylene
are
not
required
to
submit
or
obtain
an
Agency
~nr~rovcdcompliance plan or project completion schedule.
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________
Section 218.608
Operating Practices for Petroleum Solvent Dry
Cleaners
In order to minimize fugitive solvent emissions,
the owner or
operator of a petroleum solvent dry cleaning facilitysource shall
employ good housekeeping practices including the following:
a)
General Housekeeping Requirements
1)
Equipment containing solvent
(washers, dryers,
extractors and filters) shall remain closed at all
times except during load transfer and maintenance.
Lint filter and button trap covers shall remain
closed
except
when
solvent—laden
material
is
being
removed.
2)
Cans,
buckets, barrels and other containers of
solvent or of solvent—laden material shall
be
covered except when in use.
3)
Solvent-laden material shall be exposed to the
atmosphere only for the minimum time necessary for
load transfer.
b)
Installation and operation of equipment:
1)
All
cartridge filters shall be enclosed and
operated in accordance with the procedures and
specifications recommended by the manufacturer for
the cartridge filter.
After installation, the
cartridges shall be inspected, monitored and
maintained in accordance with the manufacturer’s
recommendations; and

286
2)
Vents on containers for new solvent and for
solvent—containing waste shall be constructed and
maintained so as to minimize solvent vapor
emissions.
Criteria for the minimization of
solvent vapor emissions include the elimination of
solvent buckets and barrels standing open to the
atmosphere, and the repair of gaskets and seals
that expose solvent—rich environments to the
atmosphere, to be determined through visual
inspection.
(Source:
Amended
at
Ill. Reg.
______,
effective
____________
Section
218.609
Program
for
Inspection
and
Repair
of
Leaks
a)
The owner or operator of
a petroleum solvent dry
cleaning facilitysource shall conduct the following
visual inspections on a weekly basis:
1)
Washers,
dryers,
solvent filters, settling tanks,
vacuum stills and containers and conveyors of
petroleum
solvent
shall
be
inspected
for
visible
-
leaks
of
solvent
liquid.
-
2)
Pipes,
hoses
and
fittings
shall
be
inspected
for
active dripping or dampness.
3)
Pumps and filters shall be inspected for leaks
around
seals
and
access
covers.
4)
Gaskets and seals shall be inspected for wear and
defects.
b)
Leaks
of petroleum solvent liquid and vapors shall be
repaired within three working days of detection, unless
necessary replacement parts are not on site.
1)
If necessary,
repair parts shall be ordered within
three working days of detection of the leak.
2)
The leak shall be repaired within three days of
delivery of necessary parts.
(Source:
Amended at
Ill. Reg.
,
effective
____________
Section 218.610
Testing and Monitoring
a)
Compliance with Sections 218.607(b) (2), 218.608 and
218.609
of
this
Part shall be.deterTnined by visual
inspection; and

287
b)
Compliance with Sections 218.607 (a) (2)
and
(b) (1)
p1
this Part shall be determined by methods described in
EPA-450/3-82-009
(1982)
incorporated by reference in
Section 218.112 of this Part.
c)
If a control device is used to comply with Section
218.607(a)
(1)
of
this
Part,
then
compliance
shall
be
determined
using
40
CFR
60
Appendix
A,
Method
25
(1984)
incorporated by reference in Section 218.112 of this
Part.
(Source:
Amended
at
Ill. Reg.
______,
effective
____________
Section 218.611
Exemption for Petroleum Solvent Dry Cleaners
The provisions of Sections 218.607 through 218.610 of this Part
shall not apply to petroleum solvent dry cleaning facilities
sources whose emissions of VON do not exceed 91 megagrams
(100
tons)
per year in the absence of pollution control equipment or
whose emissions of VON,
as limited by the operating permit, will
not
exceed
91 megagrams
(100 tons) per year in the absence of
pollution control equipment.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 218.612
Compliance Dates
(Repealed)
~owners
ana
nnr~r~torsoi
emission
sources
subject
to
35
Iii.
Acini.
Code
215.607
through
215.609
as
of
December
31,
1987
shall
have
complied with the requirements set forth therein no later than
December
31,
1987.
(Source:
Repealed at
Ill. Reg.
______,
effective
___________
Section
218.613
Compliance Plan (Repealed)
a-)-
The owner or operator of an emission source subject to
35 Ill.
Adni.
Code 215.610(a)
as of May 31,
1987 shall
èave submitted to the Agency a compliance plan,
including a project completion schedule where
applicable,
no later than Hay
31,
1987.
~-
The plan and schedule shall meet the requirements
of
35
Ill. Adm. Code 201.
(Source:
Repealed at
Ill.
Reg.
______,
effective
___________

288
SUBPART AA:
PAINT AND INK MANUFACTURING
Section 218.620
Applicability
a)
This ~subpart shall apply to all paint and ink
manufacturing plantssources which:
1)
Include process emission sourcesunits not subject
to Subparts B,
E,
F (excluding Section 218.204(1)
of this Part), H (excluding Section 218.405
p1
this Part),
Q,
R,
5,
T
(excluding Section 218.486
of this Part),
V,
X,
1,
Z or BB of this Part; and
which as a group both:
A)
jj~avemaximum theoretical emissions of 91 Mg
(100 tons)
or more per calendar year of VON
if no air pollution control equipment were
used,
and
B)
Aare not limited to less than 91 Mg
(100
tons)
of VOM emissions per calendar year in
the absence of air pollution control
equipment, through production or capacity
limitations contained in a federally
enforceable
construction
permit
or
a
SIP
revision,
or
2)
Produce more than 7,570,820
1
(2,000,000 gal) per
calendar year of paint or ink formulations, which
contain less than 10 percent
(by weight)
water,
and ink formulations not containing as the primary
solvents water, Magie oil or glycol.
b)
For the purposes of this Subpart, uncontrolled VOM
emissions are the emissions of VON which would result
if no air pollution control equipment were used.
(Source:
Amended at
Ill. Peg.
______,
effective
___________
Section 218.621
Exemption for Waterbase Material and
Heatset-Offset Ink
The requirements of Sections 218.624 and 218.625 and Section
218.628(a) of this Part shall not apply to equipment while
it is
being used to produce either:
a)
ppaint or ink formulations which contain 10 percent or
more
(by weight) water, or
b)
4~nkscontaining Magie oil an~glycol as the primary
solvent.

289
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
_________________________)
Section 218.623
Permit Conditions
No
person
shall
violate
any
condition
in
a
permit
when
the
condition
results
in
exclusion
of
the
plantsource
or
an
emission
sourceunit from this Subpart.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________ )
Section 218.624
Open-#Iop Mills,
Tanks, Vats or Vessels
No person shall operate an open—top mill,
tank, vat or vessel
with a volume of more than 45
1
(12 gal)
for the production of
paint or ink unless:
a)
The mill,
tank, vat or vessel
is equipped with a cover
which completely covers the mill,
tank, vat or vessel
opening except for an opening no larger than necessary
to
allow
for
safe
clearance
for
a
mixer
shaft.
Such
cover shall extend at least 1.27 cm (0.5
in) beyond the
outer
rim
of
the
opening
or
be
attached
to
the
rim.
b)
The cover remains closed except when production,
sampling, maintenance or inspection procedures require
access.
c)
The cover
is maintained in good condition such that,
when in place,
it maintains contact with the rim of the
opening for at least 90 percent of the circumference of
the rim.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.628
Leaks
The owner or operator of
a paint or ink manufacturing plantsource
shall, for the purpose of detecting leaks, conduct an equipment
monitoring program as set forth below:
a)
Each pump shall be checked by visual inspection each
calendar week for indications of leaks, that is,
liquids dripping from the pump seal.
If there are
indications of liquids dripping from the pump seal, the
pump shall be repaired as soon as practicable, but no
later than 15 calendar days after the leak
is detected.
b)
Any pump,
valve, pressure relief valve,
sampling
connection,
open—ended valve and flange or connector

290
containing
a fluid which is at least 10 percent VON by
weight which appears to be leaking on the basis of
sight,
smell or sound shall be repaired as soon as
practicable, but no later than 15 calendar days after
the leak is detected.
c)
A weather proof, readily visible tag,
in bright colors
such as red or yellow,
bearing an identification number
and the date on which the leak was detected shall
be
attached to leaking equipment.
The tag may be removed
upon
repair,
that
is,
when
the
equipment
is
adjusted
or
otherwise altered to allow operation without leaking.
d)
When a leak is detected, the owner or operator shall
record the date of detection and repair and the record
shall be retained at the plantsource for at least two
years from the date of each detection or each repair
attempt.
The record shall be made available to any
person upon verbal or written request during business
hours.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.636
-
Compliance
Schedule
Every owner or operator of ~ an emission source subject to the
control requirements of this Subpart shall comply with the
requirements thereof on and after a date consistent with Section
218.106 of this Part.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.637
Recordkeeping and Reporting
a)
Upon request by the Agency, the owner or operator of an
emission source which claims to be exempt from the
requirements of this Subpart shall submit records to
the Agency within 30 calendar days from the date of the
request which document that the emission source
is in
fact exempt from this Subpart.
These records shall
include (but are not limited to) the percent water
(by
weight)
in the paint or ink being produced and the
quantity of Magie oil, glycol and other solvents in the
ink being produced.
b)
Every owner or operator of a~emission source which is
subject to the requirements of this Subpart shall
maintain all records necessary to demonstrate
compliance with those requirements at the facility
source for three years.

291
-
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
SUBPART BB:
POLYSTYRENE
PLANTS
Section 218.875218.6.4.Q
Applicability of Cu~~art
The provisions of this Subpart shall apply to polystyrene plants:
a)
Which use continuous processes to manufacture
polystyrene
polybutadiene co—polymer; and
b)
Which fall within Standard Industrial Classification
Group No.
282, Industry No.
2821, except that the
manufacture of polystyrene resins need not be the
primary manufacturing process at the plant.
(Source:
Renumbered from Section 218.875 and amended at
____
Ill.
Peg.
_____
,
effective _______________________
Section 218.877218.642
Emissions Limitation at Polystyrene
Plants
No person shall cause or allow the emissions of VON from the
material recovery section to exceed 0.12 kg of Volatile Organic
Material per 1000 kg of polystyrene resin produced.
(Source:
Renumbered from Section 218.877 at
Ill.
Reg.
_____
effective
___________________________)
Section 218.886218.644
Emissions Testing
a)
Upon a reasonable request by the Agency, the owner
or
operator of a polystyrene plant subject to this Subpart
shall
at his own expense demonstrate compliance by use
of the following method:
40 CFR 60, Appendix A, Method
25
Determination of Total Gaseous Non—Methane Organic
Emissions as Carbon
(1984),
incorporated by reference
in Section
218.112
of this Part.
b)
A person planning to conduct a VON emissions test to
demonstrate compliance with this Subpart shall notify
the Agency of that intent not less than 30 days before
the planned initiation of the tests so the Agency may
observe the test.
(Source:
Renumbered from Section 218.886 and amended at
____
Ill.
Peg.
_____,
effective
_______________________)
Section 218.875
Applicability of Subpart BB (Renumbered)

292
(Source:
Renumbered to Section 218.640 at
____
Ill. Peg.
effective
______________)
Section 218.877
Emissions Limitation at Polystyrene Plants
(Renumbered)
(Source:
Renumbered to Section 218.642 at
____
Ill.
Reg.
effective
_______________________)
Section 218.879
Compliance Date (RePealed)
Every owner and operator of an emission source subject to 35
Il1--
Mm.
Code
215, Subpart BB,
as of December 31,
1937,
shall have
complied with its standards ~nd limitations by December 31,
1987.
(Source:
Repealed at
Ill.
Reg.
______,
effective
____________
Section 218.881
Compliance Plan
(Repealed)
a-)-
The
owner
or
operator
of
an
emission
source
formerly
subject
to
the
requirements
of
35
Ill.
Adm.
Code
215
Subpart
BE shall have submitted to the Agency a
compliance
plan
in
accordance
with
35
Ill.
Adm.
Code
-
201,
Subpart H,
including a project completion schedule
on
or
before
December
1,
1~187.
b-)-
Unless
the
submitted
compliance
plan
or
~chodu1c
was
disapproved
by
the
Agency,
the
owner
or
operator
of
a
facility or emission source subject to this Subpart may
operate the emIssion source according to the plan and
schedule
as
submitted.
e.)-
The
plan
and
schedule
shall
meet
the
requirements
of
35
Ill. Mm.
Code 201, Subpart H and Section 218.383.
(Source:
Repealed at
Ill.
Reg.
______,
effective
____________
Section 218.883
Special Requirements for Compliance Plan
kR~pealed)
F-or
sources
subject
to
this
Subpart,
an
approvable
compliance
p-lan shall include:
a-)-
A description of each process which
is subject to -a~
emissions limitation
-h-)-
Quantification of the emissions from each process
-
a)-
A description of
the-
procedures and methods
us-ed to
determine the emissions of
VON--

293
4+
A
description
of
the
methods
which
will
be
used
to
demonstrate compliance with the allowable plantwide
emission
limitation
(Section
215.877),
including
a
~-ethodof inventory,
rccordkecping and emission
.lculati-
(Source:
Repealed at
Ill.
Reg.
______,
effective
______________________
)
Section 218.886
Emissions Testing (Renumbered)
(Source:
Renumbered to Section 218.644 at
____
Ill. Peg.
effective
______________________________)
SUBPART PP:
MISCELLANEOUS FABRICATED PRODUCT
MANUFACTURING
PROCESSES
Section 218.920
Applicability
a)
The requirements of this Subpart shall apply to a
plant’s-source’s miscellaneous fabricated product
manufacturing process emission sourccsunits which are
not included within any of the source categories
specified
in
Subparts
B,
E,
F,
H,
Q,
R,
S,
~
V.,
X,
Y~.
e~Z or BB if the plantsource is subject to this
Subpart.
A plantsource is subject to this Subpart if
it contains process emission sources-units, -not
-
-
regulated by Subparts
B,
E, F (excluding Section
218.204(1)
of this Part),
H (excluding Section 218.405
of this Part),
Q,
R,
5,
T
(excluding Section 218.486 of
this Part). V,
X, Y~e~Z or BB of this Part; which as
a
group
both:
1)
fi~avemaximum theoretical emissions of 91 Mg
(100
tons) or more per calendar year of VON if no air
pollution control equipment were used,
and
2)
Aare not limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment, through
production or capacity limitations contained in a
federally enforceable construction permit or a SIP
revision.
b)
If
a plantsource ceases to fulfill the criteria of
subsection
(a)
above,
the requir-ements of this Subpart
shall continue to apply to a miscellaneous fabricated
products manufacturing process emission s-ourccunit
which was ever subject to the control requirements of
Section 218.926 of this Part.

294
c)
No limits under this Subpart shall apply to emission
sources-units with emissions of VON to the atmosphere
less than or equal to 0.91 Mg (1.0 ton) per calendar
year if the total emissions from such sources emission
units not complying with Section 218.926 does not
exceed
4.5
Mg
(5.0 tons) per calendar year of this
Part.
d)
For the purposes of this Subpart, an emission
gourceunit shall be considered regulated by a Subpart
if it is subject to the limits of that Subpart.
An
emission courceunit is not considered regulated by a
Subpart
if
it
is
not
sublect
to
the limits of that
Subpart,
e.g., the emission unit is covered by an
exemption in the Subpart or the applicability criteria
of the Subpart are not met.
its emissions arc below
the applicability cutoff level or
if
the
source
is
covered
by
an
c~cmption.
e)
For the purposes of this Subpart, uncontrolled VON
emissions are the emissions of VON which would result
if no air pollution control equipment were used.
fl
The control requirements in Subpart PP shall not apply
to sewage treatment plants; veatable oil extraction and
processing: coke ovens
(including by—product recovery
plants):
fuel combustion units; bakeries: barge loading
facilities;
iet engine test cells; production of
polystyrene foam insulation board including storage and
extrusion of scrap where blowing agent
is added to the
polystyrene resin at the source, but not including
blending and preliminary expansion of resin prior to
molding where blowing agent is incorporated into the
polystyrene resin by the producer of the resin;
production of polystyrene foam packaging not including
blending and preliminary expansion of resin trior to
molding where blowing agent is incorporated into the
polystyrene resin by the producer of the resin and not
including storage and extrusion of scrap where blowing
agent is added to the polystyrene resin at the source;
and iron and steel production.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
_________________________
)
Section 218.923
Permit Conditions
No person shall violate any condition in a permit when the
condition results in exclusion of the p-1-antsource or an emission
s-ourceunit from this Subpart~

295
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________ )
Section 218.926
Control Requirements
Every owner or operator of an emission sourccmiscellaneous
fabricated product manufacturing process emission unit subject to
this Subpart shall comply with the requirements of subsection
(a),
(b)
or
(c)
of this Section:
a)
Emission capture and control techniques which achieve
an
overall
reduction
in
uncontrolled
VON
emissions
of
at
least
81
percent
from
each
emission
unit,
or
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at a source of a
-type
that by itself is subject to control requirements
in other Subparts of this Part or 40 CFR 60,
incorporated by reference in Section 218.112,
e.g.,
a
coating line,
a printing line,
a process unit,
a
wastewater system,
or other equipment,
or is otherwise
any part or activity at a source.)
b)
For coating lines,
the daily-weighted average VON
content shall not exceed 0.42 kg VOM/l
(3.5
lbs
VON/gal)
of coating as applied
(minus water and any
compounds which are specifically exempted from the
definition of VOM) during any day.
Owners and
operators complying with this Section are not required
to comply with Section 218.301 of this Part,
or
c)
An alternative control plan which has been approved by
the Agency and approved by the USEPA in federally
enforceable permit or as a SIP revision.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 218.927
Compliance Schedule
Every owner or operator of an emission sourceunit subject to the
control requirements of this Subpart shall comply with the
requirements thereof on and after a date consistent with Section
218.106
of this Part.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.928
Testing
a)
When in the opinion of the Agency it is necessary to
conduct testing to demonstrate compliance with Section

296
281.926,
the
owner
or operator of a VON emission
sourccunit subject to the requirements of this Subpart
shall,
at his own expense, conduct
such
tests
in
accordance with the applicable test methods and
procedures specified in Section 218.105.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act,
as amended, to
require testing.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
SUBPART QQ:
MISCELLANEOUS
FORMULATION
MANUFACTURING
PROCESSES
Section 218.940
Applicability
a)
The requirements of this Subpart shall apply to a
plant’s-source’s miscellaneous formulation manufacturing
process emission sources-units, which are not included
within any of the source categories specified in
Subparts
B,
E,
F,
H,
Q,
R,
S, ~
V,
X, Y~e~Z or BB of
this Part if the plantsource is subject to this
Subpart..
A plctntsource
is subject to this Subpart if
it contains process emission s~ourocsunits,not
regulated by Subparts
B,
E, F (excluding Section
218.204(1)
of this Part), H (excluding Section 218.405
of this Part),
Q,
P,
5, T
(excluding Section 218.486 of
this Part),
V,
X,
1, e-~Z or BE of this Part; which as
a group both:
1)
E1~avemaximum theoretical emissions of 91 Mg (100
tons)
or more per calendar year of VOM if no air
pollution control equipment were used,
and
2)
Aare not limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment,
through
production or capacity limitations contained in a
federally enforceable construction permit or a SIP
revision.
b)
If a plantsource ceases to fulfill the criteria
of
subsection
(a)
of this Section, the requirements of
this Subpart shall continue to apply to a miscellaneous
formulation manufacturing process emission sourccunit
which was ever subject to the control requirements of
Section 218.946 of this Part.
c)
No limits under this Subpart shall apply to emission
sources-units with emissions
o’f
VOM
to the atmosphere

297
less than or equal to 2.3 Mg
(2.5 tons) per calendar
year if the total emissions from such emission units
sources not complying with this Section does not exceed
4.5 Mg
(5.0
tons) per calendar year.
d)
For the purposes of this Subpart, an emission
courceunit shall be considered regulated by a Subpart
if it is subject to the limits of that Subpart.
An
emission sourceunit is not considered regulated by a
Subpart
if it is not subject to the limits of that
Subpart,
e.g., the emission unit is covered by an
exemption in the Subpart or the applicability criteria
of the Subpart are not met.
its emissions arc below the
applicability
cutoff
level
or
if
the
source
is
covered
by
an
exemption.
e)
For the purposes of this Subpart, uncontrolled VOM
emissions are the emissions of VOM which would result
if no air pollution control equipment were used.
~j
The control requirements
in Subpart 00 shall not apply
to sewage treatment plants; veaetable oil extraction
and processing; coke ovens
(including by—product
recovery plants): fuel combustion units: bakeries;
barge
loading
facilities:
jet
engine
test
cells;
production of polystyrene foam insulation board
-
including storage and extrusion of scrap where blowing
agent
is added to the polystyrene resin at the source,
but not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin: production of polystyrene foam packaging
not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin and not including storage and extrusion of
scrap where blowing agent is added to the polystyrene
resin at the source; and iron and steel production.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.943
Permit Conditions
No person shall violate any condition in a permit when the
condition results in exclusion of the plantsource or an emission
sourceunit from this Subpart.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
_____
)
Section 218.946
Control Requirements

298
Every
owner
or
operator
of
a~miscellaneous formulation
manufacturing process emission s-ourccunit subject to this Subpart
shall comply with the requirements of subsection
(a)
or
(b)
below.
a)
Emission capture and control techniques which achieve
an overall reduction in uncontrolled VON emissions of
at least 81 percent from each emission unit, or
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at a source of
a
type- that by itself is sublect to control requirements
in other Subparts of this Part or 40 CFR 60,
incorporated by reference in Section 218.112, e.g.,
a
coating line,
a printing line,
a process unit,
a
wastewater system, or other equipment,
or is otherwise
anY part or activity at a source.)
b)
An alternative control plan which has been approved by
the Agency and approved by the USEPA in
a federally
enforceable permit or as a SIP revision.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.947
Compliance Schedule
Every owner or operator of an emission sourceunit subject to the
control requirements of this Subpart shall comply with the
requirements thereof on and after
a
date consistent with Section
218.106
of this Part.
(Source:
Amended at
*
Ill.
Peg.
______,
effective
____________
Section 218.948
Testing
a)
When in the opinion of the Agency it is necessary to
conduct testing to demonstrate compliance with Section
218.946 of this Part, the owner or operator of a VOM
emission sourceunit subject to the requirements of this
Subpart shall, at his own expense,
conduct such tests
in accordance-with the applicable test methods and
procedures specified in Section 218.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act,
as amended, to
require testing.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________

299
SUBPART
PR:
MISCELLANEOUS
ORGANIC
CHEMICAL
MANUFACTURING
PROCESSES
Section 218.960
Applicability
a)
The requirements of this Subpart shall apply to a
p-lant’ssource’s miscellaneous organic chemical
manufacturing process emission sources-units which are
not included within any of the source categories
specified in Subparts B,
E,
F,
H,
Q,
R,
S, ~
V1
X, Y~
Z or BB of this Part,
if the plantsource
is subject to
this Subpart.
A plantsource
is subject to this Subpart
if
it contains process emission sources-units, not
regulated by Subparts B,
E,
F (excluding Section
218.204(1)
of this Part), H (excluding Section 218.405
of this Part),
Q,
P,
5, T (excluding Section 218.486 of
this Part),
V,
X, Y~
e~
Z
or BE of this Part; which as
a group both:
1)
ll~avemaximum theoretical emissions of 91 Mg
(100
tons)
or more per calendar year of VON
if no air
pollution control equipment were used,
and
2)
tare not limited to less than 91 Mg 100
tons)
of
VON -emissions per calendar year in the absence of
air pollution control equipment, through
production or capacity limitations contained in a
federally enforceable construction permit or a SIP
revision.
b)
If a plantsource ceases to fulfill the criteria of
Subsection
(a)
of this Section, the requirements of
this Subpart shall continue to apply to
a miscellaneous
organic chemical manufacturing process emission
-s-o-urceunit which was ever subject to the control
requirements of Section 218.966 of this Part.
c)
No limits under this Subpart shall apply to emission
s-ourcesunits with emissions of VON to the atmosphere
less than or equal to 0.91 Mg
(1.0 ton)
per calendar
year if the total emissions from such emission units
sources- not complying with Section 218.966 of this Part
does not exceed 4.5 Mg
(5.0 tons)
per calendar year.
d)
For the purposes of this Subpart, an emission source
unit shall be considered regulated by a Subpart if it
is subject to the limits of that Subpart.
An emission
s-ourceunit is not considered regulated by
a Subpart if
it
is not subject to the limits of that Subpart,
e.g.,
the emission unit is covered by an exemption in
the
Subpart or the applicability criteria of the
Subpart
are not met.
its emissions ar~below the applicability

300
cutoff
level
or
if
the
s-c
eM~emption.
e)
For the purposes of this Subpart, uncontrolled VOM
emissions are the emissions of VON which would result
if
no
air
pollution
control
equipment
were
used.
~j
The control requirements in Subpart PR shall not apply
to sewage treatment plants; vegetable oil extraction
and processing; coke ovens
(including by—product
recovery plants):
fuel combustion units: bakeries;
barge
loading
facilities;
jet
engine
test
cells;
production of ~olvstvrene foam insulation board
including storage and extrusion of scrap where blowing
agent is added to the polystyrene resin at the source.
but not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin: production of polystyrene foam packaging
not including blendng and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin- by the producer
of the resin and not including storage and extrusion of
scrap where blowing agent is added to the polystyrene
resin at the source; and iron and steel -production.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.963
Permit Conditions
No person shall violate any condition in a permit when the
condition results in exclusion of the plantsource or an emission
sourccunit from this Subpart.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
Section 218.966
Control Requirements
Every owner or operator of an emission sourcca miscellaneous
organic chemical manufacturing process emission unit subject to
this -Subpart shall comply with the requirements of subsection
(a)~e~ (b)
or
(c)
below.
a)
Emission capture and control techniques which achieve
-
an overall reduction in uncontrolled VOM emissions of
at least 81 percent from each emission unit,
or
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at a source of a
type that by itself
is subject to control requirements

301
in other Subparts of this Part or 40 CFP 60,
incorporated by reference in Section 218.112,
e.g..
a
coating line,
a printing line,
a process unit,
a
wastewater system, or other equipment, or is otherwise
any part or activity at a source.)
b)
An alternative control plan which has been approved by
the Agency and approved by the USEPA in a federally
enforceable permit or as a SIP revision.
~j
Any leaks from components subject to the control
reguirements of this Subpart shall be subject to the
following control measures bY March 15.
1995:
fl
Repair any component from which a leak of VOL can
be observed. The repair shall be completed as soon
as practicable but no later than 15 days after the
leak is found, unless the leaking component cannot
be repaired until the next process unit shutdown.
in which case the leaking comPonent must be
repaired before the unit is restarted.
~j
For any leak which cannot be readily repaired
within one hour after detection. the following
records, as set forth in this subsection. shall be
kept. These records shall be maintained bY the
owner or Operator for a minimum of two years after
the date on which they are made. Copies of the
records shall be made available to the Aaency or
USEPA
upon verbal or written request.
~
The
name and identification of the leaking
component
~j
The date and time the leak is detected
~j
The action taken to repair the leak: and
p1
The date and time the leak is re~paired.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 218.967
Compliance Schedule
Every owner or operator of an emission sourceunit subject to the
control requirements of this Subpart shall comply with the
requirements of this Subpart on and after a date consistent with
Section 218.106 of this Part.
(Source:
Amended at
Ill.
Peg.
:
effective
____________

302
Section 218.968
Testing
a)
When in the opinion of the Agency it
is necessary to
conduct testing to demonstrate compliance with Section
218.966 of this Part, the owner or operator of
a VON
emission sourceunit subject to the requirements of this
Subpart shall, at his own expense, conduct such tests
in accordance with the applicable test methods and
procedures specified in Section 218.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act,
as
amended,
to
require testing.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
SUBPART TT:
OTHER EMISSION COURCES UNITS
Section 218.980
Applicability
a)
The requirements of this Subpart shall apply to a
plant’s-source’s VOM emission sources-units, which are
not included within any of the o-ouroc categories
specified
in
Subparts
B,
E,
F,
H,
Q,
R,
5,
L.
V,
X,
Y,
Z,
AA,
~
PP,
QQ, or PR of this Part,
or are not
exempted from permitting requirements pursuant to 35
Ill.
Adm. Code 201.146,
if the plantsource is subject
to this Subpart.
A plantsource is subject to this
Subpart if
it contains process emission sources-units,
not regulated by Subparts
B,
E,
F
(excluding Section
218.204(1)
of this Part),
H
(excluding Section 218.405
of this Part),
Q,
R,
5, T (excluding Section 218.486 of
this Part),
V,
X,
Y e~ Z or BE of this Part,
which as
a group both:
1)
~ave
maximum theoretical emissions of 91 Mg
(100
tons)
or more per calendar year of VON if no air
pollution control equipment were used,
and
2)
Aare not limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment, through
production or capacity limitations contained in a
federally enforceable construction or operating
permit or a SIP revision.
b)
If a plantsource ceases to fulfill the criteria of
subsection
(a)
of this Section, the requirements of
this Subpart shall continue to apply to an emission
sourceunit which was ever subject to the control
requirements of Section
2l8.9’86
of this Part.

303
c)
No limits under this Subpart shall apply to emission
sources-units with emissions of VON to the atmosphere
less than or equal to 2.3 Mg (2.5 tons) per calendar
year if the total emissions from such emission units
o-ources- not complying with Section 218.986 of this Part
does
not
exceed
4.5
Mg
(5.0
tons)
per
calendar
year.
d)
For
the
purposes
of
this
Subpart,
an
emission
o-ource
unit shall be considered regulated by a Subpart if it
is subject to the limits of that Subpart.
An emission
sourceunit is not considered regulated by a Subpart if
it
is not subject to the limits of that Subpart,
e.g.~.
the emission unit is covered by an exemption in the
Subpart or the applicability criteria of the Subpart
are not met.
its emissions are below the
applicability
cutoff level or if the source
is
covered
by
an
exemption.
e)
The control requirements in Subparts,
QQ,
PR,
SC
and TT
shall not apply to sewage treatment plants,-j vegetable
oil extraction and processingj
plants, coke ovens
(including by-product recovery plants),-j. fuel
combustion units sources,~bakeriesT~barge loading
facilitiesT.L jet engine test cellsT.L pharmaceutical
ffianufacturing production of polystyrene foam insulation
board
~including
storage
and
extrusion
of
scrap
where
blowing
agent
is
added
to
the
polystyrene
resin
at
the
plant
sourcef,
but
not
including
blending
and
preliminary expansion of resin prior to molding where
blowing agent
is incorporated into the polystyrene
resin by the producer of the resinT~production of
polystyrene foam packaging -(-not including blending and
preliminary expansion of resin prior to molding where
blowing agent is incorporated into the polystyrene
resin by the producer of the resini-, and not including
storage and extrusion of scrap where blowing agent
is
added to the polystyrene resin
at the plantsource-)--~-;
and iron and steel production.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 218.983
Permit Conditions
No person shall violate any condition in a permit when the
condition results in exclusion of the plantsource or an emission
sourceunit from this Subpart.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________

304
Section 218.986
Control Requirements
Every owner or operator of an emission sourccunit subject to this
Subpart shall comply with the requirements of subsection
(a),
(b)~e~ (c)
,
(d), or
(e)
below.
a)
Emission
capture
and
control
equipment
which
achieve
an
overall reduction in uncontrolled VON emissions of at
least
81
percent
from
each
emission
unit,
or
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at a source of a
type that by itself is subject to control requirements
in other Subparts of this Part or 40 CFR 60,
incorporated by reference in Section 218.112,
e.g..
a
coating line,
a printing line, a process unit,
a
wastewater system, or other equipment,
or is otherwise
any part or activity at a source.)
b)
For coating lines, the daily-weighted average VOM
content shall not exceed 0.42 kg VOM/l
(3.5 lbs
VON/gal)
of coating (minus water and any compounds
which are specifically ~exemptedfrom the definition of
VON)
as applied during any day.
Owners and operators
complying with this Section are not required to comply
with Section 218.301 of this Part,
or
c)
An alternative control plan which has been approved by
the Agency and approved by the USEPA in a federally
enforceable permit or as a SIP revision.
~j.
Non—contact process water cooling towers which are
subject to the control requirements of this Subpart
shall comply with the following control measures no
later than March 15,
1995 or upon initial startup:
~j.. The owner or operator of a non—contact process
water cooling tower shall Perform the following
actions to control emissions of volatile organic
material
(VON)
from such a tower:
~j
Inspect and monitor such tower to identify
leaks of VON into the water,
as further
specified in subsection
(d) (3) below
-
~j
When a leak
is identified. initiate and carry
out steps to identify the specific leaking
component or components as soon as
practicable, as further specified in
subsection
(d) (4)
below.
Qj
When a leaking compbnent is identified which:

305
fl
Can be removed from service without
disrupting production,
remove the
component from service
jJJ
Cannot be removed from service without
disrupting production. undertake repair
of the component at the next reasonable
opportunity to do so including any
period when the component is~outof
service for scheduled maintenance,
as
further specified in subsection
(d) (4)
below
p1
Maintain records of inspection and monitoring
activities,
identification of leaks and
leaking components.
elimination and repair of
leaks,
and operation of equipment as related
to these activities,
as further specified in
subsection
(d) (5) below.
21
A VON leak shall be considered to exist in a non-
contact process water cooling water system if the
VON emissions or VON content exceed background
levels as determined bY monitoring conducted in
accordance with subsection (d)(3)i~A)below.
-
The owner or operator of an non—contact process
water cooling tower shall carry out an inspection
and monitoring program to identify VOM leaks in
the cooling water system.
~j
The owner or operator of a non—contact
process water cooling tower shall submit to
the Agency a proposed monitoring Program,
accompanied bY technical justification for
the program, including justification for the
sampling location(s), parameter(s) selected
for_measurement, monitoring and inspection
frequency, and the criteria used relative to
the monitored parameters to determine whether
a
leak
exists
as specified in subsection
(d)(2)
above.
~j
This inspection and monitoring program for
non—contact process water cooling towers
shall
include, but shall not be limited to:
fl
Monitoring of each such tower with a
water flow rate of 25.000 gallons Per
minute or more at a petroleum ref
men
at least weekly and monitoring of
other
towers at least monthly

306
jjj..
Inspection of each such tower at least
weekly
if
monitoring
is
not
performed
at
least weekly.
~j
This
inspection and monitoring program shall
be carried out in accordance with written
procedures
which
the
Agency
shall
specify
as
a condition in a federally enforceable
operating permit.
These procedures shall
include the VON background levels for the
cooling tower as established by the owner or
operator through monitoring; describe the
locations at which samples will be taken;
identify the parameter(s) to be measured,
the
fre~uencvof measurements, and the procedures
for monitoring each such tower, that is,
taking of samples and other subseguent
handling and analyzing of samples; provide
the criteria used to determine that a leak
exists as specified in subsection
(d) (2)
above: and describe the records which will be
maintained.
p1
A non—contact process water cooling tower is
exemPt
from
the
requirements
of
subsections
~d)(3)(B)
and
(d)(3)(C)
above
if
all
equipment where leaks of VON into cooling
water
may
occur
is
operated
at
a
minimum
p~ssure in the cooling water of at least 35
kPa greater than the maximum pressure in the
process fluid.
ii
The repair of a leak in a non—contact process
water cooling tower shall be considered to be
com~1etedin an acceptable manner as follows:
~j.
Efforts to identify and locate the leaking
components are initiated as soon as
practicable, but in no event later than three
days after detection of the leak in the
cooling water tower
~j.
Leaking components shall be repaired or
removed from service as soon as possible but
no later than 30 days after the leak in the
cooling water ?ower
is detected, unless the
leaking components cannot be- repaired until
the next scheduled shutdown for maintenance.
~j
The owner or operator of a non—contact process
water cooling tower shalL keep records as set
forth below in this subsection. These records

307
shall
be retained at
a readily accessible location
at the source and shall be available for
inspection and copying by the Agency for at least
3 years:
~j
Records of inspection and monitoring
activity
~j
Records of each leak identified in such
tower, with date, time and nature of
observation or measured level of parameter
Qj
Records of activity to identify leaking
components, with date initiated,
summary of
comPonents inspected with dates, and method
of inspection and observations
p1
Pecords of activity to remove a leaking
comPonent from service or repair a leaking
component, with date initiated and completed,
description of actions taken and the basis
for determining the leak in such tower has
been eliminated.
If the leaking component is
riot identified, repaired or eliminated within
30 days of initial identification of a leak
in such tower, this report shall include
specific reasons why the leak could not be
eliminated sooner including all other
intervening periods when the process unit was
out of service, actions taken to minimize VOM
losses prior to elimination of the leak and
any actions taken tO prevent the recurrence
of
a leak of this type.
~j
The owner or oPerator of a non—contact Process
water cooling tower shall submit an annual report
to the Agency which provides:
~j
The number of leaks identified in each
cooling tower
-
A general description of activity to repair
Or eliminate leaks -which were identified
Qj
Identification of each leak which was not
repaired in 30 days from the date of
identification of
a leak in such a tower~
with description of the leaks,
explanation
whY the leak was not repaired in
30 days

308
p1
Identification of any periods when required
inspection and monitoring activities were not
carried out.
~j
Any leaks from components subject to the control
requirements of this Subpart shall be subject to the
following control measures by March 15.
1995:
fl
Repair any component from which a leak of VOL can
be observed. The repair shall be completed as soon
as practicable but no later than 15 days after the
--
leak is found, unless the leaking component cannot
be repaired until the next process unit shutdown,
in which case the leaking component must be
repaired before the unit is restarted.
21
For any leak which cannot be readily repaired
within one hour after detection,
the following
records,
as set forth below in this subsection,
shall be kept. These records shall be maintained
by the owner or operator for a minimum of two
years after the date on which they are made.
Copies of the records shall -be made available to
the Agency or USEPA upon verbal or written
request.
~j
The name and identification -of the leaking
component
~j.
The date and time the leak
is detected
Qj
The action taken to repair the leak: and
p1
The date and time the leak is repaired.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 218.987
Compliance Schedule
Every owner or operator of an emissions sourceunit which
is
subject to this Subpart shall comply with the requirements of
this Subpart on and after a date consistent with Section 218.106
of this Part.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 218.988
Testing
a)
When in the opinion of the Agency it is necessary to
conduct testing to demonstrat’e compliance with Section
-

-
309
218.986 of this Part,
the owner or operator of
a VOM
emission sourceunit subject to the requirements of this
Subpart shall,
at his own expense, conduct such tests
in accordance with the applicable test methods and
procedures specified in Section 218.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act, as amended, to
require testing.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________
)
SUBPART UU:
RECORDKEEPING AND REPORTING FOR NON-CTC
SOURCES
Section 218.990
Exempt Emission Sources-Units
Upon request by the Agency, the owner or operator of an emission
unit sour-ce which is exempt from the requirements of Subparts PP,
QQ, PR, TT or Section 218.208(b)
of this Part shall submit
records to the Agency within 30 calendar days from the date of
the request that document that the emission unit source is exempt
from those requirements.
(Source:
Amended at
Ill. Reg.
,
effective
____________
Section 218.991
Subject Emission Sources-Units
a)
Any owner or operator of a VOM emission sourceunit
which is subject to the requirements of Subpart PP,
QQ,
PR or TT and complying by the use of emission capture
and control equipment shall comply with the following:
1)
By a date consistent with Section 218.106 of this
Part,
or upon initial start—up of a new emission
sourceunit,
the owner or operator of the subject
VOM emission spurpeunit shall demonstrate to the
Agency that the subject emission sourceunit will
be in compliance on and after a date consistent
with Section 218.106 of this Part,
or on and after
the initial start-up date by submitting to the
Agency all calculations and other supporting data,
including descriptions and results of any tests
the owner or operator may have performed.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start—up date, the owner or operator of a subject
VON emission source shall collect and record all
of the following information each day and maintain

310
the information at the facilitysource for a period
of three years:
A)
Control device monitoring data.
B)
A log of operating time for the capture
system, control device, monitoring equipment
and the associated emission source.
C)
A maintenance log for the capture system,
control
device
and
monitoring
equipment
detailing
all routine and non—routine
maintenance performed including dates and
duration of any outages.
3)
On and after a date consistent with Section
218.106
of this Part,
the owner or operator of
a
subject VON emission source shall notify the
Agency
in the following instances:
A)
Any record showing a violation of the
requirements of Subpart PP,
QQ, PR or TT
shall be reported by sending a copy of such
--
record to the Agency within 30 days following
the occurrence of the violation.
B)
At least 30 calendar days before changing the
method of compliance with Subpart PP or TT
from the use of capture systems and control
devices to the use of complying coatings, the
owner or operator shall comply with all
requirements of subsection
(b) (1)
of this
Section.
Upon changing the method of
compliance with Subpart PP or TT from the use
of capture systems and control devices to the
use of complying coatings, the owner or
-
operator shall comply with all requirements
of subsection
(b)
of this Section.
4)
Testing
A)
When in the opinion of the Agency it is
necessary to conduct testing to demonstrate
compliance with this Subpart, the owner or
operator of a VON emission source subject to
the requirements of this Subpart shall,
at
his own expense, conduct such tests
in
accordance with the applicable test methods
and procedures specified in Section 218.105
of this Part.

311
-
B)
Nothing in this Section shall limit the
authority of the USEPA pursuant to the Clean
Air Act,
as amended, to require testing.
b)
Any owner or operator of a coating line which is
subject to the requirements of Subpart PP or TT and
complying by means of the daily-weighted average VON
content limitation shall comply with the following:
1)
By a date consistent with Section 218.106 of this
Part,
or
upon
initial
start-up
of
a
coating
line
--
subject
to
Subpart
PP
or
TT,
the
owner
or
operator
of
the
subject
coating
line
shall
certify
to
the
Agency that the coating line will be in compliance
on and after a date consistent with Section
218.106 of this Part, or on and after the initial
start-up date.
Such certification shall include:
A)
The name and identification number of each
coating line which will comply by means of
the daily-weighted average VON content
limitation.
B)
The name and identification number of each
coating as applied on each coating line.
-
C)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating line.
D)
The instrument or method by which the owner
or operator will accurately measure or
calculate the volume of each coating as
applied each day on each coating line.
E)
The method by which the owner or operator
will
create
and
maintain
records
each
day
as
required in subsection
(b) (2)
of this
Section.
F)
An example of the format in which the records
required in subsection
(b) (2)
of this Section
will be kept.
2)
On and after a date consistent with Section
218.106 of this Part,
or on and after the initial
start-up date, the owner or operator of a subject
coating line shall collect and record all of the
following information each day for each coating

312
line and maintain the information at the
facilitysource for a period of three years:
A)
The name and identification number of each
coating
as
applied
on
each
coating
line.
B)
The weight of VOM per volume and the volume
of each coating (minus water and any
compounds which are specifically exempted
from the definition of VOM) as applied each
day on each coating line.
C)
The daily-weighted average VON content of all
coatings as applied on each coating line as
defined in Section 218.104 of this Part.
3)
On and after a date consistent with Section
218.106 of this Part, the owner or operator of
a
subject coating line shall notify the Agency in
the following instances:
A)
Any record showing violation of the
requirements of Subpart PP or TT shall be
reported by sending a copy of such record to
the
Agency
and
the
USEPA
-within
30
days
following
the occurrence of the violation.
B)
At least 30 calendar days before changing the
method of compliance with Subpart PP or TT
from the use of complying coatings to the use
capture systems and control devices,
the
owner or operator shall comply with all
requirements of subsection
(a) (1)
of this
Section.
Upon changing the method of
compliance with Subpart PP or TT from the use
of complying coatings to the use capture
systems and control devices, the owner or
operator shall comply with all requirements
of subsection
(a)
of this Section.
c)
Any owner or operator of a VON emission source which is
subject to the requirements of Subpart PP,
QQ,
PR or TT
and
complying by means of an alternative control plan
which has been approved by the Agency and approved by
the
USEPA
as a SIP revision shall comply with the
recordkeeping and reporting requirements specified in
the alternative control plan.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________

313
Section 218.Appendix A
List of Chemicals Defining Synthetic Organic Chemical and Polymer
Manufacturing
CAS
No.
*
Chemical
105—57—7
Acetal
75-07-0
Acetaldehyde
107—89-1
-
Acetaldol
60-35-5
Acetamide
103-84—4
Acetanilide
64-19-7
-
Acetic acid
108-24-7
Acetic anhydride
67-64-1
Acetone
75-86-5
Acetone cyanohydrin
75-05-8
Acetonitrile
98-86-2
Acetophenone
75-36-5
Acetyl chloride
74-86—2
Acetylene
107—02—8
Acrolein
79-06-1
Acrylamide
79-10-7
Acrylic acid
& esters
107-13-1
Acrylonitrile
124-04-9
Adipic acid
111-69-3
Adiponitrile
Alkyl
naphthalenes
107—18—6
Allyl alcohol
107—05-1
Allyl chloride
1321—11—5
Aminobenzoic acid
111-41-1
Aminoethylethanolamine
123-30-8
p-aminophenol
628-63-7,
Amyl acetates
123—92—2
71_41_0c
Amyl
alcohols
110—58—7
Ainyl
amine
543-59-9
Ainyl chloride
110_68_7c
Amyl
mercaptans
1322-06-1
Ainyl phenol
62—53—3
Aniline
142-04-1
Aniline hydrochloride
29191—52—4
Anisidine
100—66—3
Anisole
118-92-3
Anthranilic acid
84-65-1
Anthraquinone
100-52-7
Benzaldehyde
55—21—0
Benzamide
71—43-2
Benzene
-
98—48-6
Benzenedisulfonic acid
CAS No.
*
Chemical
98-11—3
Benzenesulfonic acid
134—81—6
Benzil
76—93-7
BenziLic acid

314
65-85—0
Benzoic acid
119—53—9
Benzoin
100—47—0
Benzonitrile
119-61-9
Benzophenone
98-07-7
Benzotrichloride
98-88-4
Benzoyl
chloride
100—51—6
Benzyl
alcohol
100-46-9
Benzylamine
120-51-4
Benzyl
benzoate
100-44-7
-
Benzyl
chloride
98-87-3
Benzyl dichloride
92—52—4
Biphenyl
80-05-7
Bisphenol A
10-86-1
Bromobenzene
27497-51-4
Bromonaphthalene
106-99-0
Butadiene
106—98—9
l—butene
123-86-4
n-butyl acetate
141-32-2
n-butyl acrylate
71-36-3
n-butyl alcohol
78-92-2
s-butyl alcohol
75-65-0
t—butyl
alcohol
109-73-9
n-butylamine
13952—84—6
s—butylamine
75-64-9.
t-butylamine
98-73-7
p-tert-butyl benzoic acid
107-88-0
1,3—butylene glycol
123-72-8
n-butyraldehyde
107-92-6
Butyric acid
106-31-0
Butyric anhydride
109-74-0
Butyronitrile
105-60-2
Caprolactam
75-1-50
Carbon disulfide
558-13-4
Carbon tetrabromide
55-23-5
Carbon tetrachloride
9004-35-7
Cellulose acetate
79-11-8
Chloroacetic acid
108—42—9
m—chloroaniline
95-51-2
o-chloroaniline
106-47-8
p-chloroaniline
35913-09-8
Chlorobenzaldehyde
108-90-7
Chlorobenzene
118-91-2,
Chlorobenzoic acid
535—80—8,
CAS
No.
a
Chemical
74_11_3c
2136-81-4,
Chlorobenzotrichloride
2136—89—2,
5216_25_1c
1321-03-5
Chlorobenzoyl chloride
75-45-6
Chlorodifluoroethane

315
25497-29-4
Chlorodifluoromethane
67-66-3
Chloroform
25586-43-0
Chloronaphthalene
88-73—3
o—chloronitrobenzene
100-00-5
p-chloronitrobenzene
25167-80-0
Chlorophenols
126-99-8
Chloroprene
7790—94-5
Chlorosulfonic acid
108-41-8
m-chlorotoluene
95-49-8
o-chlorotoluene
106-43-4
p-chlorotoluene
75-72-9
Chlorotrifluoromethane
108—39—4
-
m—cresol
95—48—7
o—cresol
106—44—5
p—cresol
-
1319-77-3
Mixed cresols
1319—77—3
Cresylic acid
4170-30-0
Crotonaldehyde
3724-65-0
Crontonic acid
98-82-8
Cumene
80-15-9
Cumene hydroperoxide
372-09-8
Cyanoacetic acid
506-77-4
Cyanogen chloride
108-80-5
Cyanuric acid
108-77-0
Cyanuric
chloride
110827
-
Cyclohexane
108-93-0
Cyclohexanol
108-94-1
Cyclohexanone
110-83-8
Cyciohexene
108-91-8
Cyclohexylamine
111-78-4
Cyclooctadiene
112—30-1
Decanol
123-42-2
Diacetone alcohol
27576-04-1
Diaminobenzoic acid
95-76-1,
Dichloroaniline
95—82—9,
554—00—7,
608—27—5,
608—31—1,
626—43—7,
CAS No.
Chemical
27134—27—6,
57311_92_9c
541-73-1
m-dichlorobenzene
95-50-1
o-dichlorobenzene
106-46-7
p-dichlorobenzene
75-71-8
Dichlorodifluoromethane
111-44-4
Dichloroethyl ether
107-06-2
l,2-dichloroethane (EDC)
96-23-1
Dichlorohydrin
26952-23-8
Dichloropropene

316
101—83-7
Dicyclohexylamine
109-89-7
Diethylainine
111—46—6
Diethylene glycol
112-36-7
Diethylene glycol diethyl ether
111-96-6
Diethylene glycol diniethyl
ether
112-34-5
Diethylene glycol inonobutyl
ether
124-17-7
Diethylene glycol inononbutyl
ether
acetate
11L-90-0
Diethylene glycol inonoethyl
ether
112-15-2
Diethylene glycol inonoethyl
ether acetate
111-77-3
Diethylene glycol inonoinethyl
ether
64-67—5
Diethyl sulfate
75-37-6
Difluoroethane
25167—70-8
Diisobutylene
26761—40—0
Diisodecyl phthalate
27554—26—3
Diisooctyl phthalate
674-82-8
Diketene
124-40-3
Dimethylamine
121-69-7
N,N—dimethylaniline
115-10-6
N,N-diuiethyl ether
68-12-2
N,N-diinethylformamide
57-14-7
Dimethyihydrazine
77—78—1
Dimethyl sulfate
75—18—3
Dixnethyl sulfide
67-68-5
Dimethyl sulfoxide
120-61-6
Diniethyl terephthalate
99-34—3
3,5—dinitrobenzoic acid
51-28-5
Dinitrophenol
Dinitrotoluene
123—91—1
pioxane
646—06-0
Dioxilane
CAS No.
a
Chemical
122-39-4
Diphenylamine
101-84-4
Diphenyl oxide
102-08-9
Diphenyl thiourea
25265-71-8
Dipropylene glycol
25378-22-7
Dodecene
28675—17—4
Dodecylaniline
27193-86-8
Dodecyiphenol
106-89-8
Epichlorohydrin
64175
Ethanol
141_43_5c
Ethanolaxnines
141-78-6
Ethyl acetate
141-97-9
Ethyl acetoacetate
140885
Ethyl .acrylate

317
75-04-7
Ethylainine
100-41-4
Ethylbenzene
74-96-4
Ethyl bromide
9004—57-3
Ethylcellulose
75-00-3
Ethyl chloride
105-39-5
Ethyl chloroacetate
105-56-6
Ethylcyanoacetate
74-85-1
Ethylene
96-49-1
Ethylene carbonate
107-07-3
Ethylene chlorohydrin
107-15-3
Ethylenediainine
106-93-4
Ethylene dibroinide
107-21-1
Ethylene glycol
111-55-7
Ethylene glycol diacetate
110-71-4
Ethylene glycol dimethyl ether
111-76-2
Ethylene glycol monobutyl ether
112-07-2
Ethylene glycol inonobutyl ether
acetate
110-80-5
Ethylene glycol monoethyl ether
111-15-9
Ethylene glycol inonoethyl ether
acetate
109-86-4
Ethylene glycol monoethyl ether
110-49-6
Ethylene glycol inonomethyl
ether acetate
122-99-6
Ethylene glycol inonophenyl
ether
2807-30-9
Ethylene glycol inonopropyl
ether
75-21-8
Ethylene oxide
60-29-7
Ethyl ether
104-76-7
2—ethylhexanol
122-51-0
Ethyl orthoformate
95-92-1
Ethyl oxa1~te
41892-71-1
Ethyl sodium oxaloacetate
CAS No.
a
Chemical
50-00-0
Formaldehyde
75-12-7
Formamide
64-18—6
Formic acid
110-17-8
Fumaric acid
98-01-1
Furfural
56-81-5
Glycerol
(Synthetic)
26545-73-7
Glycerol dichiorohydrin
25791-96-2
Glycerol triether
56—40—6
Glycine
107—22—2
Glyoxal
118-74-1
Hexachlorobenzene
67-72-1
Hexachloroethane
36653—82-4
Hexadecyl alcohol
124—09—4
Hexamethylenediamine
629—11-8
Hexamethylene glycol
100-97-0
Hexame~thy1enetetrainine

318
74-90-8
Hydrogen cyanide
123-31-9
Hydroquinone
99-96-7
p—hydroxybenzoic acid
26760-64—5
Isoamylene
78—83-1
Isobutanol
110-19-0
Isobutyl acetate
115—11—7
Isobutylene
78-84-2
Isobutyraldehyde
79-31-2
Isobutyric acid
25339-17—7
Isodecanol
26952—21—6
Isooctyl alcohol
78784
Isopentane
78-59-1
Isophorone
121-91-5
Isophthalic acid
78-79-5
Isoprene
67-63-0
Isopropanol
108-21-4
Isopropyl acetate
75-31-0
Isopropylamine
75-29-6
Isopropyl chloride
25168—06—3
Isopropylphenol
463-51—4
Ketene
Linear alkyl sulfonate*
l23013
Linear alkylbenzene
110—16—7
Maleic acid
108—31—6
Maleic anhydride
6915—15—7
Malic acid
141-79—7
Nesityl oxide
121—47—1
Netanilic acid
79-41-4
Nethacrylic acid
563-47-3
Methallyl chloride
67-56—1
Methanol
CAS No.
a
Chemical
79-20-9
Methyl acetate
105-45-3
Methyl acetoacetate
74-89—5
Methylamine
100—61—8
n—inethylaniline
74-83-9
Methyl bromide
37365-71-2
Methyl butynol
74-87-3
Methyl chloride
108-87-2
Methyl cyclohexane
1331-22-2
Methyl cyclohexanone
75-09-2
Methylene chloride
101-77—9
Methylene dianiline
101-68-8
Methylene diphenyl diisocyanate
78-93-3
Methyl ethyl ketone
107-31-3
Methyl
forinate
108-11-2
Methyl isobutyl carbinol
108-10-1
Methyl isobutyl ketone
80-62—6
Methyl methacrylate
77-75-8
Methylpentynol
98-83-9
B-methylstyrene

319
110-91-8
Morpholine
85-47-2
a-naphthalene sulfonic acid
120—18-3
B-naphthalene sulfonic acid
90-15—3
a—naphthol
135-19-3
B-naphthol
75-98-9
Neopentanoic acid
88—74-4
o—nitroaniline
100—01-6
p—nitroaniline
91-23-6
o-nitroanisole
100—17-4
p—nitroanisole
98-95-3
Nitrobenzene
27178_83_2c
Nitrobenzoic acid
(0,
m
&
p)
79-24-3
Nitroethane
75-52-5
Nitromethane
88-75-5
Nitrophenol
25322-01-4
Nitropropane
1321-12—6
Nitrotoluene
27215—95—8
Nonene
25154-52-3
Nonyiphenol
27193-28—8
Octylphenol
123-63-7
Paraldehyde
115-77-5
Pentaerythritol
109—66—0
n—pentane
109—67—1
1-pentene
127-18-4
Perchioroethylene
594-42-3
Perchioromethyl mercaptan
94-70-2
o-phenetidine
156-43-4
p—phenetidine
CAS No.
a
Chemical
108—95—2
Phenol
98-67—9,
Phenolsulfonic acids
585—38—6,
609—46—1,
l33_39_7c
91-40-7
Phenyl anthranilic acid
Phenylenediamine
7544-5
Phosgene
85-44-9
Phthalic anhydride
85-41-6
Phthalimide
108—99-6
b-picoline
110—85—0
Piperazine
9003-29-6,
Polybutenes
25036_29_7c
25322—68—3
Polyethylene glycol
25322-69-4
Polypropylene glycol
123-38-6
Propionaldehyde
79-09-4
Propionic acid
71—23—8
n-propyl alcohol
107-10-8
Propylainine
540-54-5
Propyl chloride
115—07—1
PropyLene

320
127-00-4
Propylene chlorohydrin
78-87-5
Propylene dichloride
57-55-6
Propylene glycol
75-56-9
Propylene oxide
110—86—1
Pyridine
106-51-4
Quinone
108-46-3
Resorcinol
27138-57-4
Resorcylic acid
69—72—7
Salicylic acid
127-09-3
Sodium acetate
532-32-1
Sodium benzoate
9004-32-4
Sodium carboxyinethyl cellulose
3926-62-3
Sodium chloroacetate
141—53-7
Sodium formate
139-02-6
Sodium phenate
110-44-1
Sorbic acid
100-42—5
Styrene
110-15-6
Succinic acid
110—61—2
Succinitrile
121—57—3
Sulfanilic acid
126—33—0
Sulfolane
1401—55—4
Tannic acid
100-21-0
Terephthalic acid
79_34_5C
Tetrachioroethanes
CAS No.~*
Chemical
117-08-8
Tetrachlorophthalic anhydride
78-00-2
Tetraethyllead
119-64-2
Tetrahydronaphthalene
85-43-8
Tetrahydrophthalic anhydride
75-74-1
Tetramethyllead
110-60-1
Tetramethylenediamine
110-18-9
Tetramethylethylenediamine
108-88-3
Toluene
95-80-7
Toluene—2,4-diamine
584-84-9
Toluene-2
,
4-diisocyanate
26471-62-5
Toluene diisocyanates
(mixture)
1333-07-9
Toluene sulfonamide
104_15_4c
Toluenesulfonic acids
98-59-9
Toluene sulfonyl chloride
26915—12—8
Toluidines
87-61-6,
Trichlorobenzenes
108—70—3,
l20_82_1c
71-55—6
l,l,l—trichloroethane
79—00—5
1, 1
,2—trichloroethane
79-01-6
Trichloroethylene
75-69-4
Trichlorofluoromethane
96-18-4
1,2, 3-trichloropropane
76—13—1
1,1, 2—trichloro—l, 2,2—trifluoro
ethane
121-44-8
Triethylamine

321
112-27-6
Triethylene glycol
112-49-2
Triethylene glycoldimethyl
ether
7756-94-7
Triisobutylene
75-50-3
Trimethylainine
57—13—6
Urea
108—05-4
vinyl acetate
75-01-4
Vinyl chloride
75-35-4
Vinylidene chloride
25013-15-4
Vinyl toluene
1330—20-7
Xylenes
(mixed)
95—47-6
o—xylene
106-42-3
p—xylene
1300—71—6
Xylenol
1300—73—8
Xylidine
methyl tert-butyl ether
9002—88-4
Polyethylene
Polypropylene
9009—53—6
Polystyrene
a)
CAS numbers refer to the Chemical Abstracts Registery
numbers assigned to specific chemicals,
isomers or mixtures
of chemicals.
Some isomers or mixtures that are covered by
the standards do not have CAS numbers assigned to them.
The
standards apply to all of the chemicals listed, whether CAS
numbers have been assigned or not.
b)
No CAS number(s) have been assigned to this chemical, to its
isomers, or mixtures containing these chemicals.
c)
CAS numbers for some of the isomers are listed:
the
standards apply to all of the isomers and mixtures, even if
CAS numbers have not been assigned.
(Source:
Amended at
Ill. Reg.
______,
effective
___________

322
Section 218.Appendix B
VON Measurement Techniques for Capture Efficiency
Procedure G.1
-
Captured
VOG~J
Emissions
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the volatile organic materialsoompoundo (VO~j)content of
captured gas streams.
It is intended to be used as a segment in
the development of liquid/gas or gas/gas protocols for
determining
VO~
capture efficiency
(CE)
for surface coating and
printing operations.
The procedure may not be acceptable in
certain site-specific situations,
e.g., when:
(1) direct fired
heaters or other circumstances affect the quantity of
VO.G~
at the
control device inlet; and
(2) particulate organic aerosols are
formed in the process and are present in the captured emissions.
1.2
Principle.
The amount of
VO~j
captured
(G)
is calculated as
the sum of the products of the
VO~j
content
(CG), the flow rate
and the sample time
(Ta)
from each captured emissions
point.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each captured or fugitive
emissions point as follows:
~
=
5.5 percent and
C0~
=
±5.0percent.
Based on these numbers, the probable
uncertainty for G is estimated at about ±7.4percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours,
unless otherwise approved.
1.5
Notes.
Because this procedure is often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment
and
installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations (percent, ppm) are by
volume, unless otherwise noted.
2.
APPARATUS AND REAGENTS
2.1
Gas
VO~M
Concentration.
A schematic of the measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1
Sample Probe.
Stainless steel,
or equivalent.
The probe
shall be heated to prevent
VOGN
condensation.
2.1.2
Calibration Valve Assembly.
Three—way valve assembly at
the outlet of sample probe to direct the zero and calibration

323
gases to the analyzer.
Other methods,
such as quick—connect
lines, to route calibration gases to the outlet of the sample
probe are acceptable.
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak—free pump, to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components of the
pump that contact the gas stream shall be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample Flow Rate Control.
A sample flow rate control
valve and rotameter,
or equivalent, to maintain a constant
sampling rate within 10 percent.
The flow rate control valve and
rotameter must be heated to prevent condensation.
A control
valve may also be located on the sample pump bypass loop to
assist in controlling the sample pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion of
the sample gas stream to the flame ionization analyzer
(FIA), and
the remainder to the bypass discharge vent.
The manifold
components shall
be constructed of stainless steel or Teflon.
If
captured or fugitive emissions are to be measured at multiple
locations, the measurement system shall be designed to use
separate sampling probes,
lines, and pumps for each measurement
location and a common sample gas manifold and FIA.
The sample
gas manifold and connecting lines to the FIA must be heated to
prevent condensation.
2.1.7
Organic Concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however,
other span values may be used if
it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration Drift.
Less than ±3.0percent of the span
value.
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.1.7.4
Response Time.
Less than 30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition. system used to integrate
the FIA response or compute the average response and record

324
measurement data.
The minimum data sampling frequency for
computing average or integrated values
is one measurement value
every 5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required) are contained in
compressed gas cylinders.
All calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtures, such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent H2/60 percent He or 40 percent H2/60
percent
N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material (as propane or carbon equivalent)
or less than
0.1 percent of the span value, whichever is greater.
2.1.9.3
FIA Linearity Calibration Gases.
Low-, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
45-55,
and 70—80 percent of the span
value
in air, respectively.
Other calibration values and other
span values may be used if
it can be shown that more accurate
measurements would be achieved.
2.1.10
Particulate Filter.
An in-stack or an out-of-stack glass
fiber filter is recommended
if exhaust gas particulate loading
is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless
it can be demonstrated that no
condensation occurs.
2.2
Captured Emissions Volumetric Flow Rate.
2.2.1
Method
2 or 2A Apparatus.
For determining volumetric flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if it can be justified.

325
2.2.3
Method
4 Apparatus and Reagents.
For determining moisture
content,
if necessary.
3.
DETERMINATION OF VOLUMETRIC FLOW RATE OF CAPTURED EMISSIONS
3.1
Locate all points where emissions are captured from the
affected f-~cilityemissionunit.
Using Method
1, determine the
sampling points.
Be sure to check each site for cyclonic or
swirling flow.
3.2
Measure the velocity at each sampling site at least once
every hour during each sampling run using Method
2 or 2A.
4.
DETERMINATION
OF VOGM CONTENT OF CAPTURED EMISSIONS
4.1
Analysis Duration.
Measure the
VOG~
responses at each
captured emissions point during the entire test run or,
if
applicable, while the process
is operating.
If there are
multiple captured emission locations, design a sampling system to
allow a single FIA to be used to determine the
VOGM
responses at
all sampling locations.
4.2
Gas
VOGM
Concentration.
4.2.1
Assemble the sample train as shown in Figure
1.
Calibrate
the FIA according to the procedure in Section 5.1.
4.2.2
Conduct a system check according to the procedure in
Section 5.3.
4.2.3
Install the sample probe
so that the probe
is centrally
located in the stack, pipe,
or duct,
and
is sealed tightly at the
stack port connection.
4.2.4
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach zero.
Measure the
system response time as the time required for the system to reach
the effluent concentration after the calibration valve has been
returned to the effluent sampling position.
4.2.5
Conduct
a system check before and a system drift check
after each sampling run according to the procedures in Sections
5.2 and 5.3.
If the drift check following a run indicates
unacceptable performance, the run is not valid.
The tester may
elect to perform system drift checks during the run not to exceed
one drift check per hour.
4.2.6
Verify that the sample lines,
filter,
and pump
temperatures are 120 ±5°C.

326
4.2.7
Begin sampling at the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
appropriate.
If multiple captured emission locations are sampled
using a single FIA, sample at each location for the same amount
of time (e.g.,
2 minutes) and continue to switch from one
location to another for the entire test run.
Be sure that total
sampling time at each location is the same at the end of the test
run.
Collect at least
4 separate measurements from each sample
point during each hour of testing.
Disregard the measurements at
each sampling location until two times the response time of the
measurement system has elapsed.
Continue sampling for at least
1
minute and record the concentration measurements.
4.3
Background Concentration.
4.3.1
Locate all NDO’s of the TTE.
A sampling point shall be
centrally located outside of the TTE at
4 equivalent diameters
from each NDO,
if possible.
If there are more than
6 NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.2
Assemble the sample train as shown in Figure
2.
Calibrate
the FIA and conduct a system check according to the procedures in
Sections 5.1 and 5.3.
NOTE:
This sample train shall be a
separate sampling ~rain from the one to measure the captured
emissions.
4.3.3
Position the probe at the sampling location.
4.3.4
Determine the response time, conduct the system check and
sample according to the procedures described in Sections 4.2.4 to
4.2.7.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described in Section 7.2 of Method 18 may be
used to determine the gas VOC concentration.
The system must be
designed to collect and analyze at least one sample every 10
minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA
Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the
FIA
and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero— and the high—range calibration
gases and adjust the analyzer calibration to provide the proper
responses.
Inject the low- and mid-range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable If the responses for all

327
four gases are within
5 percent of the respective gas values.
If
the performance of the system
is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct a calibration
and linearity check after assembling the analysis system and
after a major change is made to the system.
5.2
Systems Drift Checks.
Select the calibration gas that most
closely approximates the concentration of the captured emissions
for conducting the drift checks.
Introduce the zero and
calibration gas at the calibration valve assembly and verify that
the appropriate gas flow rate and pressure are present at the
FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained in Section 5.1
is less than 3 percent of the span
value.
Conduct the system drift checks at the end of each run.
5.3
System Check.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
The
performance of the system is acceptable
if the measurement system
response is within
5 percent of the value obtained in Section 5.1
for the high range calibration gas.
Conduct a system check
before and after each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
6.
NOMENCLATURE
A1
=
area
of
NDO
i,
ft2--~
AN
=
total
area
of
all
NDO’s
in
the
enclosure,
ft2-ri
=
corrected average
VOGN
concentration
of
background
emissions at point
i, ppm propane-~j
C8
=
average background concentration, ppm propane-~
CGJ
=
corrected average
VOGN
concentration of captured
emissions at point
j,
ppm propane-~
=
average measured concentration for the drift check
calibration gas, ppm propane-~j
C~
=
average system drift check concentration for zero
concentration gas, ppm propane-a
=
actual concentration of the drift check
calibration gas, ppm prqpane~

328
C1
=
uncorrected average background
VOGN
concentration
measured at point
i, ppm propane~-~
=
uncorrected average
VOGN
concentration measured at
point
j,
ppm propane--j.
G
=
total
VOGN
content of captured emissions,
kg~-j.
K1
=
1.830 x 10~kg/(m3—ppm).-j~.
n
=
number of measurement points--.j
Q~
=
average effluent volumetric flow rate corrected to
standard conditions at captured emissions point
j,
m3/min--j
T~
=
total duration of captured emissions sampling run,
mm.
7.
CALCULATIONS
7.1
Total
VOGN
Captured Emissions.
n
G
=
E
(C01
-
CB
)
Q~T~K1
Eq.
1
j=1
7.2
VOGN
Concentration of the Captured Emissions at Point
j.
C01
=
(C~
-
C~)
CH
Eq.
2
CDO
7.3
Background
VOGN
Concentration at Point
i.
C81
=
(C1
-
C~)
CH
Eq.
3
-
C~
7.4
Average Background Concentration.
n
E
C81A~
C8
=
i-i
Eq.
4
nAN
NOTE:
If the concentration at each point
is within 20 percent of
• the average concentration of all points, the terms
“A1” and “AN”
may be deleted from Equation 4.

329
Procedure G.2
-
Captured
VOGN
Emissions
(Dilution Technique)
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the volatile organic oompound3materials
(VOGN)
content
of
captured gas streams.
It is intended to be used as a segment in
the development of a gas/gas protocol in which fugitive emissions
are measured for determining
VOGN
capture efficiency
(CE)
for
surface coating and printing operations.
A dilution system is
used to reduce the
VOGN
concentration of the captured emission to
about the same concentration as the fugitive emissions.
The
procedure may not be acceptable in certain site—specific
situations, e.g., when:
(1) direct fired heaters or other
circumstances affect the quantity of
VOGN
at the control device
inlet; and
(2) particulate organic aerosols are formed in the
process and are present in the captured emissions.
1.2
Principle.
The amount of
VOGN
captured
(G)
is calculated as
the sum of the products of the
VOGN
content
(C0),
the flow rate
(Q01),
and the sampling time
(Ta) from each captured emissions
point.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each captured or fugitive
emissions point as follows:
Q0~
=
±5.5percent and C0~
= ±5
percent.
Based on these numbers, the probable uncertainty for G
is estimated at about ±7.4percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.
1.5
Notes.
Because this procedure is often applied in highly
explosive areas,
caution and care should be exercised in choosinç
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations (percent, ppm) are by
volume, unless otherwise noted.
2.
APPARATUS
AND REAGENTS
2.1
Gas
VOGN
Concentration.
A schematic of the measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1
Dilution System.
A Kipp in-stack dilution probe and
controller or similar device may be used.
The dilution rate may
be changed by substituting different critical orifices or
adjustments of the aspirator supply pressure.
The dilution

330
system shall be heated to prevent
VOGN
condensation.
Note:
An
out-of-stack dilution device may be used.
2.1.2
Calibration Valve Assembly.
Three-way valve assembly at
the outlet of sample probe to direct the zero and calibration
gases to the analyzer.
Other methods, such as quick—connect
lines,
to route calibration gases to the outlet of the sample
probe are acceptable.
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak-free pump,
to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components of the
pump that contact the gas stream shall be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample Flow Rate Control.
A sample flow rate control
valve and rotameter,
or equivalent,
to maintain a constant
sampling rate within 10 percent.
The flow control valve and
rotameter must be heated to prevent condensation.
A control
valve may also be located on the sample pump bypass loop to
assist in controlling the sample pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion of
the sample gas stream to the flame ionization analyzer
(FIA),
and
the remainder to the bypass discharge vent.
The manifold
components shall be constructed of stainless steel or Teflon.
If
captured or fugitive emissions are to be measured at multiple
locations, the measurement system shall be designed to use
separate sampling probes,
lines, and pumps for each measurement
location and a common sample gas manifold and FIA.
The sample
gas manifold and connecting lines to the FIA must be heated to
prevent condensation.
2.1.7
Organic Concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however,
other span values may be used if it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration Drift.
Less than ±3.0percent of the span
value.
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.

331
2.1.7.4
Response Time.
Less than 30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel, and combustion air
(if required)
are contained in
compressed gas cylinders.
All calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtures,
such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent H2/60 percent He or 40 percent 112/60
percent
N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from
a mean value.
2.1.9.2
Carrier Gas and Dilution Air Supply.
High purity air
with less than
1 ppm of organic material
(as propane or carbon
equivalent)
or less than 0.1 percent of the span value, whichever
is greater.
2.1.9.3
FIA Linearity Calibration Gases.
Low-,
mid-, and
high—range gas mixture standards with nominal propane
concentrations of 20-30, 45-55,
and 70-80 percent of the span
value
in air, respectively.
Other calibration values and other
span values may be used if it can be shown that more accurate
measurements would be achieved.
2.1.9.4
Dilution Check Gas.
Gas mixture standard containing
propane in air, approximately half the span value after dilution.
2.1.10
Particulate Filter.
An in-stack or an out-of-stack glass
fiber filter is recommended
if exhaust gas particulate loading is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless
it can be demonstrated that no
condensation occurs.
2.2
Captursd Emissions Volumetric Flow Rate.

332
2.2.1
Method
2 or 2A Apparatus.
For determining volumetric flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if it can be justified.
2.2.3
Method
4 Apparatus and Reagents.
For determining moisture
content, if necessary.
3.
DETERMINATION OF VOLUMETRIC FLOW RATE OF CAPTURED EMISSIONS
3.1
Locate all points where emissions are captured from the
affected facility. Using Method
1, determine the sampling points.
Be sure to check each site for cyclonic or swirling flow.
3.2
Measure the velocity at each sampling site at least once
every hour during each sampling run using Method
2 or 2A.
4.
DETERMINATION
OF
VOGM
CONTENT OF CAPTURED EMISSIONS
4.1
Analysis Duration.
Measure the
VOGN
responses at each
captured emissions point during the entire test run or,
if
applicable, while the process is operating.
If there are a
multiple captured emissions locations, design a sampling system
to allow a single FIA to be used to determine the
VOGN
responses
at all sampling locations.
4.2
Gas
VOGN
Concentration.
4.2.1
Assemble the sample train as shown
in Figure
1.
Calibrate
the FIA according to the procedure in Section 5.1.
4.2.2
Set the dilution ratio and determine the dilution factor
according to the procedure in Section 5.3.
4.2.3
Conduct a system check according to the procedure in
Section 5.4.
4.2.4
Install the sample probe so that the probe
is centrally
located in the stack, pipe,
or duct,
and is sealed tightly
at
the
stack port connection.
4.2.5
Inject zero gas at the calibration valve assembly.
Measure the system response time as the time required for the
system to reach the effluent concentration after the calibration
valve has been returned to the effluent sampling position.
4.2.6
Conduct a system check before and a system drift check
after each sampling run according to the procedures in Sections
5.2 and 5.4.
If the drift check following a run indicates
unacceptable performance, the run is not valid.
The tester may

333
elect to perform system drift checks during the run not to exceed
one drift check per hour.
4.2.7
Verify that the sample lines,
filter, and pump
temperatures are 120 ±5°C.
4.2.8
Begin sampling at the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
appropriate.
If multiple captured emission locations are sampled
using a single FIA, sample at each location for the same amount
of time (e.g.,
2 minutes) and continue to switch from one
location to another for the entire test run.
Be sure that total
sampling time at each location is the same at the end of the test
run.
Collect at least
4 separate measurements from each sample
point during each hour of testing.
Disregard the measurements at
each sampling location until two times the response time of the
measurement system has elapsed.
Continue sampling for at least
1
minute and record the concentration measurements.
4.3
Background Concentration.
4.3.1
Locate all NDO’s of the TTE.
A sampling point shall be
centrally located outside of the TTE at
4 equivalent diameters
from each NDO,
if possible.
If there are more than
6 NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.2
Assemble the sample train as shown in Figure
2.
CalibratE
the FIA and conduct a system check according to the procedures
ir
Sections 5.1 and
5.4.
4.3.3
Position the probe at the sampling location.
4.3.4
Determine the response time,
conduct the system check and
sample according to the procedures described in Sections 4.2.4
tc
4.2.8.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described in Section 7.2 of Method 18 may be
used to determine the gas
VOGN
concentration.
The system must bE
designed to collect and analyze at least one sample every
10
minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA
Calibration
and
Linearity
Check.
Make
necessary
adjustments
to
the
air
and
fuel
supplies
for
the
FIA
and ignite
the
burner.
Allow
the
FIA
to
warm
up
for
the
period
recommended
by
the manufacturer.
Inject
a calibration gas into the
measurement system after the dilution system and adjust the back-
pressure regulator to the value requir&i to achieve the flow

334
rates specified by the manufacturer.
Inject the zero— and the
high-range calibration gases and adjust the analyzer calibration
to provide the proper responses.
Inject the low- and mid—range
gases and record the responses of the measurement system.
The
calibration and linearity of the system are acceptable if the
responses for all four gases are within
5 percent of the
respective gas values.
If the performance of the system is not
acceptable, repair or adjust the system and repeat the linearity
check.
Conduct a calibration and linearity check after
assembling the analysis system and after a major change
is made
to the system.
5.2
Systems Drift Checks.
Select the calibration gas that most
closely approximates the concentration of the diluted captured
emissions for conducting the drift checks.
Introduce the zero
and calibration gas at the calibration valve assembly and verify
that the appropriate gas flow rate and pressure are present at
the FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained in Section 5.1 is less than
3 percent of the span
value.
Conduct the system drift check at the end, of each run.
5.3
Determination of Dilution Factor.
Inject the dilution check
gas into the measurement system before the dilution system and
record the response.
Calculate the dilution factor using
Equation
3.
5.4
System Check.
Inject the high range calibration gas at the
inlet to the sampling probe while the dilution air
is turned off.
Record the response.
The performance of the system is acceptable
if the measurement system response is within
5 percent of the
value obtained in Section 5.1 for the high range calibration gas.
Conduct a system check before and after each test run.
5.5
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
6.
NOMENCLATURE
A1
=
area
of
NDO
i,
ft2-~-j
AN
=
total
area
of
all
NDO’s
in
the
enclosure,
ft2--j
CA
=
actual concentration of the dilution check gas,
ppm propane--j
C81
=
corrected average
VOGN
concentration of background
emissions at point
i, ppm propane--;.

335
CB
=
average background concentration, ppm propane-j
CDH
=
average measured concentration for the drift check
calibration gas, ppm propane.~
=
average system drift check concentration for zero
concentration
gas, ppm propane--;
=
actual concentration of the drift check
calibration gas, ppm propane.~
C1
=
uncorrected average background
VOGN
concentration
measured at point
i, ppm propane~-j
Ci
=
uncorrected average
VOGN
concentration measured at
point
j,
ppm propane~
CM
=
measured concentration of the dilution check gas,
ppm propane--j
DF
=
dilution factor~-~
G
=
total VOCN content of captured emissions, kg~
Xl
=
1.830
x
10~
kg/(m3-ppm)-rj.
n
=
number of measurement points--.L
Q0,
=
average effluent volumetric flow rate corrected to
standard conditions at captured emissions point
j,
m3/min--j
T0
=
total
duration of capture efficiency sampling run,
mm.
7.
CALCULATIONS
7.1
Total
VOGN
Captured Emissions.
n
G
=
E
C01
Q~T~ K1
Eq.
1
j=l
7.2
VOGN
Concentration of the Captured Emissions at Point
j.
C~
= DF
(C1
-
C~)
CH
Eq.
2
-
C~
7.3
Dilution
Factor.

336
DF
=
CA~
Eq.
3
CM
7.4
Background
VOGN
Concentration at Point
i.
C81
=
(C1
-
C~)
CN
Eq.
4
C~
-
C~
7.5
Average Background Concentration.
n
E
•C~A1
C8
=
i=1
Eq.
5
nAN
NOTE:
If
the
concentration
at
each
point
is
within
20
percent
of
the average concentration of all points, the terms
“A1” and
“AN”
may be deleted from Equation 4.
Procedure F.2
-
Fugitive
VOGN
Emissions from Building Enclosures
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the fugitive volatile organic comnpoundomaterials
(VOG!j) emissions
from a building enclosure
(BE).
It is intended to be used as
a
segment in the development of liquid/gas or gas/gas protocols for
determining
VOGN
capture efficiency
(CE)
for surface coating and
printing operations.
1.2
Principle.
The ‘total amount of fugitive
VOGN
emissions
(F8)
from the BE is calculated as the sum of the products of the
VOGN
content
(CFJ)
of each fugitive emissions point,
its flow rate
(QF~)I
and time
(TF).
1.3
Measurement Uncertainty.
The measurement uncertainties are
estimated for each fugitive emissions point as follows:
QF1
=
±5.0percent and
CFJ
=
±5.0percent.
Based on these numbers, the
probable uncertainty for F8 is estimated at about ±11.2percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.
1.5
Notes.
Because this procedure is often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations (percent, ppm)
are by
volume,
unless otherwise noted.

337
2.
APPARATUS
AND REAGENTS
2.1
Gas
VOGN
Concentration.
A
schematic
of
the
measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1
Sample Probe.
Stainless steel, or equivalent.
The probe
shall be heated to prevent
VOGN
condensation.
2.1.2
Calibration Valve Assemb~y. Three—way valve assembly at
the outlet of sample probe to direct the zero and calibration
gases to the analyzer.
Other methods, such as quick—connect
lines,
to route calibration gases to the outlet of the sample
probe are acceptable.
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak-free pump, to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components of the
pump that contact the gas stream shall be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample’ Flow Rate Control.
A sample flow rate control
valve and rotameter,
or equivalent,
to maintain a constant
sampling rate within 10 percent.
The flow rate control valve and
rotameter must be heated to prevent condensation.
A control
valve may also be located on the sample pump bypass loop to
assist in controlling the sample pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion of
the sample gas stream to the flame ionization analyzer
(FIA),
and
the
remainder
to
the
bypass
discharge
vent.
The
manifold
components
shall
be
constructed
of
stainless
steel
or
Teflon.
If
emissions are to be measured at multiple locations, the
measurement system shall be designed to use separate sampling
probes,
lines, and pumps for each measurement location and a
common sample gas manifold and FIA.
The sample gas manifold must
be heated to prevent condensation.
2.1.7
Organic Concentration Analyzer.
An FIA with a span value
of
1.5
times
the
expected
concentration
as
propane;
however,
other span values may be used if it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.

338
2.1.7.2
Calibration Drift.
Less than ±3.0percent of the span
value.
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.1.7.4
Response Time.
Less than 30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values
is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required)
are contained in
compressed gas cylinders.
All calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
.,~For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtures, such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent H2/60 percent He or 40 percent
112/60
percent N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material
(propane or carbon equivalent)
or less than 0.1
percent of the span value, whichever is greater.
2.1.9.3
FIA Linearity Calibration Gases.
Low—, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
45-55,
and 70-80 percent of the span
value in air, respectively.
Other calibration values and other
span values may be used if it can be shown that more accurate
measurements would be achieved.
2.1.10
Particulate Filter.
An in-stack or an out-of-stack glass
fiber filter is recommended
if exhaust gas particulate loading is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless
it can be demonstrated that no
condensation occurs.

339
2.2
Fugitive Emissions Volumetric Flow Rate.
2.2.1
Flow Direction Indicators.
Any means of indicating inward
or outward flow, such as light plastic film or paper streamers,
smoke tubes,
filaments?
and sensory perception.
2.2.2
Method
2
or 2A Apparatus.
For determining volumetric flow
rate.
Anemometers or similar devices calibrated according to the
manufacturer’s instructions may be used when low velocities are
present.
Vane anemometers
(Young—maximum response propeller),
specialized pitots with electronic manometers
(e.g.,
Shortridge
Instruments Inc., Airdata Multimeter 860) are commercially
available with measurement thresholds of 15 and
8 mpm (50 and
25 fpm),
respectively.
2.2.3
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if it can be justified.
2.2.4
Method
4 Apparatus and Reagents.
For determining moisture
content,
if
necessary.
3.
DETERMINATION OF VOLUMETRIC FLOW RATE OF FUGITIVE EMISSIONS
3.1
Preliminary Determinations.
The purpose of this exercise is
to determine
which exhaust points should be measured for volumetric flow rates
and
VOGN
concentrations.
3.1.1
Forced Draft Openings.
Identify all forced draft
openings.
Determine the volumetric flow rate according to Method
2.
3.1.2
NDO’s Exhaust Points.
The NDO’s
in the roof of a facility
the building or room
in which the emission unit is located are
considered to be exhaust points.
Determine volumetric flow rate
from these NDO’s.
Divide the cross—sectional area according to
Method
1 using 12 equal areas.
Use the appropriate velocity
measurement devices, e.g., propeller anemometers.
3.1.3
Other NDO’s.
3.1.3.1
This step
is optional.
Determine the exhaust flow rate,
including that of the control device,
from the enclosure and the
intake air flow rate.
If the exhaust flow rate divided by the
intake air flow rate
is greater than 1.1, then all other NDO’s
are not considered to be significant exhaust points.
3.1.3.2
If the option above is not taken,
identify all other
NDO’s and other potential points through which fugitive emissions
may escape the enclosure.
Then use the following criteria to

340
determine whether flow rates and
VOGM
concentrations need to be
measured:
3.1.3.2.1
Using the appropriate flow direction indicator,
determine the flow direction.
An NDO with zero or inward flow is
not an exhaust point.
3.1.3.2.2
Measure
the
outward
volumetric
flow
rate
from
the
remainder of the NDO’s.
If the collective flow rate is
2
percent,
or
less,
of
the
flow
rate
from
Sections
3.1.1
and
3.1.2,
then these NDO’s, ‘except those within two equivalent diameters
(based on NDO.opening) from ~
VOGN
oourccoemitting point, may be
considered to be non—exhaust points.
3.1.3.2.3
If
the
percentage
calculated
in
Section
3.1.3.2.2
is
greater than
2 percent, those NDO’s
(except those within two
equivalent diameters from a
VOGN
oourcccemitting
point)
whose
volumetric flow rate total
2 percent of the flow rate from
Sections 3.1.1 and 3.1.2 may be considered as non—exhaust points.
All
remaining
NDO’s
shall
be
measured
for
volumetric
flow
rate
and VOGN concentrations during the CE test.
3.1.3.2.4
The tester may choose to measure VOGN concentrations
at the forced exhaust points and the NDO’s.
If the total
VOGM
emissions from the NDO’s are less than
2 percent of the emissions
from
the
forced
draft
and
roof
NDO’s,
then
these
NDO’s
may
be
eliminated from further consideration.
3.2
Determination of Flow Rates.
3.2.1
Measure
the
volumetric
flow
rate
at
all
locations
identified
as
exhaust
points
in Section 3.1.
Divide each
exhaust
opening
into
9
equal areas for rectangular openings and
8
for
circular openings.
3.2.2
Measure
the
velocity
at
each
site
at
least
once
every
hour
during each sampling run using Method
2 or 2A,
if applicable,
or
using
the
low
velocity
instruments
in
Section
2.2.2.
4.
DETERMINATION
OF
VOGM
CONTENT
OF
FUGITIVE
EMISSIONS
4.1
Analysis Duration.
Measure the
VOGN
responses at each
fugitive emission point during the entire test run or,
if
applicable, while the process is operating.
If there are
multiple emissions locations, design a sampling system to allow a
single FIA to be used to determine the
VOGN
responses at all
sampling locations.
4.2
Gas
VOGN
Concentration.

341
4.2.1
Assemble the sample train as shown in Figure
1.
Calibrate
the FIA and conduct a system check according to the procedures in
Sections 5.1 and 5.3, respectively.
4.2.2
Install the sample probe
so that the probe is centrally
located in the stack, pipe,
or duct, and is sealed tightly at the
stack port connection.
4.2.3
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach zero.
Measure the
system
response
time
as
the
time
required
for
the
system
to
reach
the effluent concentration after the calibration valve has been
returned to the effluent sampling position.
4.2.4
Conduct a system check before and a system drift check
after
each
sampling
run
according
to
the
procedures
in
Sections
5.2 and 5.3.
If the drift check following a
run
indicates
unacceptable performance,
the run is not valid.
The tester may
elect to perform drift checks during the run not to exceed one
drift
check
per
hour.
4.2.5
Verify
that
the
sample
lines,
filter,
and
pump
temperatures are 120 ±5°C.
4.2.6
Begin sampling at the start of the test period and
continue to sample during the entire run.’
Record the starting
and ending times and any required process information as
appropriate.
If multiple emission locations are sampled using a
single FIA,
sample at each location for the same amount of time
(e.g.,
2 minutes)
and continue to switch from one location to
another for the entire test run.
Be sure that total sampling
time at each location is the same at the end of the test run.
Collect at least
4 separate measurements from each sample point
during each hour of testing.
Disregard the response measurements
at each sampling location until two times the response time of
the measurement system has elapsed.
Continue sampling for at
least
1 minute and record the concentration measurements.
4.3
Alternative Procedure
The direct interface sampling and
analysis procedure described in Section 7.2 of Method 18 may be
used to determine the gas
VOGN
concentration.
The system must be
designed to collect and analyze at least one sample every 10
minutes.
5.
CALIBRATION
AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rate~specified by the

342
manufacturer.
Inject the zero— and the high—range calibration
gases
and adjust the analyzer calibration to provide the proper
responses.
Inject the low- and mid-range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable if the responses for all
four gases are within
5 percent of the respective gas values.
If
the performance of the system is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct a calibration
and linearity check after assembling the analysis system and
after a major change is made to the system.
5.2
Systems Drift Checks.
Select the calibration gas that most
closely approximates the concentration of the captured emissions
for conducting the drift checks.
Introduce the zero and
calibration gas at the calibration valve assembly and verify that
the appropriate gas flow rate and pressure are present at the
FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained in Section 5.1
is less than
3 percent of the span
value.
Conduct a system drift check at the end of each run.
5.3
System Check.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
‘The
performance of the system is acceptable if the measurement system
response is within
5 percent of the value obtained in Section 5.1
for the high range calibration gas.
Conduct a system check
before each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
6.
NOMENCLATURE
CDH
average measured concentration for the drift check
calibration gas, ppm propane-ri.
=
average system drift check concentration for zero
concentration gas, ppm propane~
=
corrected average VOGN concentration of fugitive
emissions at point
j,
ppm propane-a
CR
=
actual concentration of the drift check
calibration gas, ppm propane-~
C1
=
uncorrected average VOGN concentration measured at
point
j,
ppm propane-~

343
F8
=
total VOGN content of fugitive emissions from the
building,
kg--;.
K1
=
1.830 x 10~kg/(m3-ppm)-~j
n
=
number of measurement points-a
Q~
=
average effluent volumetric flow rate corrected to
standard conditions at fugitive emissions point
j,
m3/min.-.L
TF
=
total duration of capture efficiency sampling run,
• nun.
7.
CALCULATIONS
7.1
Total VOGN Fugitive Emissions From the Building.
n
F8
=
&
CE,
QF,
TE
K1
Eq.
1
j=1
7.2
VOGN
Concentration of the Fugitive Emissions at Point
j.
CF~
=
(~,
-
C~)
CR
Eq.
2
CDH
-
C~
Procedure F.1
Fugitive VOGN Emissions from Temporary Enclosures
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the fugitive volatile organic compoundcmaterials
(VOGN)
emissions
from a temporary total enclosure (TTE).
It is intended to be
used as a segment in the development of liquid/gas or gas/gas
protocols for determining
VOGM
capture efficiency
(CE)
for
surface coating and printing operations.
1.2
Principle.
The amount of fugitive VOGN emissions
(F) from
the TTE is calculated as the sum of the products of the
VOGN
content (CF~)~the flow rate
(QF,),
and the sampling time
(TE)
from
each fugitive emissions point.
1.3
Estimated Measurement Uncertainty.’
The measurement
uncertainties
are
estimated
for each fugitive emission
point
as follows:
QFJ
=
±5.5percent and CF1
=
±5.0percent.
Based on
these numbers, the probable uncertainty for F is estimated at
about ±7.4percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.

344
1.5
Notes.
Because
this
procedure
is
often
applied
in
highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations
(percent, ppm) are by
volume, unless otherwise noted.
2.
APPARATUS
AND
REAGENTS
2.1
Gas
VOGN
Concentration.
A schematic of the measurement
system is shown in Figure
1.
The
main
components
are
described
below:
2.1.1
Sample Probe.
Stainless steel, or equivalent.
The probe
shall
be
heated
to
prevent
VOGN
condensation.
2.1.2
Calibration
Valve
Assembly.
Three-way
valve
assembly
at
the
outlet
of
sample
probe
to
direct
the
zero
and
calibration
gases
to
the
analyzer.
Other
methods,
such
as
quick—connect
lines,
to
route
calibration
gases
to
the
outlet
of
the
sample
probe
are
acceptable.
2.1.3
Sample
Line.
Stainless
steel
or
Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be
heated
to
prevent
condensation.
2.1.4
Sample
Pump.
A
leak-free
pump,
to
pull
the
sample
gas
through the system ‘at a flow rate sufficient to minimize the
response time of the measurement system.
The components of the
pump
that
contact
the
gas
stream
shall
be constructed of
stainless steel or Tefion.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample Flow Rate Control.
A sample flow rate control
valve
and
rotameter,
or
equivalent,
to
maintain
a
constant
sampling
rate
within
10
percent.
The
flow
control
valve
and
rotameter
must
be
heated
to
prevent
condensation.
A
control
valve
may
also
be
located
on
the
sample
pump
bypass
loop
to
assist
in
controlling
the
sample
pressure
and
flow
rate.
2.1.6
Sample
Gas
Manifold.
Capable
of diverting a portion of
the
sample
gas stream to the flame ionization analyzer
(FIA),
and
the remainder to the bypass discharge vent.
The manifold
components
shall
be constructed of stainless steel or Teflon.
If
emissions are to be measured at multiple locations, the
measurement system shall be designed to use separate sampling
probes,
lines, and pumps for each measurement location and a
common sample gas manifold and FIA.
The sample gas manifold and
connecting lines to the FIA must be heated to prevent
condensation.

345
2.1.7
Organic
Concentration
Analyzer.
An
FIA
with
a
span
value
of 1.5 times the expected concentration as propane; however,
other span values may be used if
it can be demonstrated that they
would
provide
more
accurate
measurements.
The
system
shall
be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration
Drift.
Less
than
±3.0 percent
of
the
span
value.
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.1.7.4
Response
Time.
Less
than
30
seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing
average or integrated values is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and
combustion
air
(if
required)
are
contained
in
compressed gas cylinders.
All calibration gases shall be
traceable
to
NIST
standards
and
shall
be
certified
by
the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtures,
such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent 112/60 percent He or 40 percent H2/60
percent N2 gas mixture is recommended to avoid an oxygen
synergism
effect that reportedly occurs when oxygen concentration
varies significantly from a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material
(as
propane
or
carbon
equivalent)
or
less
than
0.1 percent of the span value, whichever is greater.
2.1.9.3
FIA Linearity Calibration Gases.
Low-,
mid-,
and
high—range gas mixture standards with nominal propane
concentrations
of
20-30,
45-55,
and
70-80
percent
of
the
span
value in air, respectively.
Other calibration values and other

346
span values may be used if it can be shown that more accurate
measurements
would
be
achieved.
2.1.10
Particulate Filter.
An in-stack or an out—of-stack glass
fiber filter is recommended if exhaust gas particulate loading is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless it can be demonstrated that no
condensation occurs.
2.2
Fugitive Emissions Volumetric Flow Rate.
2.2.1
Method
2 or 2A Apparatus.
For determining volumetric flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if
it can be justified.
2.2.3
Method
4 Apparatus and Reagents.
For determining moisture
content,
if
necessary.
2.3
Temporary
Total
Enclosure.
The
criteria
for designing a TTE
are discussed in Procedure T.
3.
DETERMINATIONOF
VOLUMETRIC
FLOW RATE OF FUGITIVE EMISSIONS
3.1
Locate all points where emissions are exhausted from the
TTE.
Using Method
1,
determine
the
sampling
points.
Be
sure
to
check
each
site
for
cyclonic
or
swirling
flow.
3.2
Measure the velocity at each sampling site at least once
every
hour
during
each
sampling
run
using
Method
2
or
2A.
4.
DETERMINATION
OF
VOGM
CONTENT OF FUGITIVE EMISSIONS
4..
Analysis
Duration.
Measure
the
VOGN
responses at each
fugitive emission point during the entire test run or,
if
applicable,
while
the
process
is
operating.
If
there
are
multiple emission locations, design a sampling system to allow a
single FIA to be used to determine the
VOGM
responses at all
sampling
locations.
4.2
Gas VOGN Concentration.
4.2.1
Assemble the sample train as shown
in Figure
1.
Calibrate
the FIA and conduct a system check according to the procedures
in
Sections 5.1 and 5.3, respectively.
4.2.2
Install the sample probe so that the probe
is centrally
located in the stack,
pipe, or duct,
and
is sealed tightly at the
stack port connection.

347
4.2.3
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach zero.
Measure the
system response time as the time required for the system to reach
the effluent concentration after the calibration valve has been
returned to the effluent sampling position.
4.2.4
Conduct a system check before and a system drift check
after each sampling run according to the procedures in Sections
5.2
and
5.3.
If
the
drift
check
following
a
run
indicates
unacceptable performance, the run is not valid.
The tester may
elect
to
perform
system
drift
checks
during
the
run
not
to
exceed
one drift check per hour.
4.2.5
Verify that the sample lines,
filter, and pump
temperatures are 120 ±5°C.
4.2.6
Begin sampling at the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
appropriate.
If multiple emission locations are sampled using a
single FIA, sample at each location for the same amount of time
(e.g.,
2 minutes)
and continue to switch from one location to
another
for
the
entire
test
run.
Be
sure
that
total
sampling
time at each location is
the
same
at
the
end
of
the
test
run.
Collect at least
4 separate measurements from each sample point
during each hour of testing.
Disregard the response measurements
at
each
sampling
location
until
two
times
the
response
time
of
the measurement system has elapsed.
Continue sampling for at
least
1 minute and record the concentration measurements.
4.3
Background Concentration.
4.3.1
Determination of VOGN Background Concentration.
4.3.1.1
Locate all NDO’s of the TTE.
A sampling point shall be
centrally
located
outside
of
the
TTE
at
4 equivalent diameters
from
each
NDO,
if
possible.
If
there
are
more
than
6
NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.1.2
Assemble the sample train as shown in Figure
2.
Calibrate the FIA and conduct a system check according to the
procedures in Sections 5.1 and 5.3.
4.3.1.3
Position the probe at the sampling location.
4.3.1.4
Determine the response time, conduct the system check
and sample according to the procedures described in Sections
4.2.3
to
4.2.6.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described in Section 7.2 of Method 18 may be
used
to
determine
the
gas
VOGN
concentfation.
The
system
must
be

348
designed to collect and analyze at least one sample every 10
minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the
burner.
Allow
the
FIA
to
warm
up
for
the
period
recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero— and the high—range calibration
gases and adjust the analyzer calibration to provide the proper
responses.
Inject the low— and mid—range gases and record the
responses
of
the
measurement
system.
The
calibration
and
linearity
of
the
system
are
acceptable
if
the
responses
for
all
four gases are within
5
percent of the respective gas values.
If
the performance of the system is not acceptable,
repair or adjust
the system and repeat the linearity check.
Conduct a calibration
and linearity check after assembling the analysis system and
after a major change is made to the system.
5.2
Systems Drift Checks.
Select the calibration gas
concentration that most closely approximates that of the fugitive
gas emissions to conduct the :dr~tchecks.
Introduce the zero
and calibration gas at the calibration valve assembly and verify
that
the
appropriate
gas
flow
rate
and
pressure
are present at
the
FIA.
Record
the
measurement
system
responses
to
the
zero
and
calibration
gases.
The performance of the system is acceptable
if the difference between the
drift
check
measurement
and
the
value obtained in Section 5.1 is less than
3 percent of the span
value.
Conduct a system drift check at the end of each run.
5.3
System Check.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
The
performance of the system is acceptable if the measurement system
response is within
5 percent of the value obtained in Section 5.1
for the high range calibration gas.
Conduct a system check
before each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within
10
percent.
6.
NOMENCLATURE
=
area
of
NDO
i,
ft2-~j
AN
=
total area of all NDO’s in the enclosure, ft2-~

349
C81
=
corrected average
VOGN
concentration of background
emissions at point
1, ppm propane.~
C8
=
average background concentration, ppm propane~-j
CDH
=
average measured concentration for the drift check
calibration gas, ppm propane-~j
C~
=
average system drift check concentration for zero
concentration gas, ppm propane~
CFi
=
corrected average
VOGN
concentration of fugitive
emissions at point
j,
ppm propane1-j
CR
=
actual concentration of the drift check
calibration gas, ppm propane-~
C1
=
uncorrected average background VOGN concentration
measured at point
i, ppm propane--j
C,
=
uncorrected average
VOGN
concentration measured at
point
j,
ppm propane~-j
G
=
total
VOGN
content of captured emissions,
kg-ri
K1
=
1.830 x 10~kg/(m3-ppm).-j
n
=
number of measurement points--;
QFJ
=
average effluent volumetric flow rate corrected to
standard conditions at fugitive emissions point
j,
m3
/
min-i.
TF
=
total duration of fugitive emissions sampling run,
mm.
7.
CALCULATIONS
7.1
Total
VOGN
Fugitive Emissions.
n
F
=
E
(CF,
-
C8
)
Q~TF K1
Eq.
1
j=1
7.2
VOGN Concentration of the Fugitive Emissions at Point
j.
CE,
=
(C1
-
C~)
CR
Eq.
2
CDH
-
7.3
Background
VOGN
Concentration at Point
i.

350
CBI
=
(C1
-
C~)
Eq.
3
-
CDO
7.4
Average Background Concentration.
n
E
C81
A,
C8
=
i=1
Eq.
5
nAN
NOTE:
If the concentration at each point is within 20 percent of
the average concentration of all points, the terms
“At” and “AN”
may be deleted from Equation 4.
Procedure L
-
VOGN
Input
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the input of volatile organic compound~materials (VOGN).
It
is
intended to be used as a segment in the development of liquid/gas
protocols for determining
VOGN
capture efficiency
(CE) for
surface coating and printing operations.
1.2
Principle.
The amount of
VOGN
introduced to the process
(L)
is the sum of the products of the weight
(W)
of each
VOGN
containing liquid
(ink, paint,
solvent,
etc.)
used and its
VOGN
content
(V).
A sample of each VOGN containing liquid is analyzed
with a flame ionization analyzer
(FIA)
to determine V.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each
VOGN
containing liquid as
follows:
W
=
2.0 percent and V
=
±12.0percent.
Based on these
numbers, the probable uncertainty for L is estimated at about
±12.2percent for each VOGN containing liquid.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.
1.5
Notes.
Because this procedure is often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations (percent, ppm)
are by
volume, unless otherwise noted.
2.
APPARATUS
AND
REAGENTS
2.1
Liquid Weight.

351
2.1.1
Balances/Digital Scales.
To weigh drums of VOGN
containing liquids to within 02
lb.
2.1.2
Volume Measurement Apparatus (Alternative).
Volume
meters,
flow meters, density measurement equipment, etc.,
as
needed to achieve same accuracy as direct weight measurements.
2.2
VOGN Content
(Flame Ionization Analyzer Technique).
The
liquid sample analysis system is shown in Figures
1 and 2.
The
following equipment is required:
2.2.1
SampleCollection Can.
An appropriately sized metal can
to be used to collect
VOGN
containing materials.
The can must be
constructed in such a way that it can be grounded to the coating
container.
2.2.2
Needle Valves.
To control gas flow.
2.2.3
Regulators.
For carrier gas and calibration gas
cylinders.
2.2.4
Tubing.
Teflon or stainless steel tubing with diameters
and lengths determined by connection requirements of equipment.
The tubing between the sample oven outlet and the FIA shall• be
heated to maintain a temperature of
120.±5°C.
2
2
5
Atmospheric Vent
A tee and 0- to 0 5-liter/mm
rotameter
placed in the sampling line between the carrier gas cylinder and
the
VOGN
sample vessel to release the excess carrier gas.
A
toggle valve placed between the tee and the rotameter facilitates
leak tests of the analysis system.
2.2.6
Thermometer.
Capable of measuring the temperature of the
hot water bath to within 1°C.
2.2.7
Sample Oven.
Heated enclosure, containing calibration gas
coil heaters,
critical orifice, aspirator,
and other liquid
sample analysis components,
capable of maintaining a temperature
of 120 ±5°C.
2.2.8
Gas Coil Heaters.
Sufficient lengths of stainless steel
or Teflon tubing to allow zero and calibration gases to be heated
to the sample oven temperature before entering the critical
orifice or aspirator.
2.2.9
Water Bath.
Capable of heating and maintaining a sample
vessel temperature of 100 ±5°C.
2.2.10
Analytical Balance.
To measure ±0.001g.
2.2.11
Disposable Syringes.
2-cc or 5-cc.

352
2.2.12
Sample Vessel.
Glass,
40—nil septum vial.
A separate
vessel
is needed for each sample.
2.2.13
Rubber Stopper.
Two—hole stopper to accommodate 3.2-mm
(1/8-in.) Teflon tubing, appropriately sized to fit the opening
of the sample vessel.
The rubber stopper should be wrapped in
Teflon tape to provide a tighter seal and to prevent any reaction
of the sample with the rubber stopper.
Alternatively, any
leak—free closure fabricated of non—reactive materials and
accommodating the necessary tubing fittings may be used.
2.2.14
Critical Orifices.
Calibrated critical orifices capable
of providing constant flow rates from 50 to 250 ml/min at known
pressure drops.
Sapphire orifice assemblies
(available from
O’Keefe Controls Company)
and glass capillary tubing have been
found to be adequate for this application.
2.2.15
Vacuum Gauge.
0- to 760-mm
(0- to 30-in.) Hg U-Tube
manometer or vacuum gauge.
2.2.16
Pressure Gauge.
Bourdon gauge capable of measuring the
maximum air pressure at the aspirator inlet
(e.g.,
100 psig).
2.2.17
Aspirator.
A device capable of generating sufficient
vacuum at the sample vessel to create critical flow through the
calibrated orifice when sufficient air pressure is present at the
aspirator inlet.
The aspirator must also provide sufficient
sample pressure to operate the FIA.
The sample is also mixed
with the dilution gas within the aspirator.
2.2.18
Soap Bubble Meter.
Of an appropriate size to calibrate
the critical orifices in the system.
2.2.19
Organic concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however other
span values may be used if
it can be demonstrated that they would
provide more accurate measurements.
The system shall be capable
of meeting or exceeding the following specifications:
2.2.19.1
Zero Drift.
Less than ±3.0percent of the span value.
2.2.19.2
Calibration Drift.
Less than ±3.0percent of span
value.
2.2.19.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.2.20
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values
is one measurement value

353
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.2.21
Chart Recorder (Optional).
A chart recorder or similar
device is recommended to provide a continuous analog display of
the measurement results during the liquid sample analysis.
2.2.22
Calibration and Other Gases.
For calibration,
fuel,
and
combustion air
(if required) contained in compressed gas
cylinders.
All calibration gases shall be traceable to NIST
standards and shall be certified by the manufacturer to ±1
percent of the tag value.
Additionally, the manufacturer of the
cylinder should provide a recommended shelf life for each
calibration gas cylinder over which the concentration does not
change more than ±2percent from the certified value.
For
calibration gas values not generally available,
alternative
methods for preparing calibration gas mixtures, such as dilution
systems, may be used with prior approval.
2.2.22.1
Fuel.
A 40 percent H2/60 percent He or 40 percent 112/60
percent N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from a mean value.
2.2.22.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material
(as propane)
or less than 0.1 percent of the
span value, whichever is greater.
2.2.22.3
FIA Linearity Calibration Gases.
Low-, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
45-55, and 70—80 percent of the span
value in air, respectively.
Other calibration values and other
span values may be used if
it can be shown that more accurate
measurements would be achieved.
2.2.22.4
System Calibration Gas.
Gas mixture standard
containing propane in air, approximating the undiluted
VOGM
concentration expected for the liquid samples.
3.
DETERMINATION OF LIQUID INPUT WEIGHT
3.1
Weight Difference.
Determine the amount of material
introduced to the process as the weight difference of the feed
material before and after each sampling run.
In determining the
total
VOGN
containing liquid usage, account for:
(a) the initial’
(beginning) VOGN containing liquid mixture;
(b) ~ny solvent added
during the test run;
(c)
any coating added during the test run;
and
(d) any residual
VOGN
containing liquid mixture remaining at
the end of the sample run.

354
3.1.1
Identify all points where VOGN containing liquids are
introduced to the process.
To obtain an accurate measurement of
VOGN
containing liquids, start with an empty fountain (if
applicable).
After completing the run, drain the liquid in the
fountain back into the liquid drum (if possible), and weigh the
drum again.
Weigh the
VOGN
containing liquids to ±0.5percent of
the total weight
(full)
or ±0.1percent of the total weight of
VOGM containing liquid used during the sample run, whichever is
less.
If the residual liquid cannot be returned to the drum,
drain the fountain into a preweighed empty drum to determine the
final weight of the liquid.
3.1.2
If it is not possible to measure a single representative
mixture, then weigh the various components separately
(e.g.,
if
solvent is added during the sampling run, weigh the solvent
before it is added to the mixture).
If a fresh drum of
VOGM
containing liquid is needed during the run, then weigh both the
empty drum and fresh drum.
3.2
Volume Measurement
(Alternative).
If direct weight
measurements are not feasible, the tester may use volume meters
and flow rate meters
(and density measurements) to determine the
weight of liquids used if it can be demonstrated that the
technique produces results equivalent to the direct weight
measurements.
If a single representative mixture cannot be
measured, measure the components separately.
4.
DETERMINATION OF VOGN
CONTENT
IN INPUT LIQUIDS
4.1
Collection of Liquid Samples.
4.1.1
Collect a 100-nil or larger sample of the
VOGN
containing
liquid mixture at each application location at the beginning and
end of each test run.
A separate sample should be taken of each
VOGN
containing liquid added to the application mixture during
the test run.
If a fresh drum is needed during the sampling run,
then obtain a sample from the fresh drum.
4.1.2
When collecting the sample, ground the sample container to
the coating drum.
Fill the sample container as close to the rim
as possible to minimize the amount of headspace.
4.1.3
After the sample is collected,
seal the container so the
sample cannot leak out or evaporate.
4.1.4
Label the container to identify clearly the contents.
4.2
Liquid Sample VOGN Content.
4.2.1
Assemble the liquid
VOGN
content analysis system as shown
in Figure
1.

355
4.2.2
Permanently identify all of the critical orifices that may
be used.
Calibrate each critical orifice under the expected
operating conditions
(i.e.,
sample vacuum and temperature)
against a volume meter as described in Section 5.3.
4.2.3
Label and tare the sample vessels (including the stoppers
and caps)
and the syringes.
4.2.4
Install an empty sample vessel and perform a leak test of
the system.
Close the carrier gas valve and atmospheric vent and
evacuate the sample vessel to 250
mm
(10 in.) Hg absolute or less
using the aspirator.
Close the toggle valve at the inlet to the
aspirator and observe the vacuum for at least one minute.
If
there
is any change in the sample pressure, release the vacuum,
adjust or repair the apparatus as necessary and repeat the leak
test.
4.2.5
Perform the analyzer calibration and linearity checks
according to the procedure in Section 5.1.
Record the responses
to each of the calibration gases and the back—pressure setting of
the FIA.
4.2.6
Establish the appropriate dilution ratio by adjusting the
aspirator air supply or substituting critical orifices.
Operate
the aspirator at a vacuum of at least 25
mm
(1 in.) Hg greater
than the vacuum necessary to achieve critical flow.
Select the
dilution ratio so that the maximum response of the FIA to the
sample does not exceed the high-range calibration gas.
4.2.7
Perform system calibration checks at two levels by
introducing compressed gases at the inlet to the sample vessel
while the aspirator and dilution devices are operating.
Perform
these checks using the carrier gas (zero concentration) and the
system calibration gas.
If the response to the carrier gas
exceeds ±0.5percent of span,
clean or repair the apparatus and
repeat the check.
Adjust the dilution ratio as necessary to
achieve the correct response to the upscale check,
but do not
adjust the analyzer calibration.
Record the identification of
the orifice, aspirator air supply pressure, FIA back—pressure,
and the responses of the FIA to the carrier and system
calibration gases.
4.2.8
After completing the above checks,
inject the system
calibration gas for approximately
10 minutes.
Time the exact
duration of the gas injection using a stopwatch.
Determine the
area under the FIA response curve and calculate the system
response factor based on the sample gas flow rate, gas
concentration, and the duration of the injection as compared to
the integrated response using Equations
2 and 3.
4.2.9
Verify that the sample oven and ,cample line temperatures
are 120 ±5°C
and that the water bath temperature
is 100 ±5°C.

356
4.2.10
Fill a tared syringe with approximately
1 g of the
VOGN
containing liquid and weigh it.
Transfer the liquid to a tared
sample vessel.
Plug the sample vessel to minimize sample loss.
Weigh the sample vessel containing the liquid to determine the
amount of sample actually received.
Also,
as a quality control
check, weigh the empty syringe to determine the amount of
material delivered.
The two coating sample weights should agree
within ±0.02g.
If not, repeat the procedure until an acceptable
sample
is obtained.
4.2.11
Connect the vessel to the analysis system.
Adjust the
aspirator supply pressure to the correct value.
Open the valve
on the carrier gas supply to the sample vessel and adjust it to
provide a slight excess flow to the atmospheric vent.
As soon as
the initial response of the FIA begins to decrease,
immerse the
sample vessel in the water bath.
(Applying heat to the sample
vessel too soon may cause the FID response to exceed the
calibrated range of the instrument, and thus invalidate the
analysis.)
4.2.12
Continuously measure and record the response of the FIA
until all of the volatile material has been evaporated from the
sample and the instrument response has returned to the baseline
(i.e., response less than 0.5 percent of the span value).
Observe the aspirator supply pressure, FIA back—pressure,
atmospheric vent,
and other system operating parameters during
the run; repeat the analysis procedure if any of these parameters
deviate from the values established during the system calibration
checks in Section 4.2.7.
After each sample perform the drift
check described in Section 5.2.
If the drift check results are
acceptable, calculate the
VOGN
content of the sample using the
equations in Section
7.
Integrate the area under the FIA
response curve,
or determine the average concentration response
and the duration of sample analysis.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero— and the high—range calibration
gases and adjust the analyzer calibration to provide the proper
responses.
Inject the low— and mid—range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable if the responses for all
four gases are within
5 percent of the respective gas values.
If
the performance of the system is not acceptable,
repair or adjust
the system and repeat the linearity check.
Conduct a calibration

357
and linearity check after assembling the analysis system and
after a major change is made to the system.
5.2
Systems Drift Checks.
After each sample, repeat the system
calibration checks in Section 4.2.7 before any adjustments to the
FIA or measurement system are made.
If the zero or calibration
drift exceeds ±3percent of the span value, discard the result
and repeat the analysis.
5.3
Critical Orifice Calibration.
5.3.1
Each critical orifice must be calibrated at the specific
operating conditions that it will be used.
Therefore, assemble
all components of the liquid sample analysis system as shown in
Figure
3.
A stopwatch is also required.
5.3.2
Turn on the sample oven,
sample line,
and water bath
heaters and allow the system to reach the proper operating
temperature.
Adjust the aspirator to a vacuum of 380 mm
(15 in.)
Hg vacuum.
Measure the time required for one soap bubble to move
a known distance and record barometric pressure.
5.3.3
Repeat the calibration procedure at a vacuum of 406 mm
(16
in.) Hg and at 25-mm
(1-in.) Hg intervals until three consecutive
determinations provide the same flow rate.
Calculate the
critical flow rate for the orifice in nil/mm
at standard
conditions.
Record the vacuum necessary to achieve critical
flow.
6.
NOMENCLATURE
AL
=
area under the response curve of the liquid
sample,
area count--.L
A8
=
area under the response curve of the calibration
gas, area count--j
C8
=
actual concentration of system calibration gas,
ppm propane-~
K
=
1.830 x 10~g/(ml-ppm)-~
L
=
total VOGM content of liquid input, kg~-~~
ML
=
mass of liquid sample delivered to the sample
vessel,
g’-.~
q
=
flow rate through critical orifice, ml/min~-~
RF
=
liquid analysis system response factor, g/area
count--j

358
T8
=
total gas injection time for system calibration
gas during integrator calibration,
min--.L
=
final
VOGN
fraction of VOGN containing liquid
~-rj.
V11
=
initial
VOGN
fraction of
VOGN
containing liquid
J~.L
VAJ
=
VOGN fraction of
VOGN
containing liquid
j
added
during the run-~
V
=
VOq~
fraction of liquid samnple-a-j
=
weight of VOGN containing liquid
j
remaining at
end of the run,
kg--j.
=
weight of VOGN containing liquid
j
at beginning of
the run,
kg--j
WAJ
=
weight of VOGN containing liquid
j
added during
the run, kg.
7.
CALCULATIONS
7.1
Total
VOGN
Content of the Input
VOGN
Containing Liquid.
n
n
n
L=
EVIJW,JVFjWFJ+
E
VA~WAJ
R
Eq.l
j1
j=l
j=l
7.2
Liquid
Sample
Analysis
System
Response
Factor
for
Systems
Using Integrators, Grams/Area Counts.
RF
=
~g~jç
Eq.
2
A8
7.3
VOG~
Content of the Liquid Sample.
V=~~
Eq.
3
ML
Procedure T
Criteria for and Verification of a Permanent or
Temporary Total Enclosure
1.
INTRODUCTION
1.1
Applicability.
This procedure is used to determine whether
a permanent or temporary enclosure meets the criteria of a total
enclosure.

359
1.2
Principle.
An enclosure is evaluated against a set of
criteria.
If the criteria are met and if all the exhaust gases
are ducted to a control device, then the volatile organic
compoundomaterials
(VOGN)
capture efficiency
(CE)
is assumed to
be 100 percent and CE need not be measured.
However,
if part of
the exhaust gas stream is not ducted to a control device, CE must
be determined.
2.
DEFINITIONS
2.1
Natural Draft Opening
(NDO)
--
Any permanent opening in the
enclosure that remains open during operation of the facility
emission unit and is not connected to a duct in which a fan is
installed.
2.2
Permanent Total Enclosure
(PTE)
--
A permanently installed
enclosure that completely surrounds a~oourcc of emissioneunit
such that all
VOGN
emissions are captured and contained for
discharge through a control device.
2.3
Temporary Total Enclosure
(TTE)
—-
A temporarily installed
enclosure that completely surrounds a~oourcc of emissionsunit
such that all
VOGN
emissions are captured and contained for
discharge through ducts that allow for the accurate measurement
of
VOGN
rates.
3.
CRITERIA OF A TEMPORARY TOTAL ENCLOSURE
3.1
Any NDO shall be at least
4 equivalent opening diameters
from each
VOGN
emitting, point.
3.2
Any exhaust point from the enclosure shall be at least
4
equivalent duct or hood diameters from each NDO.
3.3
The total area of all NDO’s shall not exceed
5 percent of
the surface area of the enclosure’s four walls,
floor,
and
ceiling.
3.4
The average facial velocity
(FV)
of air through all NDO’s
shall be at least 3,600
ni/hr
(200 fpm).
The direction of air
through all NDO’s shall
be into the enclosure.
3,5
All access doors and windows whose areas are not included in
Section 3.3 and are not included
in the calculation in Section
3.4 shall
be closed during routine operation of the
prooccoemission unit.
4.
CRITERIA OF A PERMANENT TOTAL ENCLOSURE
4.1
Same as Sections 3.1 and 3.3
3.5.

360
4.2
All
VOGN
emissions must be captured and contained for
discharge through a control device.
5.
PROCEDURE
5.1
Determine the equivalent diameters of the NDO’s and
determine the distances from each
VOGN
emitting point to all
NDO’s.
Determine the equivalent diameter of each exhaust duct or
hood and its distance to all NDO’s.
Calculate the distances in
terms of equivalent diameters.
The number of equivalent
diameters shall be at least
4.
5.2
Measure the total area
(A1) of the enclosure and the total
area
(AN)
of all NDO’s of the enclosure.
Calculate the NDO to
enclosure area ratio
(NEAR)
as follows:
NEAR
= AN/Al
The NEAR must be
0.05.
5.3
Measure the volumetric flow rate, corrected to standard
conditions,
of each gas stream exiting the enclosure through an
exhaust duct or hood using EPA Method
2.
In some cases
(e.g.,
when the building is the enclosure),
it may be necessary to
measure the volumetric flow rate, corrected to standard
conditions,
of each gas stream entering the enclosure through a
forced makeup air duct using Method
2.
Calculate FV using the
following equation:
FV
=
Q0
-
QI/AN
where:
Q0
=
the sum of the volumetric flow from all gas
streams exiting the enclosure through an exhaust
duct or hood.
Q1
=
the sum of the volumetric flow from all gas
streams into the enclosure through a forced makeup
air duct;
zero,
if there is no forced makeup air
into the enclosure.
AN
=
total area of all NDO’s in enclosure.
The FV shall
be at least 3,600
ni/hr
(200 fpm).
5.4
Verify that the direction of air flow through all NDO’s
is
inward.
Use streamers,
smoke tubes,
tracer gases,
etc.
Strips
of plastic wrapping film have been found to be effective.
Monitor the direction of air flow at intervals of at least 10
minutes for at least
1 hour.

361
6.
QUALITY
ASSURANCE
6.1
The
success
of
this
protocol
lies
in
designing
the
TTE
to
simulate the conditions that exist without the TTE,
i.e.,
the
effect of the TTE on the normal flow patterns around the affected
faoilityemission unit or the amount of fugitive
VOGN
emissions
should be minimal.
The TTE must enclose the application
stations,
coating reservoirs,
and all areas from the application
station to the oven.
The oven does not have to be enclosed
if
it
is under negative pressure.
The
NDO’s of the temporary enclosure
and a fugitive exhaust fan must be properly sized and placed.
6.2.
Estimate the ventilation rate of the TTE that best
simulates the conditions that exist without the
TTE,
i.e., the
effect of the TTE on the normal flow patterns around the affected
fzicilityemission unit or the amount of fugitive
VOGN
emissions
should be minimal.
Figure
1
may be used as an aid.
Measure the
concentration
(C0)
and flow rate
(Q0)
of the captured gas stream,
specify a safe concentration
(CE)
for the fugitive gas stream,
estimate the CE,
and then use the plot in Figure
1
to determine
the volumetric flowrate of the fugitive gas stream
(QF).
A
fugitive
VOGN
emission exhaust fan that has a variable flow
control
is desirable.
6.2.1
Monitor the concentration of
VOGN
into the capture device
without the TTE.
To minimize the effect of temporal variation on
the captured emissions, the baseline measurement should be made
over as long a time period as practical.
However, the process
conditions must be the same for the measurement in Section 6.2.3
as they are for this baseline measurement.
This may require
short measuring times for this quality control check before and
after the construction of the TTE.
6.2.2
After the TTE is constructed, monitor the
VOGN
concentration inside the TTE.
This concentration shall not
continue to increase and must not exceed the safe level according
to OSHA requirements for permissible exposure limits.
An
increase in
VOGN
concentration indicates poor TTE design or poor
capture efficiency.
6.2.3
Monitor the concentration of
VOGN
into the capture device
with the TTE.
To limit the effect of the TTE on the process, the
VOGN concentration with and without the TTE must be within ±10
percent.
If the measurements do not agree,
adjust the
ventilation rate from the TTE until they agree within 10 percent.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

362
Section 218.Appendix C
Reference Test Methods ana ProccdurcoFor Air Oxidation Processes
Introduction
This Appendix presents the reference, methods and procedures
required for implementing Reasonably Available Control Technology
(RACT).
Methods and procedures are identified for two types of
RACT implementation:
a)
Determination of
VOGN
destruction efficiency for evaluating
compliance with the 98 weight percent
VOGN
reduction or 20
ppmv emission limit specified in Sections 215.520 through
215.527; and
b)
Determination of offgas flowrate, hourly emissions and
stream net heating value for calculating TRE.
All reference methods identified
in this Appendix refer to the
reference methods specified at 40 CFR 60, Appendix A,
incorporated by reference in Section 215.105.
VOGN
DESTRUCTION EFFICIENCY DETERMINATION
The following reference methods and procedures are required for
determining compliance with the percent destruction efficiency
specified in Sections 215.520 through 215.527.
a)
Reference Method
1 or 1A for selection of the sampling site.
The control device inlet sampling site for determination of
vent stream molar composition or total organic compound
destruction efficiency shall be prior to the inlet of any
control device and after all recovery devices.
b)
Reference Methods
2,
2A,
2C or 2D for determination of the
volumetric flowrate.
c)
Reference Method
3 to measure oxygen concentration of the
air dilution correction.
The emission sample shall be
corrected to
3 percent oxygen.
d)
Reference Method 18 to determine the concentration of total
organic compounds
(minus methane and ethane)
in the control
device outlet and total organic compound reduction
efficiency of the control device.
TRE DETERMINATION
The following reference methods and procedures are required for
determining the offgas flowrate, hourly emissions,
and the net
heating value of the gas combusted to calculate the vent stream
TRE.

363
a)
Reference Method
1 or 1A for selection of the sampling site.
The sampling site for the vent stream flowrate and molar
composition determination prescribed in
(b) and
(c)
shall be
prior to the inlet of any combustion device, prior to any
post-reactor dilution of the stream with air and prior to
any post-reactor introduction of halogenated compounds into
the vent stream.
Subject to the preceding restrictions on
the sampling site,
it shall be after the final recovery
device.
If any gas stream other than the air oxidation vent
stream is normally conducted through the recovery system of
the affected facility, such stream shall be rerouted or
turned off while the vent stream is sampled, but shall be
routed normally prior to the measuring of the initial value
of the monitored parameters for determining compliance with
the recommended RACT.
If the air oxidation vent stream is
normally routed through any equipment which is not a part of
the air oxidation process as defined in 35 Ill.
Adm. Code
211.122,
such equipment shall be bypassed by the vent stream
while the vent stream is sampled,
but shall not be bypassed
during the measurement of the initial value of the monitored
parameters for determining compliance with Subpart V.
b)
The molar composition of the vent stream shall be determined
using the following methods:
1)
Reference Method 18 to measure the concentration of all
organics, including those containing halogens, unless a
significant portion of the compounds of interest are
polymeric (high molecular weight), can polymerize
before analysis or have low vapor pressures,
in which
case Reference Method 25(a)
shal.l be used.
2)
ASTM D1946-67
(reapproved 1977),
incorporated by
reference in Section 215.105, to measure the
concentration of carbon monoxide and hydrogen.
3)
Reference Method
4 to measure the content of water
vapor,
if necessary.
c)
The volumetric flowrate shall be determined using Reference
Method
2,
2A,
2C or 2D,
as appropriate.
d)
The net heating value of the vent stream shall be calculated
using the following equation:
n
H=K
E
CiHi
i=1
Where:
H
=
Net heating value of the sample, NJ/scm, where the

364
net enthalpy per mole of offgas is based on
combustion at 25°Cand 760 mm Hg, but the standard
temperature for determining the volume
corresponding to one mole is 20°C,as in the
definition of F
(vent stream flowrate)
below.
K
=
Constant,
1.740 x 10~(1/ppm)
(mole/scm)
(MJ/kcal)
where standard temperature for mole/scm is 20°C.
Ci
=
Concentration of sample component i, reported on
a
wet basis,
in ppm,
as measured by Reference Method
18 or ASTN Dl946—67
(reapproved 1977),
incorporated by reference in Section 215.105.
Hi
=
Net heat of combustion of sample component
i,
kcal/mole based on combustion at 25~Cand 760 mm
Hg.
If published values are not available or
cannot be calculated,
the heats of combustion of
vent stream components are required to be
determined using ASTN D2382-76,
incorporated by
reference in Section 215.105.
e)
The emission rate of total organic compounds in the process
vent stream shall be calculated using the following
equation:
n
E=K
F
E
CIM1
i=1
Where:
E
=
Emission rate of total organic compounds
(minus
methane and ethane)
in the sample in kg/hr~-;
K
=
Constant 2.494 x l0~(1/ppm)
(mole/scm)
(kg/g)
(min/hr), where standard temperature for
(mole/scm)
is 20°C.L
Mi
=
Molecular weight of sample component
i
(g/mole)~
F
=
Vent stream flowrate (scm/mm),
at a standard
temperature of 20°C.
f)
The total vent stream concentration
(by volume)
of compounds
containing halogens
(ppmv,
by compound) shall be summed from
the individual concentrations of compounds containing
halogens which were measured by Reference Method 18.
(Source:
Amended at
Ill. Reg.
______,
effective
____________

365
Section 218.Appendix D
Coefficients for the Total Resource Effectiveness Index
(TRE)
Equation
This Appendix contains values for the total resource
effectiveness index
(TRE)
equation in Subpart V.
If a flow rate falls exactly on the boundary between the
indicated ranges, the operator shall use the row in which the
flow rate is maximum.
COEFFICIENTS FOR TRE EQUATION FOR CHLORINATED PROCESS
VENT STREAMS WITH
NET HEATING VALUE LESS
THAN
OR EQUAL TO 3.5 MJ/scm
FLOW RATE
(scm/mm)
Mm.
Max.
a
b
c
d
e
f
0.0
13.5
48.73
0.
0.404
—0.1632
0.
0.
13.5
700.
42.35
0.624
0.404
—0.1632
0.
0.0245
700.
1400.
84.38
0.678
0.404
—0.1632
0.
0.0346
1400.
2100.
126.41
0.712
0.404
—0.1632
0.
0.0424
2100.
2800.
168.44
0.747
0.404
—0.1632
0.
0.0490
2800.
3500.
210.47
0.758
0.404
—0.1632
0.
0.0548
COEFFICIENTS
FOR
TRE
EQUATION
FOR
CHLORINATED PROCESS
VENT
STREAMS
WITH
NET
HEATING
VALUE
GREATER
THAN
3.5
NJ/scm
FLOW
RATE
(scm/mm)
Mimi.
Max.
a
b
c
d
e
£
0.
13.5
47.76
0.
—0.292
0.
0.
0.
13.5
700.
41.58
0.605 —0.292
0.
0.
0.0245
700.
1400.
82.84
0.658 —0.292
0.
0.
0.0346
1400.
2100.
123.10
0.691 —0.292
0.
0.
0.0424
2100.
2800.
165.36
0.715
—0.292
0.
0.
0.0490
2800.
3500.
206.62
0.734
—0.292
0.
0.
0.0548
COEFFICIENTS
FOR TRE EQUATION
FOR NONCHLORINATED
PROCESS
VENT STREAMS WITH
NET
HEATING
VALUE
LESS
THAN
OR EQUAL TO 0.48
NJ/scm
FLOW RATE
(scm/mm)
Mm.
Max.
a
b
c
d
e
f
0.
13.5
19.05
0.
0.113
—0.214
0.
0.
13.5 1350.
.
16.61
0.239
0.113
—0.214
0.
0.0245
1350.
2700.
32.91
0.260
0.113
—0.214
0.
0.0346
2700.
4050.
49.21
0.273
0.113
—0.214
0.
0.0424

366
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS
VENT STREAMS
WITH NET HEATING VALUE GREATER
THAN
0.48 AND LESS
THAN
OR
EQUAL TO 1.9 NJ/scm
FLOW RATE
(scm
/
mm)
Mimi.
Max.
a
b
c
d
e
f
0.
13.5
19.74
0.
0.400
—0.202
0.
0.
13.5
1350.
18.30
0.138
0.400
—0.202
0.
0.0245
1350.
2700.
36.28
0.150
0.400
—0.202
0.
0.0346
2700.
4050.
54.26
0.158
0.400
—0.202
0.
0.0424
COEFFICIENTS
FOR
TRE
EQUATION
FOR
NONCHLORINATED
PROCESS
VENT
STREAMS
WITH NET HEATING VALUE GREATER
THAN
1.9 AND LESS
THAN
OR
EQUAL TO 3.6
NJ/scm
FLOW
RATE
(scm
/
mm)
Mm.
Max.
a
b
c
d
e
f
.0
13.5
15.24
0.
0.033
0.
0.
0.
13.5 1190.
13.63
0.157
0.033
0.
0.
0.0245
1190.
2380.
26.95
0.171
0.033
0.
0.
0.0346
2380.
3570.
40.27
0.179
0.033
0.
0.
0.0424
COEFFICIENTS
FOR TRE EQUATION
FOR NONCHLORINATED
PROCESS
VENT STREAMS WITH
NET HEATING VALUE GREATER
THAN
3.6 MG/scm
FLOW RATE
(scm/mimi)
Mimi.
Max.
a
b
c
d
e
f
0.
13.5
15.24
0.
0.
0.0090
0.
0.
13.5
1190.
13.63
0.
0.
0.0090
0.0503
0.0245
1190.
2380.
26.95
0.
0.
0.0090
0.0546
0.0346
2380.
3570.
40.27
0.
0.
0.0090
0.0573
0.0424
(Source:
Amended at
Ill.
Reg.
______,
effective
)

367
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE
B:
AIR POLLUTION
CHAPTER
I:
POLLUTION
CONTROL BOARD
SUBCHAPTER
C:
EMISSIONS
STANDARDS
AND
LIMITATIONS
FOR
STATIONARY
SOURCES
PART 219
ORGANIC MATERIAL EMISSION STANDARDS AND LIMITATIONS
FOR METRO EAST AREA
SUBPART A:
GENERAL
PROVISIONS
Section
219.100
219. 101
219.102
219.103
219.104
219. 105
219. 106
219.107
219.108
219.109
219.110
219.111
219.112
219.113
Introduction
Clcan—up and Disposal OperationSavings Clause
Abbreviations and Conversion Factors
Applicability
Definitions
Test Methods and Procedures
Compliance Dates
Operation of Afterburners
Exemptions, Variations, and Alternative Means of
Control or Compliance Determinations
Vapor Pressure of Volatile Organic Liquids
Vapor Pressure of Organic Material or Solvent
Vapor Pressure of Volatile Organic Material
Incorporations by Reference
Monitoring for Negligibly-Reactive Compounds
SUBPART
B:
ORGANIC EMISSIONS
FROM STORAGE
AND
LOADING OPERATIONS
SUBPART C:
ORGANIC EMISSIONS
FROM
MISCELLANEOUS EQUIPMENT
Section
219.141
219.142
219.143
219. 144
Separation Operations
Pumps and Compressors
Vapor Blowdown
Safety Relief Valves
SUBPART E:
SOLVENT CLEANING
Solvent Cleaning in General
Cold Cleaning
Section
219. 121
219.122
219.123
219.124
219.125
219.126
Storage Containers
Loading Operations
Petroleum Liquid Storage Tanks
External Floating Roofs
Compliance Dates
(Repealed)
Compliance Plan
(Repealed)
Section
219.181
219.182

368
219.183
219.184
219. 185
219.186
Section
219.204
219.205
219.206
219.207
219.208
219.209
219.210
219.211
SUBPART
Section
219.421
219.422
219.423
219.424
219.425
219.426
219.427
219.428
219.429
219.430
Open Top Vapor Degreasing
Conveyorized Degreasing
Compliance Schedule
(Repealed~L
Test Methods
SUBPART F:
COATING OPERATIONS
Emission Limitations for Manufacturing r~lant~
Daily-Weighted Average Limitations
Solids Basis Calculation
Alternative Emission Limitations
Exemptions From Emission Limitations
Exemption From General Rule on Use of Organic Material
Compliance Schedule
Recordkeeping and Reporting
SUBPART G:
USE OF ORGANIC MATERIAL
Use of Organic Material
Alternative Standard
Fuel Combustion Emission gource-oUnits
Operations with Compliance Program
SUBPART H:
PRINTING
AND
PUBLISHING
Flexographic and Rotogravure Printing
Applicability
Compliance Schedule
Recordkeeping and Reporting
Heatset-Web-Offset Lithographic Printing
Q:
LEAKS FROM SYNTHETIC ORGANIC CHEMICAL AND POLYMER
MANUFACTURING EQUIPMENT PLANT
General Requirements
Inspection Program Plan for Leaks
Inspection Program for Leaks
Repairing Leaks
Recordkeeping for Leaks
Report for Leaks
Alternative Program for Leaks
Open-Ended Valves
Standards for Control Devices
Compliance Date
(Repealed)
Section
219. 301
219.302
219.303
219.304
Section
219.401
219.402
219.403
219.404
219.405

369
SUBPART
R:
PETROLEUM
REFINING
AND
RELATED
INDUSTRIES;
ASPHALT MATERIALS
Section
219.441
219.442
219.443
219.444
219.445
219.446
219.447
219.448
219.449
219.450
219.451
219.452
219.453
Petroleum Refinery Waste Gas Disposal
Vacuum Producing Systems
Wastewater
(Oil/Water)
Separator
Process Unit Turnarounds
Leaks:
General Requirements
Monitoring Program Plan for Leaks
Monitoring Program for Leaks
Recordkeeping for Leaks
Reporting for Leaks
Alternative Program for Leaks
Sealing Device Requirements
Compliance Schedule for Leaks
Compliance Dates
(Repealed)
Section
219.480
219.481
SUBPART
5:
RUBBER AND MISCELLANEOUS
PLASTIC PRODUCTS
Manufacture of Pneumatic Rubber Tires
Green Tire Spraying Operations
Alternative Emission Reduction Systems
Tccting and MonitoringEmission Testing
Compliance Dates
(Repealed)
Compliance Plan
(Repealed)
SUBPART T:
PHARMACEUTICAL MANUFACTURING
Applicability
-
Control of Reactors, Distillation Units,
Crystallizers,
Centrifuges and Vacuum Dryers
219.482
Control of Air Dryers, Production Equipment Exhaust
Systems and Filters
219.483
Material Storage and Transfer
219.484
In-Process Tanks
219.485
Leaks
219.486
Other Emission Courcec Units
219.487
Testing
219.488
Monitoring and Rcoordkccping for Air Pollution Control
Equipment
219.489
Recordkeeping for Air Pollution Control Equipment
SUBPART V:
AIR OXIDATION PROCESSES
Section
219.521
219.525
219.526
219.527
Definitions
(Repealed)
Emission Limitations for Air Oxidation Processes
Testing and Monitoring
Compliance Date
(Repealed)
Section
219.461
219.462
219.463
219.464
219.465
219.466

370
SUBPART
W:
AGRICULTURE
Section
219.541
Pesticide Exception
SUBPART X:
CONSTRUCTION
Section
219.561
Architectural Coatings
219.562
Paving Operations
219.563
Cutback Asphalt
SUBPART Y:
GASOLINE DISTRIBUTION
Section
219.581
Bulk Gasoline Plants
219.582
Bulk Gasoline Terminals
219.583
Gasoline Dispensing Facilities
-
Storage Tank Filling
Operations
219.584
Gasoline Delivery Vessels
219.585
Gasoline Volatility Standards
219.586
Gasoline Dispensing Faciliticc Operations
-
Motor
Vehicle Fueling Operations
SUBPART Z:
DRY CLEANERS
Perchloroethylene Dry Cleaners
Exemptions
Leaks
Compliance Dates
(Repealed)
Compliance Plan (Repealed)
Exception to Compliance Plan
(Repealed)
Standards for Petroleum Solvent Dry Cleaners
Operating Practices for Petroleum Solvent Dry
Program for Inspection and Repair of Leaks
Testing and Monitoring
Exemption for Petroleum Solvent Dry Cleaners
Compliance Dates
(Repealed)
Compliance Plan
(Repealed)
SUBPART AA:
PAINT
AND
INK MANUFACTURING
Applicability
Exemption for Waterbase Material and Heatset-Offset Ink
Permit Conditions
Open-~IopMills,
Tanks, Vats or Vessels
Grinding Mills
Storage Tanks
Leaks
Clean Up
Section
219. 601
219.602
219.603
219.604
219.605
219.606
219.607
219.608
219.609
219.610
219.611
219.612
219.613
Section
219.620
219. 621
219.623
219.624
219.625
219.626
219.628
219.630
Cleaners

371
219.636
219.637
Section
219.640
219.642
219.644
219.875
219.877
219.879
219.881
219.883
219.886
Compliance Schedule
Recordkeeping and Reporting
SUBPART BB:
POLYSTYRENE PLANTS
Applicability of Subpart EB
Emissions Limitation at Polystyrene Plants
Emissions Testing
Applicability of Subpart BB
(Renumbered)
Emissions Limitation at Polystyrene Plants
(Renumbered)
Compliance Date
(Repealed)
Compliance Plan (Repealed)
Special Requirements for Compliance Plan
(Repealed)
Emissions Testing
(Renumbered)
SUBPART PP:
MISCELLANEOUS FABRICATED PRODUCT
MANUFACTURING PROCESSES
Section
219.920
219.923
219.926
219.927
219.928
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART
QQ:
MISCELLANEOUS
FORMULATION MANUFACTURING PROCESSES
Section
219.940
219.943
219.946
219.947
219.948
Section
219.960
219.963
219.966
219.967
219.968
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART RR:
MISCELLANEOUS
ORGANIC CHEMICAL
MANUFACTURING PROCESSES
Applicability
Permit Conditions
Control Requirements
Compliance Schedule
Testing
SUBPART TT:
OTHER EMISSION SOURCES UNITS
Applicability
Permit Conditions
Control Requirements
Section
219.980
219.983
219.986
219.987
Compliance Schedule

372
219.988
Testing
SUBPART UU:
RECORDKEEPING AND REPORTING FOR NON-CTC SOURCES
Section
219.990
Exempt Emission SouroccUnits
219.991
Subject Emission CourcccUnits
Section 219.Appendix A:
List of Chemicals Defining Synthetic
Organic Chemical and Polymer
Manufacturing
Section 219.Appendix B:
VOM Measurement Techniques for Capture
Efficiency
Section 219.Appendix C:
Reference Test Methods and Procedures
For Air Oxidation Processes
Section 219.Appendix D:
Coefficients for the Total Resource
Effectiveness Index
(TRE)
Equation
AUTHORITY:
Implementing Section
10 and authorized by Section
28.5 of the Environmental Protection Act
(Ill. Rev.
Stat.
1991,
ch.
111½, par.
1010)
(P.A.
87—1213, effective September 26,
1992)
415
ILCS 5/10 and 28.5.
SOURCE:
Adopted at R91-8
at 15
Ill.
Reg.
12491, effective August
16,
1991; amended in R9l—24 at
16
Ill. Reg.
13597, effective
August 24,
1992; amended
in R91—30 at 16 Ill.
Reg.
13883,
effective August 24,
1992; emergency amendment in R93-12 at Ill.
Reg.
8295,
effective May 24,
1993,
for a maximum of 150 days,
amended in
R93-9
at 17
Ill.
Reg.
______,
effective
______________
_____________
and October 21,
1993.
SUBPART A:
GENERAL PROVISIONS
Section 219.100
Introduction
a)
This Part contains standards and limitations for
emissions of organic material and volatile organic
material from stationary sources located
in the Metroz
-
East area, which is comprised of Madison, Monroe,
and
St. Clair Counties.
b)
Sources subject to this Part may be subject to the
following:
1)
Permits required under 35
Ill.
Adm. Code 201t
~
2)
Air quality standards under
35 Ill.
Adm. Code
c)
This Part is divided into Subparts which are grouped as
follows:

-
373
1)
Subpart A:
General Provisions~
2)
Subparts B-F:
Emissions from equipment and
operations
in common to more than one industry;
3)
Subpart G:
Emissions from use of organic
material;
4)
Subparts H-ei~4~:
Special rEules for various
industry groups.
~J
Subpart TT:
Rules for emission units not
otherwise addressed.
~j
Subpart UU:
Recordkeepina and reporting for
equipment and operation addressed by Subparts
PP.
00. RR and TT.
(Source:
Amended at
_____,
Ill. Reg.
_____,
effective
_________
____________________ )
Section 219.101
Cflr~mmri
ana uisposal OpcrationSavings Clause
Emission of organic material released during clean-up operations
and disposal shall be included with other emissions of organic
material from the related emission source or air pollution
control equipment in determining total emissions.
EverY owner or operator of an emission unit formerly subject to
35 Ill.
Adni.
Code 215 shall have complied- with its standards and
limitations by the dates and schedules applicable to the emission
unit in accordance with Part 215 or upon initial start-up.
All
compliance dates or schedules found
in Part 215 are not
superseded by this Part and remain in full force and effect.
(Source:
Section repealed, new Section added at
______
,
Ill.
Reg.
,
effective ______________________________________)
Section 219.102
Abbreviations and Conversion Factors
The following abbreviations arc uscu in cni~ii~urc:
ASTM
American Society for Testing and Materials
barrels
(42 gallon&)-
degrees Celsius or
~rnt,i~rnd~
em
centimeters
cu
in
cubic
inches
dr~circcs
Fahrenheit
r’cacral
Implcmcnta
feet
square feet

374
grams
~pm
-
gallons per
mi~~
g/mole
grams per mole
gallons
hours
inchcs
-~4c
degrees Kelvin
kcal
kilocalorics
kg
kilograms
kg/hr
kilograms
per
hour
kilopaseals; one thousand newton
meter
liters
1/sec
liters per second
pounds
lbs/hr
pounds
per
hour
lbs/gal
pounds per gallon
lower explosive
ii~i~
meters
square
meters
cubic
meters
milligrams
Mg
Mcgagrams,
metric tons or tonncs
milliliters
minutes
megajoules
mm Hg
millimeters of mercury
ppm
parts per million
ppmv
parts per million by volume
pounds per square inch
psia
pounds per square inch absolute
ps-ig
pounds per square inch gauge
ocf
standard cubic feet
scm
standard cubic meters
Sec
seconds
S~P
State
Implementation
Plan
TTE
temporary total enclosure
eq
cm
quare
centimeters
sq
in
square
manes
English ton
~en
English ton
UCEPA
United States Environmental Proc
~GG
volatile organic compounds
volatile organic liquids
volatile ~
materials
s-)-
The following conversion factors are used in this Part.
English
Metric
-1 gal
3.785
1
1,000 gal
3,7-85
1 or 3.785 m~

375
I ps-ia
6.897 kPa
(51.
2.205
lbs
1
kg
1
bbl
159.0
1
1 cu in
16.39 ml
-I- lb/gal
119,800
Thrill
I ton
0.907 Mg
0.907 Hg
The abbreviations and conversion factors of
35 Ill.
Adm. Code 211
apply to this Part.
(Source:
Amended at
____,
Ill. Reg.
____
effective
__________
Section 219.104
Definitions
The following terms are defined for
th-’
---~“
-~-~----~~
-~-~-
“Accelacota” means
a pharmaceutical coating operation
which consists of a horizontally rotating perforated
drum in which tablets are placed,
a coating is applied
by spraying, and the coating is dried by the flow of
ai-r across the drum through the perforations.
“Accumulator” means the reservoir of a condensing unit
receiving
the
condensate
from
a
surface
condenser.
iI,Acid Cases” means for the purposes of Section 9.4 of
the Environmental Protection Act
(the Act)
(Ill. Rev.
Stat.
1987,
oh.
111 1/2,
par. 1009.4), hydrogen
chloride, hydrogen fluoride and hydrogen bromide, which
exist as gases,
liquid mist,
or any combination
thereof.
“Actual emissions” means the actual quantity of VON
emissions from an emission source during a particular
time period.
“Actual Heat Input” means the quantity of heat produced
by the combustion of fuel using the gross heating value
of the fuel.
“Adhesive” means any substance or mixture of substances
fi~~
r~s—r~ii—’r~—~
r~
i—i ‘nri
r~rflnr~r~l1’flri
-
“Afterburner” means a control device in which materials
in gaseous effluent are combusted.
“Air contaminant” means any solid,
liquid,
or gaseous
matter,
any odor,
or any form
of
energy,
that is
capable of being released into the atmosphere from an
t~Th’!~~1
r~r~
~~r~rr~r’

376
“-Air dried coatings” means any coatings that dry by use
of
air
or forced air at temperatures up to
363.15~K
(194°F)
.
“Air
pollution”—
.•.~.....
-~
~.
~
th....
one or more air contaminants in sufficient quantities
and of such characteristics- and duration as to be
injurious- to human, plant,
or animal life,
to health,
or to property,
or to unreasonably interfere with the
enjoyment of life or property.
“Air pollution control equipment”
means- any equipment
or facility of
a type intended to eliminate, prevent,
reduce or control the emission of specified air
contaminants to the atmosphere.
“Air suspension copter/dryer” means a pharmaceutical
~-~tinn
t~hi~h
~
~f
~rt,i~1
chambers
in which tablets or
is applied and then
particles are placed,
and a coating
dried while the tablets or
in a fluidized state by the passage
particles are kept
of air upward through the chambers.
atmosohcr-’
rif
1
-~-~~-“
-~-~--
method
in which
~fl-rflnF,
“Air
~
the coating is atomized by forcing it
opening at high pressure. The coating liquid
is not
mixed with air before exiting from the nozzle.
1
~
means
~
method which combines compressed air with hydraulic
pressure to atomize the coating material into finer
droplets- than is achieved with pure airless spray.
Lower hydraulic pressure
is-
us-cd than with airless
s-pray.
“Allowable
emissions”
means
the
quantity
of
VON
emissions during
a particular time period from a
stationary source calculated using the maximum rated
capacity of the source (unless restricted by federally
enforceable limitations on operating rate,
hours of
operation,
or both)
and the most stringent of:
the
applicable standards in 40 CFR Parts 60 and 61;
the
applicable implementation plan;
or a federally
enforceable permit.
“Ambient air quality standards’1 means those standards
designed to protect the public health and welfare
codified in
40 CFR Part 50 and promulgated from time to
t~mi-
by
thr.
TTF1~P7~
-~imt-
tn
mthnrity
r~nntrrint~’r1In
~.1
~
Section 108 of the Clean Air Act,
42 U.S.C.
7401 et
~
~imc~ndn~d
from
tiimr
to
time
,
Lac,

377
~Applicator” means a device
us-ed in
a
coating
line
to
apply coating.
“As applied” means the exact formulation of a coating
during application on or impregnation into a substrate.
“Architectural Coating” means any coating us-ed for
residential or commercial buildings- or their
appurtenances,
or for industrial buildings-,
which is
site
1r~ri1ir’r1~
“Asphalt” means the dark-brown to black cementitious
material
(solid,
s-crni~olid,
or
liquid
in
consistency)
Ui. wiiiuu
LU~
~uUin oonL.T...iLuents ~.i.rc
~.~tumen~
WI1.LUJ1
oueur
~-aturallyor
as- a residue of petroleum refining.
“Asphalt
Prime
Coat”
means a low-viscosity liquid
-
asphalt applied to an absorbent surface as the first of
more than one asphalt coat.
“Automobile” means
a motor vehicle capable of carrying
no more than 12
passengers-.
“Automobile or light duty truck assembly plant” means a
facility where parts are assembled or finished for
eventual inclusion into a finished automobile or
light-duty truck ready for
s-ale to vehicle dealers-, but
not including customizers-, body chops,
and other
r-epaintcrs-.
“Automobile or light-duty truck refinishing” means the
~-cpaintingof used automobil~and light-du~1trucks.
dried in an o
90°C (194°F).
“-Batch
Loading”
means
the
process
of
loading
a
number
of
individual
parts-
at
the
same
time
for
dcgreasing.
“Bead-Dipping” means
the
dipping
of
an assembled tire
bead into a solvent—based cement.
11-Bindcrs” means- organic materials and resins which do
n-ct contain VON.
“Bituminous
coatings-”
means black or brownish coating
m-aterials-
which
are
soluble
in
carbon
dis-ulfidc,
which
consist mainly of hydrocarbons,
and which are obtained
from natural dcposits- or as res-idues from the
~-
“P.n1r~
coatings”
means
any
coating
uh~h i~
where the
p
-~
.-.4- 4 ~lI
4

378
“British
Thermal
Unit”
means
the
quantity
of
heat
required
to
raise
one
pound
of
water
from
60°F
to
61°F
~(a-bbreviated
btu)—~-
“Brush
or
wipe
coating”
means
a manual method
-of
applying a coating using a brush,
cloth,
or similar object.
~
gasoline
plant”
means
a
gasoline
storage anu
distribution
facility
with
an average throughput of
76,000
1
(20,000
gal)
or
less- on a 30—day rolling
average that distributes gasoline to gasoline
dispensing facilities-.
•~jjçLa~omineTerminam~means- any gasoline ~coragc anu
distribution facility that receives gasoline by
pipeline,
s-hip or barge,
and distributes gasoline to
bulk gasoline plants- or gasoline dispensing facilities.
“Can”
means- any metal container,
with or without a top,
cover,
spout or handles-, into which solid or liquid
materials- are
packaged.
“Can coating” means any coating applied on a single
walled container that is manufactured from metal sheets
~
~
irt
t~1A1
4~...
“Can coating
means a facility that includes one
ting line(s).
or
more
can coa
“Cpn coating line” means a coating line in which any
protective, decorative,
or functional coating is
applied onto the surface of cans or can components.
of
collecting
-so-lven-t
oth~
a duct.
The pollutant can then be
Ilution control device such as an
afterburner or carbon ads-orber.
Sometimes- the term is
used loosely to include the control device.
i-on
of all VON
-
“Capture” means the containment or recovery o#
emissions from a process for direction into a duct
which may be exhausted through a stack or vent to a
control device.
The overall abatement of emissions
from a process with an add-on control device
is- a
function both of the capture efficiency and of the
control device.
“Capture device” means
a hood.
enclosed room floor
~w-eco
or
other
~
into
generated
byaprocess
that
are
dircotca
abatement or recovery device.
-

379
“Capture system” means- all equipment
(including, but
not limited to,
hoods, ducts,
fans,
ovens-,
dryers,
etc.)
us-cd
to
contain,
collect
and
transport
an
air
pollutant to a control device.
“Clean Air Act” means the Clean Air Act of 1963,
as
amended,
including the Clean Air Act Amendments of
1977,
(42 U.S.C.
7401 et s-eq.), and the Clean Air Act
Amendments of 1990,
(P.L.
101-549).
“Clear coating” means coatings that lack color and
opacity or are transparent using the undercoat as a
reflectant base or undertone color.
“Clear topcoat” means the final coating which contains
binders,
but not opaque pigments,
and is specifically
formulated to form a transparent or translucent solid
protective film.
“Closed Purge System” means a system that is not open
to the atmosphere and that is composed of piping,
connections-,
and,
if necessary,
flow inducing devices
that transport liquid or vapor from a piece or pieces
of equipment to a control device,
or return the liquid
or vapor to the process- line.
“Closed vent system” means
a system that is not open to
the atmosphere and
is- composed of piping, connections,
and,
if necessary,
flow inducing devices that transport
gas or vapor from an emission source to
a control
device.
“Coating” means
a material applied onto or impregnated
into a substrate for protective,
decorative,
or
functional purposes. Such materials includc, but are
not limited to,
paints,
varnishes-,sealers-, adhesives,
thinners, diluents, and
inks-.
“Coating applicator” means equipment us-cd to apply a
coating.
-fl-Coating line” means
an operation consisting of a
series of one or more coating applicators- and any
associated flash—off areas, drying areas,
and ovens
wherein a surface coating is applied, dried,
or cured.
(It
is not necessary for an operation to have an oven,
or flash—off area,
or drying area to be included in
this- definition.)
“Coating plant” means any plant that contains- one or
more coating line(s).

380
“Coil” means any flat metal sheet or strip that is
rolled or wound in concentric rings.
“-Coil coating” means- any coating applied on any flat
metal sheet or strip that comes in rolls- or -coils.
“Coil coating facility” means-
a facility that includes
one
or
more
coil
coating
line(s).
ucoil
coating
line”
means-
a
coating
line
in
which
any
protective,
decorative
or
functional
coating
is-
applied
onto
the
surface
of
flat
metal
sheets,
strips-,
rolls-,
or
coils
for
industrial
or
commercial
use.
“Cold cleaning” means- the
process-
of
cleaning
and
removing soils from ~urfaccs-by s-praying,
brushing,
flushing,
or immersion while maintaining the organic
solvent below
its- boiling point.
Wipe cleaning is not
included
in this definition.
“Complete Combustion” means a process in which all
carbon contained in a fuel or gas stream is converted
to carbon dioxide.
“Component” means, with respect to synthetic organic
chemical and polymer manufacturing equipment,
and
petroleum refining and related industries,
any piece of
equipment which
has- the potential to leak VON
including, but not limited to, pump seals-, compress-or
seals,
seal oil degas-sing vents, pipeline valves,
pressure relief devices, process drains,
and open ended
pipes.
This- definition excludes valves- which are not
externally regulated,
flanges-, and equipment in heavy
liquid service.
For purposes- of Subpart Q of
this-
Part, this definition also excludes bleed ports of gear
pumps in polymer service.
“Concrete curing compounds” means any coating applied
to freshly poured concrete to retard the evaporation of
water.
“Condensate” means volatile organic liquid separated
from
its- associated gases, which condenses due to
changes in the temperature or pressure and remains-
liquid at standard conditions-.
“Continuous- process” means-, with respect to polystyrene
rt~in
~
mc’thnsl
nf
m
iif~-~r~ti,rr in
uhir~h
thr’
-‘tyrenc ~
material
is delivered on
a continuous basis to the
reactor in which the styrcnc
is- polymerizcd to
polystyrene.

4—.,—.-.
.—.~
*
381
“Control device” means equipment
(such as an
afterburner or adsorber) used to remove or prevent the
emission of air pollutants from a contaminated exhaust
stream.
“Control device efficiency” means- the ratio of the
pollution prevented by a control device and the
pollution introduced to the control device,
express-cd
as- a percentage.
“Conveyorizcd dcgreasing” means the continuous process
of cleaning and removing soils from surfaces utilizing
either cold or vaporized solvents.
ni
1
~
m--~n
r~—rt-nri1
ly
nr~r~nrri
m
i
yturr’
wh
i
r~h
cons-~~
nyarocarnons-
and
sulfur,
nitrogen,
oxygen derivatives of hydrocarbons and which is a
liquid at standard conditions.
“Crude
oil
gathering”
means
the
transportation
of
crude
oil or condensate after custody transfer between a
production facility and a reception point.
“Custody transfer” means the transfer of produced
petroleum and/or condensate after processing and/or
treating in the producing operations,
from storage
tanks- or automatic transfer facilities to pipelines or
any other forms of transportation.
11-Cutback
Asphalt”
means
any
asphalt
which
has
been
liquified
by
blending
with
petroleum
solvents
other
than
residual
fuel
oil
and
has
not
been
emulsified
with
water.
“Daily-weighted
average
VON
content”
means
the
average
VON
content
of
two
or
more
coatings
as-
applied
on
a
coating
line
during
any
day,
taking
into
account
the
fraction
of
total
coating
volume
that
each
coating
represents-,
as- calculated with the following equation:
E
V1—G~
i/vT
i
—1
where:
The
average
VON
content
of
two
or
more
coatings
as
applied
each
day
on
a
coating
line
in
units
of
kg
VON/i
(lbs
VON/gal)
of
coating
(minus
water
and
-any

382
compounds-
which
arc
specifically
exempted
from
the
definition
of
VON),
inc
rium~er or
aiffcrcnt
coatings-
as-
applied
each
day
on
a
coating
line,
The
volume
of
each
coating
~mmnus
waL.cr
ana
any
compounds
which
arc
specifically
exempted
from
the
definition
of
VON)
applied each day on a coating line in
units
of
1
(gal).
inc
vur~icontent
ci.
eacn
coa~1r~r~
as
applied
each
day
on
a
coating
line
in
units
of
kg
VON/l
(lbs
VON/gal)
of
coai.~ing
tmmnu~ water
and
any
compounds
which
are
specifically
exempted
from
the
fir~ifinr~
nf
1JnM\
The -total
volume
of
all
coatings
(minus-
water
and
~nv
compounds
which
arc
s-pccmricaiiy
exempted
from
tnc
definition
of
VON)
as-
applied
each
day
on
a
coating
line
in
units-
of
1
(gal).
“Day”
means
the
consecutive
24
hours-
beginning
at
12:00
AN
(midnight)
local
time.
-
“Dcgreascr” means any equipment or system used in
solvent
cleaning.
“Delivery
vessel”
means-
any
tank
truck
or
trailer
equipped
with
a
storage
tank
that
is-
used
for
the
transport
of
gas-oil-nc
to
a
stationary
storage
tank
at
a
gasoline
di-spensing
facility,
bulk
gasoline
plant,
or
bulk
gasoline
terminal.
“Dip
coating”
means-
a
method
of
applying
coatings
in
which
the
n~rt
is
subme-rnied
in
a
tank
filled
with
the
coating.
“Distillate
Fuel
Oil”
means
fuel
oils-
of
grade
No.
1
or
2
.~ospecified in detailed requirement
for
fu~1nil
D—369—69
(1971).
“Dry Cleaning Facility” means a facility engaged in the
cleaning
of
fabrics-
using
an
essentially
nonaqueous-
solvent
by
means
of
one
or
more
solvent
washes,
extraction
of
excess
solvent
by
spinning
and
drying
by
tumbling in an airstreain.
The facility includes, but

is
not
limited
to,
was-hers-,
dryers-,
filter
and
purification
systems,
waste
disposal
systems,
holding
tanks-,
pumps
and
attendant
piping
and
valves.
“Effluent
Water
Separator”
means-
any
tank,
box,
sump
or
other
apparatus-
in
which
any
organic
material
floating
on
or
entrained
or
contained
in
i~ator
t~nterincc
ouch
...,
~
.~~rc~tusis-
phyolcaily
“Electrostatic
bell
or
disc
spray”
means
an
electrostatic
spray
coating
method
in
which
a
rapidly-spinning
bell-
or
disc-shaped
applicator
is
us-cd
to
create
a
fine
mist
and
apply
the
coating
with
high
transfer
efficiency.
“Electrostatic
spray”
means-
a
s-pray
coating
method
in
which
opposite
e1nr~t-r4r--~1
r~huirir~i
irr~
~rir~1ir~d
tn
thr’
3-
-_3-
-~
-
-I- 1-.
coating.
The coating is attracted to
the
object
due
to
the
electrostatic
potential
between
them.
“Emission Rate” means total quantity of any air
contaminant discharge into the atmosphere in any
period.
“Emission
source”
and
“source”
mean any facility from
which VON
is
emitted
or
capable
of
being
emitted
into
the
atmosphere.
“Enamel”
means-
a
coating
that
cures
by
chemical
cross—linking
of its base resin.
Enamels can
b-c
distinguished
from
lacquers-
because
enamels-
arc
not
readily
resoluble
in
their
original
solvent.
“Enclose”
means
to
cover
any
VOL
surface
that
is
exposed
to
the
atmosphere.
-“-End
scaling
compound
coat”
means
a
compound
applied
tc
can
ends
which
functions
as
a
gasket
when
the
end—i-s
.a
~SLtMS
~
~Z
L ~
~1
£
--~cess
i~ir”
means
air
supplied
in
addition
to
the
theoretical
quantity
necessary
for
complete
combustion
of
all
fuel
and/or
combustible
waste
material.
“Excessive
release”
means-
a
discharge
of
more
than
295
g
(0.65 lbs)
of mercaptans- and/or hydrogen sulfide into
~he
atmosphere
in
any
5-minute
period.
383
tank,
bc
-~r~
-
,t
r’.

..
e,_
~
-—
-.
——
384
exterior of aeon
body,
or flat
shcet
to
provide
protection to
the
metal
or
to
provide
background
for
any
lithographic
or
printing
operation.
JlExtcrior
end
coat”
means
a
coating
applied
to
the
‘~-~-‘--
-‘-~-1
of
a
can
to
provide
protection
to
t-hr’
metal.
“External
floating
roof”
means
a
cover
over
an
open
top
storage
tank
consisting
of
a
double
deck
or
pontoon
cingle
deck
which
rests-
upon
and
is
supported
by
the
volatile
organic
liquid
being
contained
and
is
equipped
with a closure s-cal or
seals
to
close
the
space
between
the
roof
edge
and
tank
s-hell.
“Extreme
environmental
conditions”
means
exposure
to
any
or
all
of
the
following:
ambient
weather
conditions;
temperatures
cons-is-tently
above
95°C
+203°F);
detergents;
abrasive
and
scouring
agents;
~o1
~rr’r~t
or
r~nrrn’~ii~n
~rm
r-~nr’rn-
“Extreme
performance
during
intended
us-c
coating”
is
exposed
means
any
coating
which
to
extreme
environmental
condi
ti
on~
-
1-Fabric
coating”
means-
any
coating
applied
on
textile
-fabric-—-—--F-abric coating
includes
the
application
of
coatings
-by
impregnation.
“Fabric
coating
facility”
means
a
facility
that
includes
one
or
more
fabric
coating
lines.
“Fabric
coating
line”
means-
a
coating
line
in
which
any
protective,
decorative,
or
functional
coating
or
reinforcing
material
is-
applied
on
or
impregnated
into
a
texti-1-c fabric.
-
“Federally
enforceable”
means
all
limitations
and
conditions-
which
arc
enforceable
by
the
Administrator
including
those
requirements
developed
pursuant
to
40
CFR
Parts
60
and
61;
requirements
within
any
applicable
implementation
plan;
and
any
permit
requirements
established
pursuant
to
40
CFR
52.21
or
under
regulations
approved
pursuant
to
40
CFR
Part
51
Subpart
I-and
-40
CFR
51.166.
“-Final repair coat”
means- the repainting of any topcoat
which
is
damaged
during
vehicle
assembly.

385
“Fircbox”
means-
the
chamber
or
compartment
of
a
boiler
or
furnace
in
which
materials
are
burned,
but
not
the
combustion
chamber
or
afterburner
of
an
incinerator.
“Fixed-roof
tank”
means
a
cylindrical
shell
with
a
permanently
affixed
roof.
“Flexographic
printing”
means
the
application
of
words,
designs,
and
pictures-
to
a
substrate
by
means
of
a
roll
printing
technique
in
which
the
pattern
to
be
applied
is
raised
above
the
printing
roll
and
the
image
carrier
is-
made
of
elas-tomcric
materials-.
“Flexographic
printing
line”
means-
a
printing
line
in
which
each
roll
printer
uses
a
roll
with
raised
areas
for
applying
an
image
such
as-
words,
designs,
or
pictures-
to
a
substrate.
The
image- carrier
on
the
roll
is
made
of
rubber
or
other
elas-tomeric
material.
“Floating
roof”
means-
a
roof
on
a
stationary
tank,
reservoir,
or
other
container
which
moves
vertically
upon
change
in
volume
of
the
stored
material.
“Fountain
solution”
means
the
solution
which
is
applied
to
the
image
plate
to
maintain
hydrophilic
properties
of
the
non—image
areas-.
“Freeboard
Height”
means-
for
open
top
vapor
degreasers,
the
distance
from
the
top
of
the
vapor
zone
to
the
top
of the degreaser tank.
For cold cleaning degreascrs-,
the distance from the solvent to the top of the
degrcascr
tank-.-
“Fuel
combustion
emission
source”
means-
any
furnace,
boiler,
or
similar
equipment
us-ed
for
the
primary
purpose of producing heat or power by indirect heat
transfer-.-
“Fuel
gas-
system”
means
a
system
for
collection
of
refinery
fuel
gas-
including,
but
not
limited
to,
piping
for
collecting
tail
gas
from
various
process-
units-,
mixing
drums-
and
controls-,
and
distribution
piping.
“Gas-
service”
means
that
the
component
contains
process-
fluid
that
is
in
the
gaseous
s-tate
at
operating
conditions-.
“Gas/gas
method”
means
either
of
two
methods
for
determining
capture
which
rely
only
on
gas-
phase
measurements.
The
first
method
requires-
construction
of
a temporary total enclosure
(TTE)
to ensure that all
would-be
fugitive
emissions-
arc
measured.
The
second

386
the
building
.ious-cc
the
facility as an enclosure.
The second method requii~
that all other VON sources- within the room be
s-hut
down
while the test
within
the
room
is- performed, but
must
be
operated
all
fans
according
and
to
blowers
normal
procedures-.
“Gasoline”
means
any
petroleum
distillate
or
petroleum
dl-Gtillate/alcohol blend having a Reid vapor pressure
of
27.6
kPa
or
greater
which
is-
used
as-
a
fuel
for
internal
combustion
engines-.
~Cas-oline
dispensing
facility”
means-
any
site
where
gasoline
is
transferred
from
a
stationary
storage
tank
to
a
motor
vehicle
gasoline
tank
used
to
provide
fuel
to
the
engine
of
that
motor
vehicle.
“Green
Tire
Spraying”
means-
the
spraying
of
green
tires,
both
ins-ide
and
outside,
with
rele~e
cnmnounci~
which
hel
n
remove
~
i
r
from
the
tire
dun
nn
mu
_-.~
~:ldin-~
4
-
~4-
~-s
-.*. —~
1 ~
~—_~ -s..
-~—
prevent the tire from sticking to
“Green
Tires-”
means-
assembled
tireo
before
molding
and
curing
have
occurred.
-“-Gross-
vehicle
weight”
means-
the
manufacturer’s
gross
weight
rating
for
the
individual
vehicle.
“Gross vehicle weight rating”
means- the value specified
by the manufacturer
as- the maximum design loaded weight
of
a
single
vehicle.
“Heated airless s-pray” means an airless spray coating
method
in
which
the
coating
is-
heated
just
prior
to
application.
-
-“H-cat-set” means
a
class
of
web-offset
lithography
which
requires
a
heated
dryer
to
solidify
the
printing
inks.
“Heatsct-web-off
set
lithographic
printing
line”
means-
a
lithographic
printing
line
in
which
a
blanket
cylind-er
is
us-ed to transfer ink from a plate cylinder to
a
substrate
continuously
fed
from
a
roll
or
an
extension
process and an oven is used to solidify the printing
inks-.
“Heavy
liquid”
means
liquid
with
a
true
vapor
pressure
of
less- than 0.3
kPa
(0.04
psi)
~t
2fl~-.~°T~(7fl°F~
determined
by
AETH
method
D2379-86
(incorporated
by
reference
in
Section
219.112);
Vapor Pressure as determined by
or
which
has-
ASTM method
0.1
Reid
D323—82
r~ nn

387
(incorporated
by
reference
in
Section
219.112);
or
which
when
distilled
requires
a
temperature
of
421.95°K
-(-300°F) or greater to recover 10 percent of the liquid
as
determined
by
ASTM
method
D06-82
(incorporated
by
reference
in
Section
219.112).
“Heavy
off-highway
vehicle
products-”
means,
for
the
purpose
of
Subpart
F
of
this
Part,
heavy
construction,
mining,
farming,
or
material
handling
equipment;
heavy
~industrial
engines-i
diesel-electric
locomotives
and
associated
power
equipment;
and
the
components
of
such
equipment
or
engines.
“Heavy
off-highway
vehicle
products
coating
facility”
means
a
facility
that
includes
one
or
more
heavy
off-highway
vehicle
products
coating
line(s).
“Heavy
off—highway
vehicle
products-
coating
line”
means
a
coating
line
in
which
any
protective,
decorative,
or
functional
coating
is
applied
onto
the
surface
of
heavy
off-highway
vehicle
products-.
“High temperature aluminum coating” means- a coating
that
is-
certified
to
withstand
a
temperature
of
537.8°C
-(1000°F)
for
24
hours-.
-
“HoOd” means a
partial
enclosure or canopy for
capturing
and
exhausting,
by
means
of
a
draft,
the
organic
vapors
or
other
fumes
rising-from
a
coating
process
or
other
source.
1’Hood
capture
efficiency”
means-
the
emissions-
from
a
process
which
are
captured
by
the
hood
and
directed
into
a
control
dc-vice,
expressed
as
a
percentage
of
all
emissions-.
“Hot
well”
means
the
reservoir
of
a condensing unit
receiving
the
condensate
from
a
barometric
condenser.
“Hour”
means
a block period of
60
minutes
(e.g.,
1:00am
to
2:00am).
“In-process
tank”
means-
a
container
us-cd
for
mixing,
blending,
heating,
reacting, holding, crystallizing,
evaporating
or
cleaning
operations
in
the
manufacture
of pharmaceutical-s.
11~In—situ
Sampling
Systems”
means
nonextractive
samplers
or in-line samplers.
-
“-In
vacuum
service”
means,
for
the
purpose
of
Subpart
Q
of~this
Part,
equipment
which
is
operating
at
an

388
internal
pressure
that
is
at
least
5
.
kPa
(0.73
ps--ia)
below ambient pressure
“Incinerator”
means-
a
combustion
apparatus
in
which
refu—te
I
hurnc~-~i—~—
-
“Indirect
heat
transfer”
means
transfer
of
heat
in
such
a
way
that
the
source
of
heat
does
not
come
into
direct
contact
with
process
materials.
“Ink”
means
a
coating
us-ed
in
printing,
impressing,
or
transferring
an
image
onto
a
substrate.
“Interior
body
spray
coat”
means
a
coating
applied
by
-~-nr~vto
the
i nteni
on
of
~
e~n
hodv_
‘!Internal-floating
roof”
mea
fixed—roof
tank
which
rests
ns
a
cover
or
roof
in
upon
and
is
supported
a
by
the
volatile
organic
liquid
being
contained
and
is
equipped
with
a
closure
s-cal
or
seals-
to
close
the
s-pace
between
the
roof
edge
and
tank
shell.
“Lacquers”
means-
any
clear
wood
finishes
formulated
with
nitrocellulose
or
synthetic
resins
to
dry
by
evaporation
without
chemical
reaction,
including
clear
lacquer
sanding
scalers.
“Large
-appliance”
means
any
residential
and
commercial
was-hers,
-dryers,
ranges,
refrigerators-,
freezers,
water
heaters-,
dishwashers,
trash
compactors-,
air
conditioners,
and
other
similar
products.
“Large appliance coating” means any coating applied to
the component metal part2
(including, but not limited
to,
doors,
cases,
lids,
panels, and interior support
parts)
of
residential
and
commercial
was-hers,
dryers,
ranges,
refrigerators-,
freezers-,
water
heaters-,-
dishwashers-,
trash
compactors-,
air
conditioners-,
and
other
similar
products-.
“Large
appliance
coating
facility”
means
a
facility
that
includes-
one
or
more
large
appliance
coating
line(s).
“Large
appliance
coating
line”
means
a
coating
line
in
which
any
protective,
decorative,
or
functional
coating
-is
applied
onto
the
surface
c-f
large
appliances.
“Light
liquid”
means-
VON
in
the
liquid
state
which
is
not
defined
as
neavy
liquid.

“Light-duty
truck”
means
any
3_O~r~
k
gros-s
~—1~
~:cight
~.
~.ins-port
~
“Liquid/gas
method”
means-
either
of
two
methods-
for
determining
capture
which
require
both
-gas-
phase
and
liquid
phase
measurements
and
analysis.
The
first
method
requires-
construction
of
a—TTE.
The
second
method
us-cs the building or room which houses- the
facility
as- an enclosure.
The second method requires
that
all
other
VflM
~onnee
tjithin
the
room
he
hut
drn~n
wniie
tn~. test
is
performed,
but
all
fans-
and blowers
within
the
room
procedures-.
must
be
operated
according
to
normal
P.e-~l”
mr’-~r~-~
r~n4m~r’j
e~l
mounted
‘hi
conti..~~.
contact
with
the
liquid
between
the
tank
wall
and
the
floating
roof
edge
around
the
eireumfer~r~ee
of
the
roof.
“Liquid
service”
means
that
the
equipment
or
component
contains
process
fluid
that
is
in
a
liquid
state
at
operating conditions.
“-Liquids
Dripping”
means
any
visible
leaking
from
a
seal including spraying, misting, clouding and ice formation.
“Lithogrc~phic
printing
line”
means
a
printing
line,
except
that
the
substrate
is-
not
necessarily
fed
from
an
unwinding
roll,
in
which
each
roll
printer
uses
a
roll
where
both
the
image
and
non—image
areas
ar—e
essentially
in
the
same plane (planographic).
l1-T-~)bJ
2-.r~
.
-~
nri
~~71~b
1
n
~
1~~t---C~ting” m~ns
a
~
T~-e.
lvcnt
th~
the
conventic~-l
cc-i-~g~
used
by
the
industry.
Low
solvent
coatings-
include
w~ter—horne,
higher
solids,
electro—depooltion
rind
tings-.
ains
“Magnet
wire”
means-
aluminum
or
copper
wire
formed
into
an
electromagnetic
coil.
-“-Magnet wire coating” means any coating or electrically
insulating
varnish
or
enamel
applied
to
magnet
wire.
“Magnet
wire
coating
facility”
means
a
facility
that
includes
one
or
more
magnet
wire
coating
line(s).
“Nagnet wire coating line” means a coating line in
w’hich
any
protective,
decorative,
or
functional
coating
is
applied
onto
the surface of a magnet wire.
389
-I—
1_
I
or
less-,
designed
mainly

“Malfunction”
means
any
sudden
and
unavoidable
failure
of air pollution
control
equipment,
process
equipment,
or a process to operate in a normal or usual manner.
Failures
that
are
caused
entirely
or
in
part
by
poor
maintenance,
careless
operation,
or
any
other
preventable
upset
condition
-or
preventable
equipment
breakdown
shall
not
be
considered
malfunctions.
“Manufacturing
process”
means
a
method
whereby
a
~r-ru-~-~
i-~mi
n~i
on
~-~ii-r~
-
.
.r’r-i
~‘r~
of
proer’ir~
r’mi
~
or~
oources-
is
us-ca
to
raw
matc;ials-,
feed
stocks,
cubas-scmblies-,
or
other
components-
into
a
product,
either
for
sale
or
for
use
as-
a
component
in
a
subsequent
manufacturing
process-.
“Naterial
Recovery
Section”
means
any
equipment
designed
to
trans-port
and
recover
styrene
monomer
and
other
impurities
from
other
products
and
by-products-
in
a
poly-s-tyrene
plant,
including
but
not
limited
to
the
etyrenc dcvolatilizer unit and styrene recovery unit.
“Maximum theoretical
emissions-”
means
the
quantity
of
volatile
organic
material emissions that theoretically
could be emitted by a stationary source before add-on
eontrols based on the design capacity or
maximum
production capacity of the source and 8760 hours- per
year.
The design capacity or maximum production
capacity—i-ncludes use of coating(s)
or ink(s) with the
highes-t volatile organic material content actually used
-i-n practice by the source.
Provided, however, the
Agency shall,
when appropriate, and upon request by the
permit applicant,
limit the “maximum theoretical
emissions” of a source by the imposition of conditions-
in a federally enforceable operating permit for such
source.
Such conditions- shall not be inconsistent with
requirement of the Clean Air Act,
as amended,
or
any
applicable requirements- established by the Board.
Such
conditions shall be established in place of design
capacity or maximum production capacity in calculating
the “maximum theoretical emissions” for such source and
~ay include,
among other things, the establishment of
production limitations-, capacity limitations, emission
limitations-,
or limitations on the volatile organic
material content of coatings or
inks-,
or the hours of
eperation of any emission source,
or a combination of
any such limitations.
Producti-on or capacity limitations
s-hall be established
en
basis of no longer than one month except in those
cases where a limit s-panning a longer period of time is
appropriate.
In such cases,
a rolling limit” shall be
employed.
Any production or capacity limitations—shall
390

.~..
~
~
Notcz
The
US-EPA
may deem operating permits which do
net
conform
to
the
operating
pcrmit
program
requirementu
~1nu
LUC
rcguiremeiILu
Ui
~
underlying
regulations,
including
the
requirement
that
limitations
be
quantifiable
and
enforceable
as
a
practical
matter,
not
“federally
enforceable.”)
“Metal
furniture”
meano
a
furniture
piece
including,
but not limited to,
tables-,
chairs, waste baskets,
beds-,
desks,
lockers,
benches-, shelving, file cabinets,
-lamps,
and room dividers-.
“Metal
furniture
coating”
means
any
non—adhesive
coating
applied
to
any
furniture
piecc
made—of
metal or
any
metal
part
which
is
or
will
be
assembled
with
other
wooa,
~abric, plastic or glass
parts- to form
furniture piece including,
but
not
limited
to,
tables,
chairs,
waste
baskets,
beds,
des-ks,
lockers,
benches,
shelving,
file
cabinets,
lamps-,
and
room
dividers.
This
definition
shall
not
apply
to
any
coating
line
coating
miscellaneous-
metal
parts
or
products-.
“Metal
furniture
coating
facility”
means
a
facilisy
that
includes
one
or
more
metal
furniture
coating
line(s).
-
“-Metal
furniture
coating
line”
means
a
coating
line
in
which
any
protective,
decorative,
or
functional
coating
i-s
applied
onto
the
surface
of
metal
furniture.
“Nctaflic
shoe—type
s-eel”
means
a
primary
or
secondary
seal
constructed
of
metal
sheets
(shoes-)
which
are
-j-eined together to form
a ring,
springs,
or levers
which
attach
the
shoes
to
thc
floating
roof
and
hold
the
shoes
against
the
tank
wall,
and
a
coated
fabric
which
is
suspended
from
the
shoes
to
the
floating
roof.
3—
-
fabricated
pr
manufacturing
the
following
Qppl±~±~s-,
and
curing
f
formulations,
emitting
VON:
-~--.--~1
Adhesives
to
fabricate
or
Lble
components-
-
391
Asphalt
solutions
to

A
manufacturing
process-
which
more
of
the
following
and
is-
VON:
compounds-
one
or
apable
of
emitting
Adhesives
Asphalt
solutions
Caulks,
scalants,
Coatings, other t
Concrete
curing
c
Dyes-
Friction materiaL
Resin -solutions-
Rubber solutions
Vi
eo~e
waterproofing ag
paint and ink
-
392
Asphalt to paper or felt
Coatings
or
dye
to
leather
Coatings-
to
plastic
Coatings-
to
rubber
or
Disinfectant
mater1
‘-~1
Plastic foam s-crap
manufacture
of
foam
c~r
material to
f-arm
r-
--
Reoin
so1ution~i
tc~
f-I-
glass
to
manufactured
-i-t~r~s
“fluff”
~~j~--t~i:
ntainers
and
r~ackaging
in pallets
fiber s”~~
r n ri(~
UL.J~’ ~1E
or
,—---.-—-- ,‘—~-~
-vis-oo~c s--oiutions
icr
iooa
casings
s
and handling
formulations
iated
‘.iith
the
proc
-described
above,
and
~.seand handling of
~
liquids and
othei.
~tances-for—clean-up operations a~
es-s
The
st
as-soc
the
subs
uuoc1uLe~
w
i-_n
the process ucs-cri~cain tni~aciinition.
“Miscellaneous-
formulation
manufacturing
process”
means:
-

393
The
storage
and
handling
of
formulations-
associated
with
the
process
described
above,
and
the
use
and
handling
of
organic
liquids
and
other
substances
for
clean-up
operations
associated
with
tne
nnocess-
described
in
this-
“Miscellaneous
metal
parts
or
products”
means
any
metal
part
or
metal
product,
even
if
attached
to
or
combined
with
a
nonmetal
part
or
product,
except
cans,
coils-,
metal
furniture,
large
appliances,
magnet
wire-,
automobiles,
ships,
and
airplane
bodies.
“Miscellaneous
metal
parts
and
products
coating”
mean-s
any
coating
applied
to
any
metal
part
or metal product,
even
if
attached
to
or
combined
with
a
nonmetal
part
or
product,
except cans,
coils, metal furniture,
large
appliances,
and magnet wire.
Prime coat,
prime
surfacer
coat,
topcoat,
and
final
repair
coat
for
automobiles
and light duty trucks are not miscellaneous
metal
parts
and
products
coatings.
However,
underbody
anti-chip
(e.g.,
underbody
plas-tis-ol)
automobile
and
light-duty
truck
coatings
arc miscellaneous metal parts
and
products
coatings.
Also,
automobile
or
light-duty
truck
refinishing
coatings,
coatings
applied
to
the
exterior
of
marine
vessels,
coatings-
applied
to
the
exterior
of
airplanes,
and
the
customized
topcoating
of
automobiles and trucks if
production
is
less
than
35
vehicles per day are not miscellaneous metal parts and
products
coatings.
“Miscellaneous
metal
parts-
or
products
coating
facility”
means
a
facility
that
includes
one
or
more
miscellaneous
metal
parts-
or
products
coating
lines.
“Miscellaneous metal parts
or products coating line”
means a coating line in which any protective,
decorative,
or functional coating
is- applied onto the
surface
of
miscellaneous
metal
parts
or
products.
“Miscellaneous-
organic
chemical
manufacturing
process”
means-:
A
manufacturing
process
which
produces-,
by
chemical reaction, one or more of the following
organic compounds or mixtures of organic compounds-
and which is capable of emitting VON:
Chemicals listed in Appendix A of this Part
d—s-ulfonated compounds

394
Di
~infeetrint~
orapecialtico
and
products-
Food additives
Oil
and
petroleum
product
additives-
4
Rubber additives
Sweeteners
Varnishes-
associated
with
the
process-
described
above
and
the
use
and
handling
of
organic
liquids
and
other
substances-
for
clean-up
operations
associated
with
the
process
described
in
this
definition.
tsr” means to measure ana rccora.
“Multiple
package
coating”
means-
a
coating
made
from
more
than
one
different
ingredient
which
must
be
mixed
nnion
to
uinn
mn
hm’~
ri
1
irnltei-1
not
life
due
to
the
chemical reaction which
mixi~
means a discharge of volatile organic material into the
atmosphere as indicated by an instrument reading of
less than 500 ppm above background as determined in
accordance with 40 CFR 60.485(c).
“Offset” means, with respect to printing and publishing
blanket
cyli~r’n
to
t~r~fr-r
mit
from the plate cylind~ to the
~
to be ~inted.
“Opaque
stains”
means-
all stains- that are not
semi-transparent stains.
“Open
top
vapor
degreas-ing”
means-
the
batch
process
of
cleaning and removing s-oils from surfaces by condensing
hot solvent vapor on the colder metal parts.
“Open-ended valve” means any valve,
except pressure
relief
devices,
having
one
side
of
the
valve
in
contact
“1~Io
fleteetmhle
Volmtile
C~irrcmnie
I4riteriril
1~miv~ion~”

395
with process-
eith~—
direct~
“Operator
of
Gasoline
Dispensing
Facility”
means-
any
person
who
is
the
lessee
of
or
operates,
controls
or
supervises-
a
gasoline
dispensing
facility.
“Organic
compound”
means
any
compound
of
carbon,
excluding carbon monoxide, carbon dioxide, carbonic
acid,
metallic
carbides-
or
carbonates-,
and
ammonium
carbonate.
“Organic
material”
means
any
chemical
compound
of
carbon including diluents and thinners which are
liquids at standard conditions and which are used as-
dissolvers,
viscosity
reducers,
or
cleaning
agents,
but
excluding
methane,
carbon
monoxide,
carbon
dioxide-i--
carbonic acid, metallic carbonic acid, metallic
carbi-d-e-~, metallic carbonates,
and ammonium carbonate.
“Oven1’ means
~.
~hambe”—
•-‘
4—i--.
4
~—
,-,~-‘
4
-
,-
‘-
-
-
4--
-.
—.
followL.~
~
or ink.
“Overall
control”
means
the
product
of
the
capture
efficiency
and
the
control
device
efficiency.
“Ovcrvarnish” means a trans-parent coating applied
directly
over
ink
or
coating.
-
“Owner of Casoline Dispensing Facility” means any
person
who
has-
legal
or
equitable title to a stationary
storage tank at a gasoline dispensing facility-.-
“Owner or operator” means any person who owns-i-
operates,
leases,
controls,
or
supervises
an
emission
s-ource or air pollution control equipment.
“Packaging
rotogravure
printing”
means
rotogravure
printing upon paper, paper board,
metal
foil, plastic
film,
and
other
substrates,
which
are,
in
subsequent
operations,
formed
into
packaging
products
or
labels
for
articles
to
be
sold.
“Packaging
rotogravure
printing
line”
means
a
rotogravure printing line in which surface coatings are
applied to paper, paperboard,
foil,
film,
or other
fluid
and
one
side
open
to
the
through
open
piping
aascous
~.
.
~e3~-”-
.~..
-~4~c
~.
-e-f
~.
-~
material
or
a
mixture
of
organic
materials-
present
in
the
atmosphere.
...~cn nec...
i.~.
us-cd for
dry,
bake,
cure,

396
substrates
which
arc
to
be
us-ed
t-o
produce
containers,
packaging products-, or labels for articles.
“Paint manufacturing plant” means
a plant that mixes,
blends-,
or
compounds
enamels,
lacquers-,
s-ealers-,
ohellacs,
stains,
varnisheo,
or
pigmented
surface
coatings.
S.
I
any coating applied
pla~ticfilin,ormccaiuic ro~ to mcxc certain
products,
including
(but
not
limited
to)
adhesive
tapes
and
labels,
book
covers-,
post
cards,
office
copier
paper,
drafting
paper,
or
press-ure
sensitive
tapes.
Paper coating includes the application of coatings by
impregnation and/or saturation.
“Paper coating facility” means
a facility that includes
one or more paper coating lines.
“Paper coating line” means- a coating line in which any
protective,
decorative,
or functional coating
is
applied on, saturated into,
or impregnated into paper,
plastic film,
or metallic foil to make certain
products-,
including
(but not limited to)
adhcs-ive tapes
ana
I-aDCis-,
~oox
covers,
post
caros,
orricc
copier
paper,
drafting-
paper,
and
pressure
sensitive
tapes.
“Parts
per
million
(volume)”
means-
a
volume/volume
ratio
~i2~
exPr
*
yuz.~couuair
contaminant
in
a
muon
unit
volume
of
gas-.
“Person”
means-
any
individual,
corporation,
partnership,
association,
State,
municipality,
political
subdivision
of
a
State;
any
agency,
department, or instrumentality of the United Ctates--
and
any
officcr,
agent,
or
employee
thereof.
~**‘
‘4-
C
~
r—~~
-LLuc
oonecnLruL.Lon
of
“Petroleum Liquid” means crude oil, condensate or any
finished
or
intermediate
product
manufactured
at
a
petroleum
refinery,
but
not
including
Number
2
through
Number
6 fuel oils as specified
in
AS-TM D-396-69,
gas
turbine
fuel
oils
Numbers
2-CT
through
4-GT
as
specified
in AS-TN
-D-2-8S0-71
or diesel fuel oils Numbers
2-D
and
4—D,
as
soecified
in
AS-TM
D—975-68.
“Petroleum refinery”
producing gasoline,
means any facility
kerosene, distillate
engaged in
fuel oils,
residual
fucl
oils,
lubricants,
or
other
products
“Petroleum”
means- the crude oil removed from the earth
and the oils derived from tar sands, shale,
and coal.

-
397
through
distillation
of
petroleum,
or
through
redis-tillation,
cracking,
or
reforming
of
unfinished
petroleum
derivatives.
cml
~
memn~
mnv
comr~ound
on
mi vtune,
othen
than
food,
us-ed
in
the
prcvcntion,
diagnosis,
alleviation,
treatment,
or
cure
of
disease
in
human
and
animal.
“Pharmaceutical
coating
operation” means a device in
which
a
coating
is
applied
to
a
pharmaceutical,
including
air
drying
or
curing
of
the
coating.
“Photochemically
Reactive
Material”
means
any
organic
material with an aggregate of more than 20 percent of
-i-ts total volume composed of the chemical compounds
e-las-sified below or the composition of which exceeds
any
of
the
following
individual
percentage
composition
limitations.
Whenever
any
photochemically
reactive
material
or
any
constituent
of
any
organic
material
may
-be
classified
from
its
chemical
structure
into
more
than
one
of
the
above
groups-
of
organic
materials
it
&iall
be
considered
as-
a
member
of
the
most
reactive
group,
that
is,
the
group
having
the
least
allowable
percent
of
the
total
organic
materials.
A
combination
of
hydrocarbons-,
alcohols,
a-ldchydes-,
esters,
ethers-
or
ketones
having
an
olefinic
or
cyclo-olefinic
types
of
unsaturation:
5
percent.
This
definition
do-cs
not
apply
to
perchloroethylene
or
trichlorocthylcnc.
A
combination
of
aromatic
compounds
with
eight
or
more
carbon
atoms
to
the
molecule
except
cthylbenzenc:
8
percent.
A combination of ethylbenzenc, ketones- having
branched hydrocarbon structures- or toluenc:
20
percent.
“Pigmented coatings-” means opaque coatings containing
binders-
and
colored
pigments
which
are formulated to
conceal
the
wood
surface
either
as-
an
undercoat
or
topcoa-t-.-
~n
Iur~
Jucanu a
:~~r:
1-
;I
-r-c~
!?plantII
11
of
th
~ollutant-emitti....~
...cti’~~
belong--
4-—
4-i--’-~
—--i”—
-~“-~-4--~---’
grouping,
-located
on
one
or
more
contiguous-
or
adjacent
properties-,
and are under the control of the same
person
(-or persons under common control),
except the
activities- of any marine vessel.
Pollutant-emitting
activities shall be considered as part of the same
~I 1
L
I

398
“Prime
coat”
means
the
first
of
two
or
more
coatings
applied to a surface.
~uinfmcen
i—~omt—”
memn—~ n
comti
r,n
n-~-ed to
touch
up
areas on the surrace of automobile or light-duty truck
bodies
not
adequately
covered
by
the
prime
coat
before
applicati~.iof the top coat.
The prime surfacer coat
is applied between the prime coat and topcoat. An
anti-chip
coating
applied
to
main
body
parts
(e.g.,
rocker
panels,
bottom
of
doors
and
fenders-,
and
leading
edge
of
roof)
is
a
prime
surfacer
coat.
“Primers”
means
any
coatings
formulated
and applied to
substrates
to
provide
a
firm
bond
between
the
substrate
and subsequent coats.
“Printing”
means-the
application
of
words,
designs-,
and
pictures
to
a
substrate
using
ink.
industrial
grouping
if
they
belong
to
the
sam-c
“Major
Croup”
(i.e.,
which
have
the
same
two-digit
code)
as
des-cribed
in
the
“Standard
Industrial
Classification
(incorporated by reference in Section
“Plasticizers” means a substance added to a
polymer
composition to
soften
and
add
flexibility
to
the
product.
“Pneumatic
Rubber
Tire
Manufacture”
means-
the
production
of
pneumatic
rubber
tires
with a bead
auamctcr up
to
DUt
not ~ncuuaing ~u.u incncs and cross
section
dimension
up to 12.8
inches-, but not including
specialty tires for antique or other vehicles when
produced on equipment separate from normal production
lines for passenger or truck type tires.
“Polystyrene Plant” means any plant using styrenc to
manufacture polystyrene resin.
“Polystyrene Resin” means substance consisting of
styrene polymer and additives which is manufactured at
a polystyrene plant.
-
“Pressure Release” means the emission of materials
resulting from system pressure being greater than set
pressure of the pressure relief device.
“Pressure Tank” means a tank in which fluids arc stored
at a pressure greater than atmospheric pressure.

399
“Printing line” means an
series- of one or more roll printers and ~
roll coaters, drying areas,
and ovens wherein one or
more coatings arc applied,
dried,
and/or cured.
“Process” means any stationary emission source other
than
a
fuel
combustion
emission
source
or
an
incinerator.
“Process
Unit”
means
components-
assembled
to
produce-1
as
intermediate
or
final
products,
one
or
more
of
the
chemicals
listed
in
35
Ill.
Adm.
Code
219
Appendix
A.
A
process
unit
can
operate
independently
if
supplied
with
sufficient
feed
or
raw
materials-
and
sufficient
storage facilities for the product.
“Process
Unit
Shutdown”
means
a
work
practice
or
operational procedure that s-tops production from a
process- unit or part of a process- unit.
An unscheduled
w-e~rk
practice or operational procedure that stops
production from a process unit or part of a process
unit
for
loss
than
24
hours
is-
not
a
process
unit
sliutdown.
The use of
s-pare
components
and
technically
feasible
bypassing
of
components
without
s-topping
production
is
not
a
process
unit
shutdown.
“-PrOduction equipment exhaust system” means a system
for
coil-eating
and
directing
into
the
atmosphere
emissions-
of
volatile
organic
material
from
reactors,
centrifuges,
and other process emission sources-.
“Publication rotogravure printing line” means—a
~-e-togravurcprinting line in which coatings- are applied
to paper which
is- subsequently formed into books,
magazines,
catalogues,
brochures,
directories-,
newspaper supplements-,
or other types of printed
material.
-
“Purged
Pro~u~~
m
n
1 fl ~‘1
,
n
ciu v
i cici r-
f
n rim
n
Fluid”
liqu~
p-t=-oocss
unit that contains volatile organic material
and that results from flushing or cleaning the sample
line(s)
of
a
process
unit
so
that
an
uncontaminated
sample
may
then
be
taken
for
testing
or
analysis-.
“Reactor”
means
a vat, vessel,
or other device in which
chemical
reactions
take
place.
-“Reasonably
Available
Control
Technology
(RACT)”
means
the
lowest
emission
limitation
that
an
emission
source
is- capable of meeting by the application
of, control
t-eohnology that
is
reasonably
available
considering
technological and economic feasibility.
* S

400
.llflefiner”
means
any
person
who owns,
leases-,
op-crates,
eentrols-,
or
supervises
a
refinery.
“Refinery Fuel Cas” means any gas which
is-
generated
by
a
petroleum
refinery
proccs-s
unit
and
which
is
combusted at the refinery, including any gaseous
mixture of
natural
gas
and
fuel
gas-.
“-Refinery unit,
process- unit or unit” means a
s-ct of
components
which
are
a
part
of
a
basic
process-
eperation such
as
distillation,
hydrotrcating-~-
e~acking,or reforming of hydrocarbons.
“Refrigerated
condenser”
means
a
surface
condenser
in
which the coolant supplied to the condenser has- been
cooled
by
a mechanical device,
other than by a cooling
tower or evaporative s-pray cooling,
such as
refrigeration
unit
or
steam
chiller
unit.
“Reid vapor pressure” means the standardized measure of
the
vapor
pressure
of
a
liquid
in
pounds
per
square
-inch absolute
(Ps-ia)
at 100°F(37.8°C).
“Repair
coatings-”
means-
coatings-
us-cd
to
correct
Tilmperfections
or
damage
to
furniture
surface.
1~~flepaired~~
means,
for the purpose of Subpart Q of this
Part,
that
equipment
component
has
been
adjusted,
or
etherwise
altered,
to eliminate a
leak.
.
-
rn~mrir
1’~d~J.
F’~sl Oi-l”
r~z~.s
fuel
cils—cf
~
No.
4,
~
a-nd
6
as specified in detailed requirements for fuel
e-ils A.S.T.N.
D-396-69
(1971).
“Retail Outlet” means any gasoline dispensing facility
at which gasoline
is sold or offered for sale for
us-c
-i-n motor
vehicles.
“Roll coater” means
an apparatus in which a uniform
layer of coating
is
applied
by
means-
of
one
or
more
rolls
across
the
entire
width
of
a
moving
substrate.
1tRoll
printer”
means-
an
apparatus
used
in
the
application
of
words,
designs-,
and pictures to a
s-ubstrate,
usually by means of one or more rolls each
w-i-th
only partial coverage.
11-Roll
printing” means the
application
of
words,
designs,
and pictures to a substrate usually by means
rif
ri
~~r-’nie~ of
hmrd
nuhhr-n
on
mr’tml
vol
1
‘z
erich
~i
th
only
partial coverage.

401
“Roller coating” means a
to
a
sheet
or
strip
in
which
the
coating
is-
trans-ferred
by
a
roller
or
series
of
rollers.
“Rolling
limit”
means-
that
a
limit
or
limitation
must
not exceed an annual limit rolled on a
basis- of at mo-st
a
month
monthly
basis-;
that
is,
for
example,
a
monthly
production
or
capacity
level
must
be
determined
for
each
parameter
subject~to
a
production
or
capacity
limitation
and
added
to
the
eleven
prior
monthly
levels-
for
monthly
comparison
with
the
annual
limit.
“Rotogravure printing” means the application of words-,
designs, and pictures- to a substrate by means- of
a roll
printing technique in which the pattern to be applied
-s recessed relative to the non—immnc area.
“Rotogravure printing line” means a printing line in
which each roll printer us-cs a roll with recessed areas
f-or
applying an image to a substrate.
“Safety relief valve” means a valve which
is- normally
closed and which is designed to open in order to
relieve excessive pressures- within a vessel or pipe.
“~sandings-ealcrs” means any coatings formulated for and
applied to bare wood for sanding and to seal the wood
f-or
subsequent application of varnish.
To be
eonsidcred a sanding seal-cr a coating must be clearly
labelled
as- such.
“-Sealer” means a coating containing binders- which seals
wood prior to the application of the subsequent
eoatings.
~Sensor” means
a device that measures- a physical
quantity or the change in a physical quantity such as
temperature,
pressure,
flow
rate,
pH,
or
liquid
level.
“Semi—transparent stains” means stains containing dyes
e-r
semi-trans-parent pigments which are formulated to
enhance wood grain and change the color of the surface
but not to conceal the surface,
including,
but not
limited to, sap stain,
toner, non—grain raising stains,
pad stain,
or s-patter stain.
“Set of safety relief valves-” means one or more safety
relief
valves
designed
to
open
in
order
to
relieve
excessive
pressures-
in
the same vessel or pipe.
t1~~j
hm~tecomt”
memn’i
ri
coriti
nc-i
~i
-~
~pp1ied to ~~a’
the
metal
is
in
sheet form to serve as either th

402
exterior
or
interior
of
a
can
f
three-piece
cans.
“S-ide-s-earn
s-pray
coat”
means
a
or
either
two—piece---er
coating
applied
to
the
scam of
a three-piece can.
application
applied
to
“~Cingle coat”
means
one
coating
ri
mr’tml
‘-iiirfmee.
“Solvent”
means
a
liquid
substance
that
is-
used
to
dissolve
or
dilute
another
substance.
“Solvent
cleaning”
means
the
process-
of
cleaning
soils
from
surfaces
by
cold
cleaning,
open
top
vapor
degroasing,
or
conveyorized
degreasing.
“Specified air contaminant” means any air contaminant
as
to
which
this-
Part
contains-
emission
standards
or
other specific limitations-.
“Splash
loading”
means
a
method
of
loading
a
tank,
~-ailroadtank car,
tank truck,
or trailer by use of
other than a submerged loading pipe.
“S-tack”
means
a
flue
or
conduit,
free-standing or with
exhaust
port
above the roof of the building on which it
is mounted, by which air contaminants are emitted into
the atmosphere.
“Standard
conditions”
means
a
temperature
of
70°F and
a
~~“re
of 14.7 nsia.
“-Standard
cubic
foot
(sef)”
means
the
volume
of
one
cubic foot of gas at standard conditions-.-
“-Standard Industrial Classification Manual” means the
Standard Industrial Classification Manual
(1987),
&uperintendent of Documents,
U.S. Government Printing
Office, Washington,
DC 20402
(incorporated by
reference
in Section 219.112).
“Start-up”
means
the
setting
in operation of an
emission source for any purpose.
“-Stationary
emission
source”
mean
an emission source
which
is- not self-propelled.
“Storage tank or storage vessel” means any stationary
tank,
reservoir or container used for the storage of
VOL.

403
“Styrene
Dcvolatilizcr
Unit”
moans
equipment
performing
the
function of separating unreacted styrene monomer
and other volatile components from polystyrene in
a
vacuum devolatilizer.
“Styrenc Recovery Unit” means equipment performing the
function of separating styrcnc monomer from other
less-
volatile components of the styren-e devolatilizer unit’s
output.
The separated styrene monomer may be reused as
a raw material in the polystyrene ~lant.
“Submerged loading pipe” means any discharge pipe or
nozzle which meets either of the following conditions+
Where the tank is filled from the top, the end of
the discharge pipe or nozzle must be totally
submerged when the liquid level
is
15 cm
(6
in.)
above the bottom of the tank.
tank
is filled from the side,
the
Where
the
discharge
pipe
or
nozzle
must
be totally submerged
when
the
liquid
level
is
46
cm
(18
in.)
above
the
be-ttom of the tank.
“Substrate” means the surface onto which a coating
is
applied
or
into
which
a coating
is impregnated.
“Surf
II
-
which
—--4-
~i1h’1tmrIr-~e
from
ri
gas stream
by
-rciuinc~
thr’
tcnipr’’—m-r-~irr-
of
the
stream,
without
direct
cont~..~oetwecn
th~
coolant
and
the
stream.
“Synthetic Organic Chemical or Polymer Manufacturing
Plant” means a plant that produces-,
as intermediates or
final
products,
one or more of the chemicals or
polymers list-cd in 35
Ill.
Adm. Code
219
Appendix
A.
“Tablet coating operation” means
a pharmaceutical
coating
operation
in
which
tablets
are
coated.
“Thirty-day rolling average” means any value
arithmetically averaged over any consecutive
thirty-days.
“Three-piece can” means a can which is made from a
rectangular sheet and two circular ends-.
“Topcoat” means
a coating applied in a multiple coat
operation other than prime coat,
final repair coat,
or
prime surfacer coat.

404
“Topcoat operation” means all topcoat spray booths-,
flash-off
areas,
and
bake
ovens- at a facility which are
us-ed
to
apply,
dry,
or
cure
the
final coatings
(except
final
off-line
repair)
on
components
light-duty truck bodies.
of
automobile
or
n,c~
I IU
I
~
~~~fer
efficiency”
the ratio of the
coating
solids-
deposited
onto
a
part
or
product
to
the
total
amount
of
coating
solids
us-cd.
“Tread End Cementing” means the application of a
solvent—based
cement
to
the
tire
tread
ends.
“True vapor pressure” means the equilibrium partial
pressure e~ertedby a volatile organic liquid as
determined in accordance with methods described in
American Petroleum Institute Bulletin 2517,
“Evaporation Loss From Floating Roof Tanks-,” second
edition, February 1980 (incorporated by reference in
Section
219.112)
“Turnaround”
means-
the
procedure
of
shutting
down
an
operating
refinery
unit,
emptying
gaseous
and
liquid
contents
to
do
inspection,
maintenance
and repair work,
mn~ nut±i na
the
uni t~ brick
into
nrriducti
or,
-
‘4~-
“Undcrcoaters-” means any coatings- formulated for and
applied to substrates to provide a smooth surface for
subsequent coats.
“Undertread Cementing” means the application of a
solvent-based cement to the underside of a tire tread.
Unregulated safety relief valve” means- a safety relief
valve which cannot be actuated by a means other than
high pressure in the pipe or vessel which it protects-.
“Vacuum producing system” means any reciprocating,
rotary,
or centrifugal blower or compressor or any jet
ejector
or device that creates suction from a pressure
below
atmospheric
and
discharges
against
a
greater
pressure.
“Valves not externally
regulated”
means
valves
that
have no external controls, such as in—line check
valves.
“Vapor balance system” means any combination of pipes
or hoses which creates a closed system between the
“Two-piece can” means
a can which is drawn from a
shallow cup and requir
only one end to be attached.

405
vapor spaces of
an
unloading
tank
and
a
receiving
tank
such that vapors displaced from the receiving tank are
transferred to the tank being unloaded.
“Vapor
collection
system”
means
all
piping,
seals,
hoses,
connections-,
pressure-vacuum
vents-,
and
other
possible
sources-
between
the
gasoline
delivery
vessel
and
the
vapor
processing
unit
and/or
the
storage
tanks-
and
vapor
holder.
“Vapor
control
system”
moans
any
system
that
limits-
or
prevents
release
to
the
atmosphere
of
organic
material
in
the
vapors
displaced
from
a
tank
during
the
transfer
of
gasoline.
“Vapor-Mounted Primary Seal” means a primary s-cal
mounted with an air space bounded by the bottom of the
primary seal, the tank wall,
the liquid surface and the
floating roof.
“Vapor recovery system” means a vapor gathering system
capable
of
collecting
all
VON
vapors
and
gases
discharged
from
the
storage
tank
and
a
vapor
disposal
system capable of processing such VON vapors and gases
so
as
to
prevent
their
emission
to
the
atmosphere.
“Vehicle” means a device by which any person or
property
may
be
propelled,
moved,
or
drawn
upon
a
highway,
excepting
a
device
moved
exclusively
by
human
power
or used exclusively upon stationary rails or
tracks.
-
“Vinyl
coating”
means
any
topcoat
or
printing
ink
applied
to
vinyl
coated
fabric
or
vinyl
sheets.
Vinyl
coating does not include plasticols.
“Vinyl coating facility” means a facility that includes
one or more vinyl coating line(s).
“Vinyl coating line” means a coating line in which any
protective, decorative or functional coating
is- applied
onto vinyl coated fabric or vinyl
sheets.
“Volatile organic liquid
(VOL)’1 means any substance
which
is liquid at storage conditions and which
contains volatile organic compounds.
“Volatile organic material
(VON)
or volatile organic
compound
(VOC)” moans “volatile organic material
(VON)
or volatile organic compound
(VOC)”,
as that term is
defined in 35
Ill. Adm. Code Part 211.

406
“Volati,le
Petroleum
Liquid”
means
any
petroleum
liquid
with
a
true
vapor
pressure
that
is
greater
than
1.5
ps-ia
(78 millimeters of mercury)
at standard
conditions.
“Wash coat” means a coating containing binders which
seals
wood
surfaces,
prevents
undesired
staining,
and
contro
is-
penetration.
“Wastowatcr
(Oil/Water)
Separator” moans any device or
piece of equipment which utilizes the difference in
density
between
oil
and
water
to
remove
oil
and
associated
chemicals
from
water,
or any device, such as
a flocculation tank or a clarifier,
which removes
netroleum
derived
eomnounn-~
rrom wa~tcwater.
“Web” means a substrate which is printed in continuous
roll—fed
presses.
“Wood furniturc-- means room furnishings including
cabinets
(kitchen,
~atn, and vanity),
tables, chairs,
beds,
sofas-,
shutters,
art objects, wood paneling, wood
flooring,
and
any
other
coated
furnishings
made
of
-
wood,
wood
composition,
or
fabricated wood materials.
“Wood
furniture
coating
facility”
moans
a
facility
that
includes one or more wood furniture coating line(s).
“Wood
furniture
coating
line”
moans
a
coating
line
in
which any protective,
decorative,
or functional coating
is applied onto wood furniture.
“Woodworking” means the shaping,
sawing,
grinding,
smoothing,
polishing,
and
making
into
products of any
form
or
~hmne
of
wood.
The definitions of
35 Iii.
Adm. Code 211 apply to this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
Section
219.105
Test Methods and Procedures
a)
Coatings, Inks and Fountain Solutions
The following test methods and procedures shall be used
to determine compliance of as applied coatings,
inks,
and
fountain
solutions
with
the
limitations
set
forth
in this Part.
1)
Sampling:
Samples collected for analyses shall be
one-liter taken into a one—liter container at a

407
location and time such that the sample will be
representative of the coating as applied
(i.e.,
the sample shall- include any dilution solvent or
other VON added during the manufacturing process).
The container must be tightly sealed immediately
after the sample is taken.
Any solvent or other
VON added after the sample is taken must be
measured and accounted for in the calculations in
subsection
(a)
(3)
of
this
Section.
For
multiple
package coatings, separate samples of each
component shall be obtained.
A mixed sample shall
not be obtained as it will cure in the container.
Sampling procedures shall follow the guidelines
presented in:
A)
ASTM D3925-8l(1985) standard practice for
sampling liquid paints and related pigment
coating. This practice is incorporated by
reference in Section 219.112 of this Part.
B)
ASTM E300-86 standard practice for sampling
-
industrial chemicals. This practice is
incorporated by reference in Section 219.112
of this Part.
2)
Analyses:
The
applicable
analytical
methods
specified below shall be used to determine the
composition of coatings,
inks,
or fountain
solutions
as applied.
A)
Method 24 of 40 CFR 60, Appendix A,
incorporated
by reference in Section 219.112
of this Part,
shall be used to determine the
VON content and density of coatings.
If it
is demonstrated to the satisfaction of the
Agency and the USEPA that plant coating
formulation data are equivalent to Method 24
results, formulation data may be used.
In
the event of any inconsistency between a
Method 24 test and a facility’s formulation
data,
the Method 24 test will govern.
B)
Method 24A of 40 CFR Part 60, Appendix A,
incorporated by reference
in
Section
219.112,
shall be used to determine the VOM content
and density of rotogravure printing inks and
related coatings.
If it is demonstrated to
the satisfaction of the Agency and USEPA that
the plant coating formulation data are
equivalent to Method 24A results, formulation
data may be used.
In the event of any
inconsistency between a Method 24A test and
a-

408
facility’s- formulation data,
the Method 24A
test will govern.
C)
The following ASTM methods are the analytical
procedures for determining VON:
i)
ASTM D1475-85: Standard test method for
density of paint, varnish,
lacquer and
related products.-
This test method is
incorporated by reference in Section
219.112 of this Part.
ii)
ASTM D2369-87: Standard test method for
volatile content of a coating. This test
method
is incorporated by reference in
Section 219.112 of this Part.
iii) ASTM D3792-86: Standard test method for
water content of water—reducible paints
by direct injection into a gas
chromatograph. This test method
is
incorporated by reference in Section
219.112 of this Part.
iv)
ASTN D4017-81(1987): Standard test
method for water content in paints and
paint materials by the Karl Fischer
method. This test method is incorporated
by reference in Section
219.112
of this
Part.
v)
ASTM D4457-85:
Standard test method for
determination of dichloromethane and
1,1,1, trichloroethane in paints and
coatings by direct injection into a gas
chromatograph.
(The procedure
delineated- above can be used to develop
protocols for any compounds specifically
exempted from the definition of VON.)
This test method is incorporated by
reference in Section 219.112 of this
Part.
vi)
ASTM D2697-86:
Standard test method for
volume non—volatile matter in clear or
pigmented coatings.
This test method is
incorporated by reference in Section
219.112 of this Part.
vii) ASTM D3980-87:
Standard practice for
interlaboratory testing of paint and
related materials.
This practice is

-
409
incorporated by reference in Section
219.112 of this Part.
viii)ASTM E180-85:
Standard practice for
determining the precision data of ASTM
methods for analysis of and testing of
industrial chemicals. This practice is
incorporated by reference in Section
219.112 of this Part.
ix)
ASTM D2372-85: Standard method of
separation of vehicle from
solvent-reducible paints. This method is
incorporated by reference in Section
219.112 of this Part.
D)
Use of an adaptation to any of the analytical
methods specified in subsections
(a) (2) (A),
(B), and
(C)
of this Section may not be used
unless approved by the Agency and USEPA.
An
owner or operator must submit sufficient
documentation for the Agency and USEPA to
find that the analytical methods specified in
subsections
(a) (2) (A),
(B), and
(C)
of this
Section will yield inaccurate results and
that the proposed adaptation is appropriate.
3)
Calculations:
Calculations for determining the
VON content, water content and the content of any
compounds which are specifically exempted from the
definition of VON of coatings,
inks and fountain
solutions as applied shall follow the guidance
provided in the following documents-~
A)
“A Guide for Surface Coating Calculation”,
EPA-340/l-86-016,
incorporated by reference
in Section 219.112 of this Part.
B)
“Procedures for Certifying Quantity of
Volatile Organic Compounds Emitted by Paint,
Ink and Other Coatings”
(revised June 1986),
EPA-450/3-84-0l9,
incorporated by reference
in Section 219.112 of this Part.
C)
“A Guide for Graphic Arts Calculations”,
August 1988,
EPA—340/1—88-003,
incorporated
by reference in Section 219.112 of this Part.
b)
Automobile or Light-Duty Truck Test Protocol
.~j,.
The protocol for testing,
including determining
the transfer efficiency~of coating applicators~

410
at primer surfacer operations and topcoat eeating
operations
at
an
automobile
or
light-duty
truck
assembly facility source shall follow the
procedure in: “Protocol for Determining the Daily
Volatile Organic Compound Emission Rate of
Automobile and Light-Duty Truck Topcoat
Operations”
(“topcoat protocol”), December 1988,
EPA-450/3-88-0l8,
incorporated by reference in
Section 219.112 of this Part.
21
Prior
to
testing
pursuant
to the topcoat protocol,
the owner or operator of a coating operation
sublect to the topcoat or primer surfacer limit in
Sections 219.204(a) (2) or 219.204(a) (3)
shall
submit a detailed testing proposal specifying the
method by which testing will be conducted and how
compliance will be demonstrated consistent with
the topcoat protocol.
The ~ro~osal shall include,
at a minimum,
a comprehensive plan
(including a
rationale)
for determining the transfer efficiency
at each booth through the use of in-plant or pilot
testing,
the selection of coatings to be tested
(for the purpose of determining transfer
efficiency)
including the rationale for coating
groupings,
the method for determining the analytic
VON content of as applied coatings and the
formulation solvent content of as applied
coatings, and a description of the records of
coating VON content as applied and coating’s usage
which will be kept to demonstrate compliance.
Upon approval of the proposal by the Agency and
USEPA, the compliance demonstration for a coating
line may proceed.
c)
Capture System Efficiency Test Protocols
1)
Applicability
The requirements of subsection
(c) (2)
of this
Section shall apply to all VON emitting processes
emission units employing capture equipment
(e.g.,
hoods, ducts), except those cases noted below.
A)
If
-a-—source installs-an emission unit is
eguipped with (or
uses)
a permanent total
enclosure
(PTE)
that meets Agency and USEPA
specifications,
and which directs all VON to
a
control
device,
then
the
sourceemission
unit is exempted from the requirements
described in subsection
(c) (2)
of this
Section.
The Agency and USEPA specifications
to determine whether a structure is

411
considered a PTE are given
in Procedure T of
Appendix B of this Part.
In this instance,
the capture efficiency is assumed to be 100
percent
and
the
s-ourceemission
unit
is
still
required
to
measure
control
efficiency
using
appropriate test methods as specified in
subsection
(d)
of this Section.
B)
If a source uses-an emission unit is ectuipped
with
(or uses)
a control device designed to
collect and recover VON (e.g., carbon
adsorber),
an explicit measurement of capture
efficiency is not necessary provided that the
conditions given below are met.
The overall
control of the system can be determined by
directly comparing the input liquid VOM to
the
recovered
liquid VOM.
The general
procedure for use in this situation is given
in 40 CFR 60.433,
incorporated by reference
in
Section
219.112
of
this Part, with the
following additional restrictions:
i)
‘wC
source must be able to
erm~c
s-oivcnt
us-age
witn
solvent
recovery
on
a
24—hour
(daily)
basis,
rather
than
a
30-day weighted average, within 72 hours
-f-o-llowing the 24-hour period.
In
addition,
one
of
the
following
two
criteria must be met: The source owner
or operator shall obtain data each
operating day for the solvent usage and
solvent recovery to permit the
determination of the solvent recovery
efficiency of the system each operating
day using a 7-day rolling period.
The
recovery efficiency for each operating
day is computed as the ratio of the
total recovered solvent for that day and
the most recent prior
6 operating days
to the total solvent usage for the same
7—day period used for the recovered
solvent, rather than a 30-day weighted
average
as
given
in
40
CFR
60.433
incorporated bY reference in Section
219.112 of this Part.
This ratio shall
be expressed as a percentage.
The ratio
shall_be computed within 72 hours
following each 7—day period.
A source
that believes that the 7—day rolling
period is not appropriate may use an
alternative multi-day rolling period not
to exceed
30 days.
with the approval of

412
the Agency and USEPA.
In addition, the
criteria in subsection
(c) (1) (B) (ii) or
subsection
(c) (1) (B)
(iii)
below must be
met.
ii)
The solvent recovery system
(i.e.,
capture
and
control
system)
must
be
dedicated to a single coating line,
printing
line,
or
other
discrete
activity that by itself
is subject to an
applicable VON emission standard,
process line
(e.g.,
one pr-ocess line
venting to a carbon adsorber system), or
iii)
If the solvent recovery system controls
more than one coating line, printing
line or other discrete activity that by
itself is subject to an applicable VON
emission standard, the overall control
(i.e. the total recovered VON divided by
the sum of liquid VON input from all
lines and other activities venting to
the control system) must meet or exceed-
the most stringent standard applicable
to
any
line
or
other
discrete
activity
venting to the control system.multiple
nnoce~s
lines,
then
the
source
must
he
_________
-
- 5
~
~tTISWS~S
1
1
‘—,
‘_4’_
-I
/I
contro~
~
total
rccovercci
s-o-lvent VON divided by the sum of liquid
V-ON
input
to
all
process
lines
venting
to the control system) meets or exceeds
the most stringent standard applicable
for any process line venting to the
control system.
2)
Specific Requirements
The capture efficiency of
a process- line~~
emission unit shall be measured using one of the
four protocols given below.
Any error margin
associated with a test protocol may not be
incorporated into the results of a capture
efficiency test.
If these techniques are not
suitable for a particular process, then the source
may use an alternative capture efficiency protocol
may be used, provided that the alternative
protocol
is approved by the Agency and approved by
the USEPA as a SIP revision.
A)
Gas/gas method using temporary total
enclosure
(TTE).
The Agency and
USEPA

413
specifications to determine whether a
temporary enclosure is considered a TTE are
given in Procedure T of Appendix B of this
Part.
The capture efficiency equation to be
used for this protocol is:
-
CE
=
Gw/(Gw
+
Fw)
where:
CE
=
capture efficiency,
decimal
fraction~
Gw
=
mass of VOM captured and delivered
to control device using a
TTEj..
Fw
=
mass of fugitive VON that escapes
from a TTE~
Procedure G.2 contained in Appendix B of this
Part is used to obtain Gw.
Procedure F.? in
Appendix B of this Part is used to obtain Fw.
B)
Liquid/gas method using TTE.
The Agency and
USEPA
specifications to determine whether
a
temporary enclosure is considered a TTE are
given
in Procedure T of
Appendix B of this
Part.
The capture efficiency equation to be
used for this protocol
is:
CE
=
(L
-
Fw)/L
where:
CE
=
capture efficiency, decimal
fractionj.
L
=
mass of liquid VON input to process
emission unit
Fw
=
mass of fugitive VON that escapes
from a TTE~
Procedure L contained in Appendix B of this
Part is used to obtain L.
Procedure F.? in
Appendix B of this Part is used to obtain Fw.
C)
Gas/gas method using the building or room
(building or room enclosure)~ in which the
affected coating line,- printinct line or other
sourceemission unit is located~as the
enclosure and in which
“F” and “G” are

414
measured while operating only the affected
line or facilityemission unit.
All fans and
blowers in the building or room must be
operated as they would under normal
-~
production.
The capture efficiency equation
to be used for this protocol
is:
CE
=
G/(G
+
F,,)
where:
CE
=
capture efficiency,
decimal
fraction~
-
G
=
mass of VON captured and delivered
to control devicej
F,,
=
mass of fugitive VON that escapes
from building enclosure~
Procedure G.2 contained in Appendix B of this
Part is used to obtain G.
Procedure F.2
in
Appendix B of this Part is used to obtain FB.
D)
Liquid/gas method using the building or room
(building or room enclosure)~in which the
affected coating line, printing line or other
sourceemission unit is located~as the
enclosure and in which “F” and “L” are
measured while operating only the affected
line facility emission unit.
All fans and
blowers in the building or room must be
operated as they would under normal
production.
The capture efficiency equation
to be used for this protocol is:
CE
=
(L
-
where:
CE
=
capture efficiency,
decimal
fraction~
L
=
mass of liquid VON input to process
emission unit
FB
=
mass of fugitive VON that escapes
from building enclosure~

415
Procedure L contained in Appendix B of this
Part is used to obtain
L.
Procedure F.2 in
Appendix B of this Part is used to obtain FB.
3)
Recordkeeping
and
Reporting
A)
All affected facilities-owners or operators
affected by this subsection must maintain a
copy
of
the
capture
efficiency
protocol
submitted to the Agency and the USEPA on
file.
All results of the appropriate test
methods and capture efficiency protocols must
be reported to the Agency within sixty
(60)
days of the test date.
A copy of the results
must be kept on file with the source for a
period of three
(3)
years.
B)
If any changes are made to capture or control
equipment,
then the source is required to
notify the Agency and the U-SEPA of these
changes and a new test may be required by the
Agency or the USEPA.
C)
The source must notify the Agency 30 days
prior to performing any capture efficiency or
control test.
At that time,
the source must
notify the Agency which capture efficiency
protocol and- control device test methods will
be used.
D)
Sources utilizing a PTE must demonstrate that
this enclosure meets the requirement given in
Procedure T
(in Appendix B of this Part)
for
a PTE during any testing of their control
device.
E)
Sources utilizing a TTE must demonstrate that
their TTE meets the requirements given
in
Procedure T
(in Appendix B of this Part)
for
a
TTE
during testing of their control device.
The source must also provide documentation
that the quality assurance criteria for a
TTE
have been achieved.
d)
Control Device Efficiency Testing and Monitoring
1)
The control device efficiency shall be determined
by simultaneously measuring the inlet and outlet
gas phase VON concentrations and gas volumetric
flow rates
in accordance with the gas phase test

416
methods specified
in subsection
(f)
of this
Section.
2)
Any owner or operator~
~
~Ihat uses an afterburner or carbon adsorber
to comply with any Section of this Part 2J~.
shall
use Agency and USEPA approved
continuous monitoring equipment which is
installed,
calibrated, maintained,
and
operated according to vendor specifications
at all times the afterburner or carbon
adsorber is in use except as provided in
subsection
(d) (3)
of this Section.
The
continuous monitoring equipment must monitor
the following parameters:
A-)-
j,J
For each afterburner which does not have
a catalyst bed, the Gcombustion chamber
temperature of each afterburner.
s-)-
jj1.
For each afterburner which has
a
catalyst bed, commonly known as a
catalytic afterburner,
the ~emperature
rise across each catalytic afterburner
bed or VOM concentration of exhaust.
s-)-
iii)
For each carbon adsorber, ~I’theVON
concentration of each carbon adsorption
bed exhaust or the exhaust of the bed
next in sequence to be desorbed.
~j
Of an automobile or light-duty truck primer
surfacer operation or topcoat operation
sublect to subsection
(d) (2) (A)
above,
shall
keep
a separate record of the following data
for the control devices, unless alternative
provisions are set forth
in
a permit pursuant
to Title V of the Clean Air Act:
~jj
For thermal afterburners for which
combustion chamber temperature
is
monitored,
all 3—hour periods of
operation in which the average
combustion temperature was more than
28°C(50°F) below the average combustion
temperature measured during the most
recent performance test that
demonstrated that the operation was in
compliance.

417
JJJ
For catalytic afterburners for which
temperature rise
is monitored, all
3—hour periods of operation in which the
average gas temperature before the
catalyst bed is more than 28°C(50°F)
below the average gas temperature
immediately before the catalyst bed
measured during the most recent
performance test that demonstrated that
the operation was in compliance.
iii) For catalytic afterburners and carbon
adsorbers for which VON concentration is
monitored, all 3—hour periods of
operation during which the average VON
concentration or the reading of organics
in the exhaust gases
is more than 20
percent greater than the average exhaust
gas concentration or reading measured by
the organic monitoring device during the
most recent determination of the
recovery efficiency of a carbon adsorber
or performance test for a catalytic
afterburner, which determination or test
that demonstrated that the operation was
in compliance.
~j.
An owner or operator that uses a carbon adsorber
to comply with Section 219.401 of this Part may
operate the adsorber during periods of monitoring
equipment malfunction, provided that:
~J
The owner or operator notifies in writing the
Agency and USEPA.
within
10 days after the
conclusion of any 72 hour period during which
the adsorber
is operated and the associated
monitoring equipment is not operational,
of
such monitoring equipment failure and
provides the duration of the malfunction,
a
description of the repairs made to the
equipment, and the total to date of all hours
in the calendar year during which the
adsorber was operated and the associated
monitoring equipment was not operational
~j
During such period of malfunction the
adsorber is operated using timed sequences as
the basis for periodic regeneration of the
adsorber
~j
The period of such adsorber operation does
not exceed 360 hours in any calendar year

418
without the approval of the Agency and USEPA
and
Qj
The total of all hours in the calendar year
during which the adsorber was operated and
the associated monitoring equipment was not
operational shall be reported,
in writing, to
the Agency and USEPA by January 31st of the
following calendar year.
e)
Overall Efficiency
1)
The overall efficiency of the emission control
system shall be determined as the product of the
capture system efficiency and the control device
efficiency or by the liquid/liquid test protocol
as specified in 40 CFR 60.433,
incorporated by
reference in Section 219.112 of this Part,
(and
revised by subsection
(c) (1) (B)
of this Section)
for each solvent recovery system.
In those cases
in which the overall efficiency is being
determined for an entire line,
the capture
efficiency used to calculate the product of the
capture and control efficiency is the total
capture efficiency over the entire line.
2)
For coating lines which are both chosen by the
owner or operator to comply with Section
219.207(a),
(d),
(e),
(f), or
(g)
of this Part by
the alternative in Section 219.207(b) (2)
of this
Part and meet the criteria allowing them to comply
with Section 219.207 instead of Section 219.204 of
this Part,
the overall efficiency of the capture
system and control device,
as determined by the
test methods and procedures specified in
subsections
(c),
(d)
and
(e) (1)
of this Section,
shall be no less than the equivalent overall
efficiency which shall be calculated by the
following equation:
E
=
(VONa
-
VON1
/VOMa)
x 100
where:
E
=
Equivalent overall efficiency of the
capture system and control device as a
percentage~j
VONa
=
Actual VON content of a coating,
or the
daily-weighted average
VON
content of
two or more coatings
(if more than one

419
coating is used),
as applied to the
subject coating line as determined by
the applicable test methods and
procedures specified in subsection
(a) (4) (i)
of this Part in units of kg
VOM/l
(lb VOM/gal)
of coating solids as
appIied7~
VON1
=
The VON emission limit specified in
Ccction 219.207(Q)
or
(b)
Sections
219.204 or 219.205 of this Part in units
of kg VON/l
(lb VOM/gal)
of coating
solids as applied.
f)
Volatile Organic Material Gas Phase Source Test Methods
The methods in 40
CFR
Part 60, Appendix A, incorporated
by reference in Section 219.112 of this Part delineated
below shall be used to determine control device
efficiencies.
1)
40 CFR Part 60, Appendix A, Method 18,
25 or 25A,
incorporated by reference in Section 219.112 g~
this Part as appropriate to the conditions at the
site,
shall be used to determine VON
concentration.
Method selection shall be based on
consideration of the diversity of organic species
present and their total concentration and on
consideration of the potential presence of
interfering gases.
Except as indicated in
subsections
(f) (1) (A)
and
(B)
below,
the test
shall consist of three separate runs,
each lasting
a minimum of 60 mm, unless the Agency and the
USEPA determine that process variables dictate
shorter sampling times.
A)
When the method is to be used to determine
the efficiency of a carbon adsorption system
with a common exhaust stack for all the
individual adsorber vessels, the test shall
consist of three separate runs,
each
coinciding with one or more complete
sequences through the adsorption cycles of
all the individual adsorber vessels.
B)
When the method is to be used to determine
the efficiency of a carbon adsorption system
with individual exhaust stacks for each
adsorber vessel, each adsorber vessel shall
be tested individually.
The test for each
adsorber vessel shall consist of three

420
separate runs.
Each run shall coincide with
one or more complete adsorption cycles.
2)
40 CFR Part 60, Appendix A, Method
1 or
1A,
incorporated by reference in Section 219.112 ~
this Part,
shall be used for sample and velocity
traverses.
3)
40 CFR Part 60, Appendix A, Method
2,
2A,
2C or
2D, incorporated by reference in Section 219.112
of this Part,
shall be used for velocity and
volumetric flow rates.
4)
40 CFR Part 60, Appendix A, Method
3, incorporated
by reference in Section 219.112 of this Part,
shall be used for gas analysis.
5)
40 CFR Part 60, Appendix A, Method
4,
incorporated
by reference in Section 219.112 of this Part,
shall be used for stack gas moisture.
6)
40 CFR Part 60, Appendix A, Methods
2,
2A,
2C,
2D,
3 and 4, incorporated by reference in Section
219.112 of this Part,
shall be performed,
as
applicable,
at least twice during each test run.
7)
Use of an adaptation to any of the test methods
specified in subsections
(f) (1),
(2),
(3)
,
(4),
(5)
and
(6) of this Section may not be used unless
approved by the Agency and the USEPA on a case by
case basis.
An owner or operator must submit
sufficient documentation for the Agency and the
USEPA to find that the test methods specified in
subsections
(f) (1)
,
(2)
,
(3)
,
(4)
,
(5)
and
(6) ~
this Section will yield inaccurate results and
that the proposed adaptation is appropriate.
g)
Leak Detection Methods for Volatile Organic Material
Owners or operators required by this Part to carry out
a leak detection monitoring program shall comply with
the following requirements:
1)
Leak Detection Monitoring
A)
Monitoring shall comply with 40 CFR 60,
Appendix A, Method
21,
incorporated by
reference in Section 219.112 of this Part.
B)
The detection instrument shall meet the
performance criteria of Method 21.

421
C)
The instrument shall be calibrated before use
on each day of its use by the methods
specified in Method 21.
D)
Calibration gases shall be:
1)
Zero air (less than loppm of hydrocarbon
in air); and
ii)
A mixture of methane or n—hexane and air
at a concentration of approximately, but
no less than,
10,000 ppm methane or
n—hexane.
E)
The instrument probe shall be traversed
around all potential leak interfaces as close
to the interface as possible as described in
Method 21.
2)
When equipment
is tested for compliance with no
detectable emissions as required, the test shall
comply with the following requirements:
A)
The requirements of subsections
(g) (1) (A)
through
(g) (1) (E)
of this Section above shall
apply.
B)
The background level shall be determined as
set forth in Method 21.
3)
Leak detection tests shall be performed consistent
with:
A)
“APTI Course SI 417 controlling Volatile
Organic Compound Emissions from Leaking
Process Equipment”,
EPA—450/2—82—0l5,
incorporated by reference in Section 219.112
of this Part.
B)
“Portable Instrument User’s Manual for
Monitoring VO~jSources”, EPA-340/
1—86-015,
incorporated by reference in Section 219.112
of this Part.
C)
“Protocols for Generating Unit-Specific
Emission Estimates for Equipment Leaks of
VOGN
and VHAP”,
EPA-450/3-88-010,
incorporated by reference in Section 219.112
of this Part.

422
D)
“Petroleum Refinery Enforcement Manual”,
EPA-340/1-80-008,
incorporated by reference
in Section 219.122219.112 of this Part.
h)
Bulk Gasoline Delivery System Test Protocol
1)
The method for determining the emissions of
gasoline from a vapor recovery system are
delineated in 40 CFR 60, Subpart XX, Section
60.503,
incorporated by reference in Section
219.112 of this Part.
2)
Other tests shall be performed consistent with:
A)
“Inspection Manual for Control of Volatile
Organic Emissions from Gasoline Marketing
Operations:
Appendix D”, EPA-340/ 1—80-012,
incorporated by reference in Section 219.112
of this Part.
B)
“Control of Hydrocarbons from Tank Truck
Gasoline Loading Terminals:
Appendix A”,
EPA-450/2-77-026,
incorporated by reference
in Section 219.112 of this Part.
i)
Notwithstanding other requirements of this Part, upon
request of the Agency where it is necessary to
demonstrate compliance,
an owner or operator of an
emission courcc unit which is subject to this Part
shall,
at his own expense, conduct tests
in accordance
with the applicable test methods and procedures
specific in this Part.
Nothing in this Section shall
limit the authority of the USEPA pursuant to the Clean
Air Act,
as amended,
to require testing.
j~
Stage II Gasoline Vapor Recovery Test Methods
The methods for determining the acceptable performance
of Stage II Gasoline Vapor Recovery System are
delineated in “Technical Guidance-Stage II Vapor
Recovery Systems for Control of Vehicle Refueling
Emissions at Gasoline Dispensing Facilities,” found at
EPA 450/3-9l-022b and incorporated by reference in
Section 219.112 of this Part.
Specifically, the test
methods are as follows:
~j
Dynamic Backpressure Test is a test procedure used
to determine the pressure drop (flow resistance)
through balance vapor collection and control
systems
(including nozzles, vapor hoses, swivels,
dispenser piping and underground piping)
at
prescribed flow rates.

423
21
Pressure Decay/Leak Test is a test procedure used
to quantify the vapor tightness of a vapor
collection and control system installed at
gasoline dispensing facilities.
fl
Liquid Blockage Test is a test procedure used to
detect low points
in any vapor collection and
control system where condensate may accumulate.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.106
Compliance Dates
Compliance with the requirements of all rules
is required by May
15,
1992,
consistent with the provisions of Section 219.103 ~i
this Part.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
_________________________)
Section 219.107
Operation of Afterburners
The operation of any natural gas fired afterburner and capture
system used to comply with this Part is not required during the
period of November
1 of any year to April
1 of the following year
provided that the operation of such devices is not required for
purposes of occupational safety or health, or for the control of
toxic substances,
odor nuisances,
or other regulated pollutants.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.109
Vapor Pressure of Volatile Organic Liquids
a)
If the VOL consists of only a single compound, the
vapor pressure shall be determined by ASTN Method
D2879-86 (incorporated by reference in Section 219.112
of this Part)
or the vapor pressure may be obtained
from a publi3hcd 3ourcepublication such as:
Boublik,
T.,
V.
Fried and E.
Hala,
“The Vapor Pressure of Pure
Substances,” Elsevier Scientific Publishing Co., New
York
(1973); Perry’s Chemical Engineer’s Handbook,
McGraw-Hill Book Company
(1984); CRC Handbook of
Chemistry and Physics, Chemical Rubber Publishing
Company
(1986-87); and Lange’s Handbook of Chemistry,
John A. Dean,
editor, McGraw-Hill Book Company
(1985).
b)
If the VOL is
a mixture, the vapor pressure shall be
determined by ASTN Method D2879—86
(incorporated by
reference in Section 219.112 of this Part)
or by the
following equation:

424
n
P~01
=
E
P1
X.
i=l
where:
=
Total vapor pressure of the mixture-i-;
n
=
Number of components in the mixtureT~
I
=
Subscript denoting an individual
component~~
P1
=
Vapor pressure of a component determined
in accordance with Subpart A of this
Partsubsection
(a)
of this Section
X~
=
Mole fraction of the component In the
total mixture.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.110
Vapor Pressure of Organic Material or Solvent
a)
If the organic material or solvent consists of only a
single compound, the vapor pressure shall be determined
by ASTN Method D2879-86 (incorporated by reference in
Section 219.112 of this Part) or the vapor pressure may
be obtained from a publishcd sourcepublication such as:
Boublik,
T.,
V.
Fried and E. Hala,
“The Vapor Pressure
of Pure Substances,” Elsevier Scientific Publishing
Co., New York (1973);
Perry’s Chemical Engineer’s
Handbook, McGraw-Hill Book Company
(1984); CRC Handbook
of Chemistry and Physics, Chemical Rubber Publishing
Company
(1986-87); and Lange’s Handbook of Chemistry,
John A. Dean,
editor, McGraw-Hill Book Company
(1985).
b)
If the organic material or solvent is in a mixture made
up of both organic material compounds and compounds
which are not organic material, the vapor pressure
shall be determined by the following equation:
n
E
P1X1
~om
1=1
n
R
X1
i=l
where:

425
=
Total vapor pressure of the portion of
the mixture which is composed of organic
mater ia 1-ri
n
=
Number of organic material components
in
the mixture-7-j
=
Subscript denoting an individual
component~~
P1
=
Vapor pressure of an organic material
component determined in accordance with
Subpart A of thi~3Partsubsection
(a)
of
this Section-~-j
X•
=
Mole fraction of the organic material
component of the total mixture.
c)
If the organic material or solvent is in a mixture made
up of only organic material compounds, the vapor
pressure shall be determined by ASTM Method D2879-86
(incorporated by reference in Section 219.112 of this
Part)
or by the above equation.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.111
Vapor Pressure of Volatile Organic Material
a)
If the VON consists of only a single compound, the
vapor pressure shall be determined by ASTN Method
D2879-86 (incorporated by reference in Section 219.112
of this Part)
or the vapor pressure may be obtained
from a publishcd sourcepublication such as:
Boublik,
T.,
V.
Fried and E.
Hala,
“The Vapor Pressure of Pure
Substances,” Elsevier Scientific Publishing Co., New
York
(1973); Perry’s Chemical Engineer’s Handbook,
McGraw-Hill Book Company
(1984); CRC Handbook of
Chemistry and Physics, Chemical Rubber Publishing
Company
(1986-87);
and Lange’s Handbook of Chemistry,
John A. Dean,
editor, McGraw-Hill Book Company
(1985).
b)
If the VOM is
in a mixture made up of both VON
compounds and compounds which are not VON, the vapor
pressure shall be determined by the following equation:

426
n
Z
P1X,
~vom
i=1
n
E
X1
i=1
where:
=
Total vapor pressure of the portion
of the mixture which is composed of
VOM~j.
n
=
Number of VON components in the
mixture7~
i
=
Subscript denoting an individual
component,-j.
P1
=
Vapor pressure of a VON component
determined in accordance with
Subpart A of this Partsubsection
(a)
of this SectionTj
=
Mole fraction of the VON component
of the total mixture.
c)
If the VOM is in a mixture made up of only VON
compounds,
the vapor pressure shall be determined by
ASTM Method D2879-86
(incorporated by reference in
Section 219.112 of this Part)
or by the above equation.
(Source:
Amended at
Ill.
Reg.
______,
effective
___________
Section 219.112
Incorporations by Reference
The following materials are incorporated by reference and do not
contain any subsequent additions or amendments:
a)
American Society for Testing and Materials,
1916 Race
Street, Philadelphia, PA 19103:
1)
ASTN
D2879—86
2)
ASTN D323—82
3)
ASTM
D86—82
4)
ASTM D—369—69
(1971)
5)
ASTN D—396—69
6)
ASTN
D2880—7l
7)
ASTN
D—975—68

427
8)
ASTN D3925—8l
(1985)
9)
ASTM E300—86
10)
ASTM Dl475—85
11)
ASTM
D2369—87
12)
ASTM
D3792—86
13)
ASTM D4017—81
(1987)
14)
ASTM D4457—85
15)
ASTM D2697—86
16)
ASTM D3980—87
17)
ASTM El80—85
18)
ASTN D2372—85
19)
ASTM D97—66
20)
ASTM E—168—87
(1977)
21)
ASTN E—169~i
22)
ASTM E—260.~~.
23)
ASTM D2504—83
24)
ASTM D2382—83
2~I
ASTM D323-82
(approved 1982)
b)
Standard Industrial Classification Manual, published by
Executive Office of the President, Office of Management
and Budget, Washington,
D.C.,
1987.
c)
American Petroleum Institute Bulletin 2517,
“Evaporation Loss From Floating Roof Tanks”, Second
ed., February,
1980.
d)
40 CFR Part 60
(July
1,
19901991)
and 40 CFR 60,
Appendix A, Method 24
(57 FR 30654, July 10,
1992).
e)
40 CFR Part 61
(July
1,
19901991)
f)
40
CFR
Part 50
(July
1,
19891991)
g)
40 CFR Part 51
(July
1,
19891991)
h)
40
CFR
Part
52
(July
1,
19891991)
jj
40 CFR Part 80
(July
1,
1991)
-)-jJ
“A Guide for Surface Coating Calculation”, United
States Environmental Protection Agency, Washington,
D.C.,
EPA—340/1—86—016.
+)-~ç1“Procedures for Certifying Quantity of Volatile Organic
Compounds
Emitted by Paint,
Ink and Other Coating”,
(revised June 1986). United States Environmental
Protection Agency, Washington D.C.,
EPA-450/3-84-0l9.
~-)-fl “A Guide for Graphic Arts Calculations”, August 1988,
United States Environmental Protection Agency,
Washington D.C.,
EPA-340/l-88-003.

428
-~-)-~j“Protocol for Determining the Daily Volatile Organic
Compound Emission Rate of Automobile and Light-Duty
Truck Topcoat Operations”, December 1988, United States
Environmental Protection Agency, Washington D.C.,
EPA—450/3—88—018.
~-)-~j“Control of Volatile Organic Emissions from
Manufacturing of Synthesized Pharmaceutical Products”,
United States Environmental Protection Agency,
Washington, D.C.,
EPA-450/2—78—029.
~-)-~j“Control of Volatile Organic Compound Leaks from
Gasoline Tank Trucks and Vapor Collection Systems”,
Appendix B, United States Environmental Protection
Agency, Washington,
D.C., EPA-450/2-78—05l.
e)-pj “Control of Volatile Organic Compound emissions from
Large Petroleum Dry Cleaners”, United States
Environmental Protection Agency, Washington, D.C.,
EPA—450/3—82—009.
~
“APTI Course SI417 Controlling Volatile Organic
Compound Emissions from Leaking Process Equipment”,
United States Environmental Protection Agency,
Washington,
D.C.,
EPA—450/2—82—0l5.
~j
“Portable Instrument User’s Manual for Monitoring VON
Sources”, United States Environmental Protection
Agency, Washington,
D.C.,
EPA-340/l—86-015.
~J
“Protocols for Generating Unit—Specific Emission
Estimates for Equipment Leaks of VON and
VHAP”,
United
States Environmental Protection Agency, Washington,
D.C.,
EPA—450/3—88—OlO.
~j
“Petroleum Refiner.y Enforcement Manual”, United States
Environmental Protection Agency, Washington, D.C.,
EPA—340/l—80—008.
~3j
“Inspection Manual for Control of Volatile Organic
Emissions from Gasoline Marketing Operations:
Appendix
D”, United States Environmental Protection Agency,
Washington,
D.C.,
EPA—340/1—80—012.
~
“Control of Hydrocarbons from Tank Truck Gasoline
Loading Terminals:
Appendix A”, United States
Environmental Protection Agency, Washington,
D.C.,
EPA—450/2—77—026.
~
“Technical Guidance—Stage II Vapor Recovery Systems for
Control of Vehicle Refueling Emissions at Gasoline

429
Dispensing Facilities”, United States Environmental
Protection Agency, Washington,
D.C.,
EPA-450/3—91—022b.
~çj. California Air Resources Board,
Compliance Division.
Compliance Assistance Program:
Gasoline Marketing and
Distribution:
Gasoline Facilities Phase
I
&
II
(October 1988,
rev. March 1991)
(CARB Manual).
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
SUBPART B:
ORGANIC EMISSIONS FROM STORAGE
AND
LOADING OPERATIONS
Section 219.121
Storage Containers
No person shall cause or allow the storage of any VOL with a
vapor pressure of 17.24 kPa (2.5 psia)
or greater at 294.3°K
(70°F) or any gaseous organic material in any stationary tank,
reservoir or other container of more than 151 cubic meters
(40,000 gal) capacity unless such tank, reservoir or other
container:
a)
Is a pressure tank capable of withstanding the vapor
pressure of such liquid or the pressure of the gas,
so
as to prevent vapor or gas loss to the atmosphere at
all times;
or,
b)
Is designed and equipped with one of the following
vapor loss control devices:
1)
A floating roof which rests on the surface of the
VOL and is equipped with a closure seal or seals
between the roof edge and the tank wall.
Such
floating roof shall not be permitted if the VOL
has a vapor pressure of 86.19 kPa
(12.5 psia)
or
greater at 294.3°K(70°F). No person shall cause
or allow the emission of air contaminants into the
atmosphere from any gauging or sampling devices
attached to such tanks,
except during sampling or
maintenance operations.
2)
A vapor recovery system consisting of:
A)
A vapor gathering system capable of
collecting 85
or more of the uncontrolled
VON that would be otherwise emitted to the
atmosphere;
and,
B)
A vapor disposal system capable of processing
such VON so as to prevent its emission to the
atmosphere.
No person shall cause or allow
the emission of air contaminants into the

430
atmosphere from any gauging or sampling
devices attached to such tank, reservoir or
other container except during sampling.
3)
Other equipment or means of equal efficiency
approved by the Agency according to the provisions
of
35 Ill.
Adrn.
Code 201,
and further processed
consistent with Section 219.108 of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.122
Loading Operations
a)
No person shall cause or allow the discharge of more
than 3.6 kg/hr
(8
lbs/hr)
of organic material into the
atmosphere during the loading of any organic material
from the aggregate loading pipes of any loading
facilityarea having through-put of greater than 151
cubic meters per day (40,000 gal/day)
into any railroad
tank car, tank truck or trailer unless such loading
facilityarea
is equipped with submerged loading pipes~
oubnicrgcd fill or a device that is equally effective in
controlling emissions and is approved by the Agency
according to the provisions of
35
Ill. Adm. Code 201,
and further processed consistent with Section 219.108
of this Part.
b)
No person shall cause or allow the loading of any
organic material into any stationary tank having a
storage capacity of greater than 946
1
(250 gal),
unless such tank is equipped with
a permanent submerged
loading pipe,
submcrgcd fill or an equivalent device
approved by the Agency according to the provisions of
35
Ill. Adm. Code 201, and further processed consistent
with Section 219.108 of this Part,
or unless such tank
is
a pressure tank as described in Section 219.121(a)
of this Part or is fitted with a recovery system as
described in Section 219.121(b) (2)
of this Part.
C)
Exception:
If no odor nuisance exists the limitations
of this Section shall only apply to the loading of VOL
with a vapor pressure of 17.24 kPa
(2.5 psia)
or
greater at 294.3°K(70°F).
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.123
Petroleum Liquid Storage Tanks
a)
The requirements of subsection
(b)
of this Section
shall not apply to any stationary storage tank:

431
1)
Equipped before January
1,
1979 with one of the
vapor loss control devices specified in Section
219.121(b)
of this Part,
except Section
219.121(b) (1)
of this Part
2)
With
a capacity of less than 151.42 cubic meters
(40,000 gal);
3)
With
a capacity of less than 1,600 cubic meters
(422,400 gal)
and used to store produced crude oil
arid condensate prior to custody transfer;
4)
With
a capacity of less than 1,430 cubic meters
(378,000 gal)
and used to store produced oil or
condensate
in crude oil gathering;
5)
Subject to new source performance standards for
storage vessels of petroleum liquid,
35
Ill.
Adm.
Code 230
40 CFR 60,
as regulations promulgated by
the U.S. Environmental Protection Agency under
Section
111 of the Clean Air Act
(42 USC 7411)
,
as
amended.
THE PROVISIONS OF SECTION
111 OF THE
CLEAN AIR ACT
...
ARE APPLICABLE IN THIS STATE AND
ARE ENFORCEABLE UNDER THE ENVIRONMENTAL PROTECTION
ACT
(Ill.
Rev.
Stat.
1991,
ch. 11l~, Par.
1009.1(b))
1415 ILCS
5/9.1(b))
6)
In which volatile petroleum liquid
is not stored;
or
7)
Which
is
a pressure tank as described
in Section
219.121(a)
of this Part.
b)
Subject to subsection
(a)
of this Section no owner
or
operator of
a stationary storage tank shall cause or
allow the storage of any VOL in the tank unless:
1)
The tank
is equipped with one of the vapor
loss
control devices specified
in Section 219.121(b)
~
this Part
2)
There are no visible holes, tears
or other defects
in the seal
or any seal fabric or material
of any
floating roof;
3)
All openings
of any floating roof deck,
except
stub drains,
are equipped with covers,
lids or
seals such that:
A)
The cover,
lid or seal
is
in the closed
position at all times except when petroleum
liquid
is transferred to or from the tank;

432
B)
Automatic bleeder vents are closed at all
times except when the roof
is floated off or
landed on the roof leg supports;
and
C)
Rim vents,
if provided,
are set to open when
the roof
is being floated off the roof leg
supports or at the manufacturer’s recommended
setting;
4)
Routine inspectic:~sof floating roof seals are
conducted through roof hatches once every six
months;
5)
A complete inspection of the cover and seal of any
floating roof tank is made whenever the tank is
emptied for reasons other than the transfer of
petroleum liquid during the normal operation of
the tank,
or whenever repairs are made as a result
of any semi—annual inspection or incidence of roof
damage or defect; and
6)
A record of the results
of each inspection
conducted under subsection
(b) (4)
or
(b) (5)
of
this Section is maintained.
c)
Owners and operators
of petroleum liquid storage tanks
wcrc required to have compliance
schedules as
summarized
in Appendix C to
35 Ill Adm.
Code
2-1-s.
(Source:
Amended
at
______
,
Ill.
Reg.
_____
,
effective
Section 219.124
External Floating Roofs
a)
In addition to meeting the requirements
of Section
219.123(b)
of this Part,
no owner or operator of
a
stationary storage tank equipped with an external
floating roof shall cause or allow the storage of any
volatile petroleum liquid in the tank unless:
1)
The tank has been fitted:
~j.
fitted wWith a continuous secondary seal
extending from the floating roof to the tank
wall
(rim mounted secondary seal)~or
~J
With any other
with
an ofreotiveness equal to or
~-~‘-
secondary seal;
-
A A~
I
I
~
A”
I~
equipment
or means of equal efficiency
approved
by
the Agency according to the
provisions
of
35
Ill.
Adn.
Code
201,
and

433
further processed consistent with Section
219.108
of this Part.
2)
Each seal closure device meets the following
requirements:
A)
The seal is intact and uniformly
in place
around the circumference of the floating roof
between the floating roof and tank wall; and
B)
The accumulated area of gaps exceeding 0.32
centimeter
(1/8
inch)
in width between the
secondary seal and the tank wall shall not
exceed 21.2
square centimeters per meter of
tank diameter
(1.0 square inche-s per foot of
tank diameter).
Compliance with this
requirement shall be determined
by:
~jj
Physically measuring the length and
width of all gaps around the entire
circumference of the secondary seal
in
each place where
a 0.32
cm
(0.125
in.)
uniform diameter probe passes freely
(without forcing or binding against the
-
seal)
between the seal and the tank
wall;
and
ii)
Summing the area of the individual gaps.
3)
Emergency roof drains are provided with slotted
membrane fabric covers or equivalent covers across
at least
90 percent of the area of the opening;
4)
Openings are equipped with projections into the
tank which remain below the liquid surface at all
times;
5)
Inspections are conducted prior
to May
1 of each
year to insure compliance with subsection
(a)
this Section
6)
The secondary seal gap
is measured prior to May
1
of each year~and within
30 days of
a written
request to demonstrate compliance with subsection
(2) (B)
of this
Sectiorij
7)
Records
of the types of volatile petroleum liquid
stored, the maximum true vapor pressure of the
liquid as stored,
the results of the inspections
and the results
of the secondary seal gap
measurements are maintained and available to the
Agency, upon verbal or written request,
at any

434
reasonable time for
a minimum of two years after
the date on which the record was made.
b)
Subsection
(a)
above does not apply to any stationary
storage tank equipped with an external floating roof:
1)
Exempted under Section 219.123(a) (2)
through
219.123
(a) (6)
of this Part
-
2)
Of
welded construction equipped with
a metallic
type shoe seal having a secondary seal from the
top of the shoe seal to the tank wall
(shoe—mounted secondary seal);
3)
Of welded construction equipped with a metallic
type shoe seal,
a liquid-mounted foam seal,
a
liquid-mounted liquid-filled-type seal,
or other
closure device of equivalent control efficiency
approved by the Agency
in which
a petroleum
liquid
with
a true vapor pressure less than 27.6 kPa
(4.0
psia)
at 294.3°K (70°F) is stored;
or
4)
Used to store crude oil with a pour point of 50°F
or higher as determined by ASTM Standard D97—66
incorporated by reference
in Section 219.112
of
this Part.
-
(Source:
Amended at
Ill.
Reg.
-
,
effective
____________
Section 219.125
Compliance Dates
(Repealed)
~
owner
or operator of an em~~onsource sub~~
Adm.
Code
215,
Subpart
B,
as of December
31,
1987
shall have
complied with its standards and limitations by December
31,
1967.
(Source:
Repealed at
Ill.
Reg.
______
,
effective
___________
Section 219.126
Compliance Plan
(Repealed)
e-)-
The owner
or operator of an emission source previously
subject to Section 215.125 shall have submitted to the
Agency
a compliance plan as required by
35
III. Adm.
Code 201.241,
including
a project completion schedule
whore applicable,
no later than April
21,
1983.
~
Unless the submitted compliance plan or schedule was
~~oved
by the Agency,
the owner or operator o~—a
~
subject
to the rules
specified
in ~ub~pptipn
(a) may operate the emission
source according
to the plan and schedule as submitt-e~-~-

435
e-)-
The plan and schedule shall meet the requirements of—9~
Ill.
Adm.
Code 201.241 including specific interim dates
as required in 35
Ill.
Adm.
Code 201.242.
(Source:
Repealed at —
Ill.
Reg.
______
,
effective
___________
SUBPART
C:
ORGANIC EMISSIONS FROM MISCELLANEOUS EQUIPMENT
Section 219.141
Separation Operations
a)
No person shall use any single or multiple compartment
effluent water separator which receives effluent water
containing
757 1/day
(200 gal/day)
or more of organic
material from any equipment processing,
refining,
treating,
storing or handling organic material unless
such effluent water separator
is equipped with air
pollution control equipment capable of reducing by
85
percent or more the uncontrolled organic material
emitted to the atmosphere.
Exception:
If no odor
nuisance exists the limitations
of this subsection
shall not apply if the vapor pressure of the organic
material
is below 17.24 kPa
(2.5 psia)
at 294.3°K
(70°F)
b)
Subsection
(a)
of this Section shall not apply to water
and crude oil separation
in the production of Illinois
crude
oil,
if the vapor pressure of
such crude oil
is
less than 34.5 kPa
(5 psia)
(Source:
Amended at
______
,
Ill.
Reg.
_____
,
effective
Section 219.143
Vapor Blowdown
No person shall cause or allow the emission of organic material
into the atmosphere
from any vapor blowdown system or any safety
relief valve,
except such safety relief valves not capable of
causing an excessive release, unless such emission
is controlled:
a)
To
10 ppm equivalent methane
(molecular weight
16.0)
or
less;
or,
b)
By combustion
in
a smokeless
flare;
or,
c)
By other air pollution control equipment approved by
the Agency according to the provisions
of
35
Ill.
Adm.
Code
201,
and further processed consistent with Section
219.108
of this Part.
(Source:
Amended at —
Ill.
Reg.
______
,
effective

436
Section 219.144
Safety Relief Valves
Section 219.143
of this Part shall not apply to any set of
unregulated safety relief valves capable of causing excessive
releases, provided the owner or operator thereof,
by October
1,
1972,
supplied the Agency with the following:
a)
A historical record of each such set
(or,
if such
records were unavailable,
of similar sets which,
by
virtue of operation under similar circumstances, may
reasonably have been presumed to have the same or
greater frequency of excessive releases)
for a
three-year period immediately preceding October
1,
1972,
indicating:
1)
Dates
on which excessive releases occurred from
each such set;
andT
2)
Duration
in minutes of each such excessive
release; andT
-
3)
Quantities
(in pounds)
of mercaptans and/or
hydrogen sulfide emitted into the atmosphere
during each
such excessive release.
b)
Proof,
using such three—year historical records, that
no -excessive release
is likely to occur from any
such
set either alone or
in combination with such excessive
releases from other sets owned or operated by the same
person and located within
a ten-mile radius from the
center point of any such
set, more frequently than
3
times
in any
12 month period;
c)
Accurate maintenance records pursuant to the
requirements
of subsection
(a)
of this Section
and,
d)
Proof,
at three-year
intervals,
using such three—year
historical records,
that such set conforms to the
requirements
of subsection
(c)
of this Section.
(Source:
Amended at
Ill. Reg.
______
,
effective
-
SUBPART
E:
SOLVENT -CLEANING
Section 219.181
Solvent Cleaning
in General
The requirements
of this
Subpart shall apply to all cold
cleaning,
open top vapor degreasing,
and conveyorized degreasing
operations which use volatile organic materials.

437
(Source:
Amended at
Ill. Reg.
______
,
effective
__________
Section 219.182
Cold Cleaning
a)
Operating Procedures:
No person shall operate
a cold
cleaning degreaser unless:
1)
Waste solvent is stored in covered containers
only
and not disposed of in such
a manner that more
than 20
of the waste solvent
(by weight)
is
allowed to evaporate into the atmosphere;
2)
The cover of the degreaser
is closed when parts
are not being handled; and
3)
Parts are drained until dripping ceases.
b)
Equipment Requirements:
No person shall operate
a cold
cleaning degreaser unless:
1)
The degreaser is equipped with
a cover which
is
closed whenever parts are not being handled
in the
cleaner.
The cover shall be designed to be easily
operated with one hand or with the mechanical
assistance
of springs, counter-weights
or
a
powered system if:
A)
The solvent vapor pressure
is greater than
2
kPa
(15 inmHg or 0.3 psi) measured at 38°C
(100°F);
B)
The solvent
is agitated;
or
C)
The solvent is heated above ambient room
temperature.
2)
The degreaser is equipped with
a facilitydevice
for draining cleaned parts.
The drainage
facilitydevice shall be constructed so that parts
are enclosed under the cover while draining
unless:
A)
The solvent vapor pressure is less than 4.3
kPa
(32 mmnHg or 0.6 psi) measured at 38°C
(100°F); or
B)
An internal drainage facilitydevice cannot be
fitted into the cleaning system,
in which
case the drainage facilitydevice may be
external.

438
3)
The degreaser is equipped with one of the
following control devices if the vapor pressure
of
the solvent
is greater than 4.3 kPa
(32
mmig
or
0.6 psi)
measured at 38°C(100°F) or
if the
solvent
is heated above 50°C(120°F) or its
boiling point:
A)
A freeboard height of 7/10 of the inside
width of the tank or 91 cm
(36 in), whichever
is
less;
or
B)
Any other equipment or
system
of equivalent
emission control as approved by the Agency
and further processed consistent with Section
219.108
of this Part.
Such a system may
include
a water cover, refrigerated chiller
or carbon adsorber.
4)
A permanent conspicuous label
summarizing the
operating procedure
is affixed to the degreaser;
and
5)
If
a solvent spray is used,
the degreaser
Is
equipped with a solid fluid stream spray,
rather
than a fine,
atomized or shower spray.
(Source:
Amended at
______
,
Ill.
Reg.
_______
,
effective
Section 219.183
Open Top Vapor Degreasing
a)
Operating Requirements:
No person shall operate an
open top vapor degreaser unless:
1)
The cover of the degreaser
is closed when
workloads are not being processed through the
degreaser;
2)
Solvent carryout emissions are minimized
by:
A)
Racking parts to allow complete drainage;
B)
Moving parts in and out of the degreaser
at
less than
3.3 m/min
(11 ft/mm);
C)
Holding the parts
in the vapor zone until
condensation ceases;
D)
Tipping out any poo1s of solvent on the
cleaned parts before removal from the vapor
zone;
and

439
E)
Allowing parts
to dry within the degreaser
until visually dry.
3)
Porous or absorbent materials,
such as cloth,
leather, wood or rope are not degreased;
4)
Less than half
of the degreaser’s open top area is
occupied with a workload;
5)
The degreaser is not loaded to the point where the
vapor level would drop more than
10 cm
(4
in) when
the workload is removed from the vapor
zone;
6)
Spraying
is done below the vapor level only;
7)
Solvent leaks are repaired immediately;
8)
Waste solvent
is stored
in covered containers
only
and not disposed of
in such a manner that more
than 20
of the waste solvent
(by weight)
is
allowed to evaporate into the atmosphere;
9)
Water is not visually detectable
in solvent
exiting from the water separator;
and
10)
Exhaust ventilation exceeding 20 cubic meters per
minute per square meter
(65 cubic feet per minute
per square foot)
of degreaser open area
is not
used,
unless necessary to meet the requirements
of
the Occupational Safety and Health Act
(29 U.S.C.
Section
651 et seq.).
b)
Equipment Requirements:
No person shall operate an
open top vapor degreaser unless:
1)
The degreaser
is equipped with
a cover designed to
open and close easily without disturbing the vapor
zone;
2)
The degreaser
is equipped with the following
switches:
A)
A deviceOne which shuts off the sump heat
source
if the amount of condenser coolant
is
not sufficient to maintain the designed vapor
level; and
B)
A
dcviceOne which shuts off the spray pump if
the vapor level drops more than
10 cm
(4
in)
below the bottom condenser coil;
and

440
C)
A dcviccQ~ which shuts off the sump heat
source when the vapor
level exceeds the
design level.
3)
A permanent conspicuous
label summarizing the
operating procedure
is affixed to the degreaser;
4)
The degreaser
is equipped with one of the
following devices:
A)
A freeboard height of
3/4
of the inside width
of the degreaser tank
or 91
cm
(36
in)
whichever
is less;
and if the degreaser
opening
is greater than
1 square meter
(10.8
ft2)
,
a powered or mechanically assisted
cover;
or
B)
Any other equipment or system of equivalent
emission control
as approved by the
Agency
and further processed consistent with Section
219.108 of this Part.
Such equipment or
system may include
a refrigerated
chiller,
an
enclosed design or
a carbon adsorption
system.
(Source:
Amended
at
_____
,
Ill.
Reg.
______
,
effective
Section 219.164
Conveyorized Degreasing
a)
Operating Requirements:
No person shall operate
a
conveyorized degreaser unless:
1)
Exhaust ventilation exceeding 20 cubic meters per
minute per square meter
(65 cubic feet per minute
per square foot)
of area
of loading and unloading
opening is not used,
unless necessary to meet the
requirements
ef the Occupational Safety and Health
Act
(29 U.S.C.
Section 651 et seq.);
2)
Solvent carryout emissions are minimized by:
A)
Racking parts for best drainage;
and
B)
Maintaining the vertical conveyor speed at
less than 3.3 m/min
(11 ft/mm);
3)
Waste solvent
is stored
in covered containers only
and not disposed of
in such
a manner that more
than 20
of the waste solvent
(by weight)
is
allowed to evaporate into the atmosphere;

441
4)
Solvent leaks are repaired immediately;
5)
Water
is not visually detectable
in solvent
exiting from the water separator; and
6)
Downtime covers are placed over entrances and
exits
of conveyorized degreasers immediately after
the conveyers and exhausts are shut down and not
removed until ju:-~before start-up.
b)
Equipment Requirements:
No person shall operate a
conveyorized degreaser unless:
1)
The degreaser
is equipped with a drying tunnel,
rotating
(tumbling)
basket or other equipment
sufficient to prevent cleaned parts from carrying
out solvent liquid or vapor;
2)
The degreaser is equipped with the following
switches:
A)
A dcviceQ~ which shuts off the sump heat
source
if the amount of condenser coolant
is
not sufficient to maintain the designed vapor
level;
B)
A dcviceQ~ which shuts off the spray pump or
the conveyor
if the vapor level drops more
than
10 cm
(4
in)
below the bottom condenser
coil;
and
C)
A deviceOné which shuts off the sump heat
source when the vapor level exceeds the
design level;
3)
The degreaser is equipped with openings for
entrances and exits that silhouette workloads
so
that the average clearance between the parts and
the edge of the degreaser opening is less than
10
cm
(4
in)
or
less than 10 percent of the width
of
the opening;
4)
The degreaser is equipped with downtime covers for
closing off entrances and exits when the degreaser
is shut down; and
5)
The degreaser is equipped with one of the
following control devices,
if the air/vapor
interface
is larger than 2.0 square meters
(21.6
ft2)

442
A)
A carbon adsorption system with ventilation
greater than or equal to
15 cubic meters per
minute per square meter
(50 cubic feet per
minute per square foot)
of air/vapor area
when downtime covers are open,
and exhausting
less than
25 ppm of solvent by volume
averaged over
a complete adsorption cycle;
or
B)
Any other equipment or system of equivalent
emission control
as approved by the Agency,
and further processed consistent with Section
219.108 of this Part.
Such equipment or
system may include
a refrigerated chiller.
(Source:
Amended at
_____
,
Ill.
Reg.
______
,
effective
Section 219.185
Compliance Schedule
(Repealed)
.---~--
previously exempt from the requirements
of Subpart E of
35 Ill.
Adm.
Code 215
(Sections 215.182-215.184)
because
it satisfied the
criteria
in either
35
Ill.
Adm.
Code 215.181(a)
or 35
Ill.
Adm.
Code 215.181(b),
shall comply with the requirements of this
Subpart
on and after a date consistent with Section 219.106.
A
source which did not satisfy the sritcria
in
a4-th-ar 35
Ill. Adm.
Code 215.181(a)
or 35
Ill.
Adm.
Code 215.181(b)
shall comply with
the requirements
of this Subpart
irnon adoption.
(Source:
Repealed at
Ill.
Reg.
______
,
effective
___________
Section 219.186
Test Methods
The following test methods shall be used to demonstrate
compliance with this Subpart:
a)
Vapor pressures shall be determined
by using the
procedure specified
in Section 219.110 of this Part.
b)
Exhaust ventilation rates shall be determined -by using
the procedures specified in Section 219.105(f) (3) ~
this Part.
c)
The performance of control devices shall be determined
-
by using the procedures specified
in Section 219.105(f)
of this Part.
(Source:
Amended at
_____
,
Ill. Reg.
______
,
effective
__________
)

443
SUBPART F:
COATING OPERATIONS
Section 219.204
Emission Limitations for Manufacturing Plants
Except as provided
in Section~219.205,
219.207 and 219.208
of
this Part,
no owner or operator of
a coating line shall apply
at
any time any coating in which the VOM content exceeds the
following emission limitations for the specified coating.
The
following emission limitations are expressed
in units of VOM per
volume of coating
(minus water and any compounds which are
specifically exempted from the definition of VOM)
as app-lied at
each coating applicator,
except where noted.
Compounds which are
specifically exempted from the definition of VOM should be
treated as water for the purpose
of calculating the “less water”
part of the coating composition.
Compliance with this Subpart
must be demonstrated through the applicable coating analysis test
methods and procedures specified
in Section 219.105(a)
of this
Part and the recordkeeping and reporting requirements specified
in Section 219.211(c)
of this Part.
(Note:
The equation
presented
in Section 219.206
of this Part shall be used to
calculate emission limitations for determining compliance by
add—on controls,
credits for transfer efficiency,
emissions
trades and cross-line averaging.)
The emission limitations are
as follows:
a)
Automobile or Light-Duty Truck Coating
kg/l
lb/gal
1)
Prime coat
-
0.14
(1.2)
2)
Primer surfacer coat
p.341.81
(-2--r&15.l)
(Note:
The primer surfacer coat limitation
is
based upon
a transfer efficiency
of
30 percent.
The usc of transfer efficiency
credits can ~e
allowed only
if approved by the Agency and
approved by the USEPA as
a SIP revisionin units
of
kg
(lbs)
of VON per
1
(gal)
of coating solids
deposited.
Compliance with the limitation shall
be based on the daily-weighted average from an
entire primer surfacer operation.
Compliance
shall
be demonstrated
in accordance with the
topcoat protocol referenced
in Section 219.105(b)
and the recordkeeping and reporting requirements
specified
in Section 219.211(f).
Testing to
demonstrate compliance shall be performed
in
accordance with the
topcoat protocol and a
detailed testing proposal approved by the A~enc~
and USEPA specifying the method of demonstratipg
compliance with the protocol.
Section 219.205
does not apply to the primer surfacer limitatio~

444
-
kg/l
lb/gal
3)
Topcoat
1.81
(15.1)
(Note:
The topcoat limitation
is
in units of kg
(lbs)
of VOM per
1
(gal)
of coating solids
deposited.
Compliance with the limitation shall
be based on the daily-weighted average VON content
from ~
entire topcoat operation
(all topcoat
spray booths,
flash—off areas and bake ovens).
Compliance shall
ae demonstrated
in accordance
with the topcoat protocol for automobiles and
light duty trucks referenced
in Section 219.105(b)
of this Part and the recordkeeping and reporting
requirements specified
in Section 219.211(f).
Testing to demonstrate compliance
shall be
performed
in accordance with the topcoat protocol
and Section 219.205 does
riot apply to the topcoat
limitation.)
At least
180 -days prior to the
-i-n-itial compliance date,
the owner or operator of
a coating line subject to the topcoat limitation
shall -have submitted to the USEPA a detailed
testing proposal approved by the Agency and USEPA
specifying the method
of demonstrating compliance
with the protocol.
The proposal shall
ha-va
included,
at
a minimum,
a comprehensive plan
(including
a rationale)
for determining the
transfer efficiency
at each booth through the usc
of in—plant,
or pilot testing; the selection of
coatings to be tested
(for the purpose of
determining transfer efficiency) including the
rationale for coating groupings;
and the -method
for determining the analytic VON con~11~
-~
applied
coati-rigs and the formulation solvent
content of
as applied coatings.
Upon approval of
~e
protocol by the USEPA,
the source may proceed
with the compliance demonstration.
Section
219.205
of this Part does not apply to the topcoat
limitation.)
kg/l
lb/gal
4)
Final repair coat
0.58
(4.8)
b)
Can Coating
kg/i
lb/gal
1)
Sheet basecoat and overvarnish 0.34
(2.8)
2)
Exterior basecoat and
overvarnish
0.34
(2.8)
3)
Interior body spray coat
0.51
(4.2)
4)
Exterior end coat
0.51
(4.2)

445
5)
Side seam spray coat
0.66
(5.5)
6)
-End sealing compound coat
0.44
(3.7)
kg/l
lb/gal
a)
Paper Coating
0.35
(2.9)
(Note:
The paper coating limitation shall not apply to
any owner or operator
of any paper coating line on
which printing
is performed
if the paper coating line
complies with the emissions limitations
in Subpart
H:
Printing and Publishing,
Sections 219.401 through
219.404.)of this Part.)
kg/l
lb/gal
d)
Coil Coating
0.31
(2.6)
e)
Fabric Coating
0.35
(2.9)
f)
Vinyl Coating
0.45
(3.8)
g)
Metal Furniture Coating
0.36
(3.0)
h)
Large Appliance Coating
0.34
(2.8)
(Note:
The limitation shall not apply to the use of
quick—drying lacquers for repair of scratches and nicks
that occur during assembly,
provided that the volume
of
coating does not exceed 0.95
1
(1 quart)
in any one
rolling eight—hour period.)
kg/l
lb/gal
i)
Magnet Wire Coating
0.20
(1.7)
j)
Miscellaneous Metal Parts and Products Coating
kg/l
lb/gal
1)
Clear coating
0.52
(4.3)
2)
Air—dried coating
0.42
(3.5)
3)
Extreme performance coating
0.42
(3.5)
jj.
Steel pail and drum
interior
coating
0.52
(4.3)
45)
All other coatings
0.36
(3.0)
k)
Heavy Off—Highway Vehicle Products Coating
kg/l
lb/gal
1)
Extreme performance prime coat
0.42
(3.5)
2)
Extreme performance top-coat

-
446
(air dried)
0.42
(3.5)
3)
Final repair coat
(air dried)
0.42
(3.5)
4)
All other coatings are subject to the emission
limitations for miscellaneous metal parts and
products coatings
in subsection
(j)
above.
1)
Wood Furniture Coating
kg/1
lb/gal
1)
Clear topcoat
0.67
(5.6)
2)
Opaque stain
0.56
(4.7)
3)
Pigmented coat
0.60
(5.0)
4)
Repair coat
0.67
(5.6)
5)
Sealer
0.67
(5.6)
6)
Semi—transparent stain
0.79
(6.6)
7)
Wash coat
0.73
(6.1)
(Note:
An owner or operator of a wood furniture
coating operation subject to this Section shall
-
apply all coatings, with the exception of no more
than 37.8
1
(10 gal)
of coating per day used for
touch-up and repair operations,
using one or more
of the following application systems:
airless
spray application system,
air-assisted airless
spray application system,
electrostatic spray
application system,
electrostatic bell or
disc-spray application system,
heated airless
spray application system,
roller coating,
brush
oi
wipe coating application system, e~dip coating
application system or high volume low pressure
(HVLP)
application system.)
-
(Source:
Amended at
Ill.
Reg.
_____
,
effective
_____________
Section 219.205
Daily—Weighted Average Limitations
No owner or operator of
a coating line subject to the limitations-
of Section 219.204
of this Part and complying by means
of this
Section shall operate the subject coating line unless the owner
or operator has demonstrated compliance with subsection~ (a)
(b),
(C),
(d)
,
(e)
or
(f)
of this Section
(depending upon the
source category of coating)
through the applicable coating
analysis test methods and procedures specified
in Section

447
-
219.105(a)
of this Part and the recordkeeping and reporting
requirements specified
in Section 219.211(d)
of this Part:
a)
No owner or operator of
a coating line subject to only
one of the
limitations from among Section 219.204(a) (1),
(a)(2),
(a)
(4)
,
(c)
,
(d)
,
(e)
,
(f)
,
(g)
,
(h)
,
or
(i)
of this
Part shall apply coatings on any such coating line,
during any day,
whose daily-weighted average VON
content exceeds the emission limitation to which the
coatings are subject.
b)
No owner or operator of
a miscellaneous metal parts and
products coating line subject to the limitations of
Section 219.204(j)
of this Part shall apply coatings to
miscellaneous metal parts or products on the subject
coating line unless the requirements
in subsection
(b) (1)
or
(b) (2)
of this Section below are met.
1)
For each coating
line which applies multiple
coatings,
all of which are subject to the same
numerical emission limitation within Section
219.204(j)
above, during the same day
(e.g.,
all
coatings
used. on the line are subject to 0.42 kg/l
3.5
lbs/gal)),
the daily-weighted average VON
content shall not exceed the coating VOM content
limit corresponding to the category of coating
used,
or
2)
For each coating line which applies coatings
sub~’iectto more than one numerical emission
limitation from more than one of the four coating
categories
in Section 219.204(j)
eve,
during the
same day,
the owner or operator shall have a
site-specific proposal approved by the Agency and
approved by the USEPA
as
a SIP revision.
To
receive approval,
the requirements
of USEPA’s
Emissions Trading Policy Statement
(and related
policy)
51
Fed.
Peg. 43814
(December
4,
1986),
must be satisfied.
c)
No owner or operator of
a can coating faciiityline
subject to the limitations of Section 24-~212.204(b)~
this Part shall operate the subject coating
facilityline using
a coating with
a VON content
in
excess of the limitations specified
in Section
~4-8j~.204(b)
of this Part unless all of the following
requirements are met:
1)
An alternative daily emission limitation for the
can coating operation,
i.e.
for all the can
coating lines at the source,
shall
be determined

448
according to subsection
(a) (2)
below.
Actual
daily emissions shall never exceed the alternative
daily emission limitation and shall be calculated
by use of the following equation.
n
Ed
=
~
V~C1
-
i=1
where:
Ed
=
Actual VON emissions for the day in
units of kg/day
(1bs/day)~j
I
=
Subscript denoting
a specific
coating appliedT~
n
=
Total number of coatings applied in
the can coating operation i.e.
all
can coating lines at the source
V
=
Volume of each coating applied for
the day in units of 1/day
(gal/day)
of coating
(minus water and any
compounds which are specifically
exempted from the definition of
VON) ~
C
=
The VON content of each coating as
applied
in units of
kg VOM/l
(lbs
VON/gal)
of coating
(minus water
and any compounds which are
specifically exempted from the
definition of VON).
2)
The alternative daily emission limitation
(Ad)
shall be determined for the can coating operatiqp~
i.e.
for all the can coating lines at the source,
on a daily basis as
follows:
n
Ad
=
E
VIL~L~
-Cl
i=1
(D1
L)
where:
The VON emissions allowed for the
day in units of kg/day (lbs/day)~~
i
=
Subscript denoting
a specific
coating applied~~

449
n
=
Total number of surface coatings
applied
in the can coating
operatI
C,
=
The
VON
content of each surface
coating as applied in units of kg
VON/l
(lbs VON/gal)
of coating
(minus water and any compounds
which are specifically exempted
from the definition of VOM)-T~
D
=
The density of VON in each coating
applied.
For the purposes of
calculating
~,
the density
is
0.882 kg VOM/l VON (7.36 lbs
VON/gal VOM)-~-~
V
=
Volume of each surface coating
applied
for the day
in units of
1
(gal)
of coating
(minus water and
any compounds which are
specifically exempted from the
definition of VON)-7-~
L1
=
The VON emission limitation for
each surface coating applied as
specified
in Section 219.204(b)
~
this Part
in units
of
kg VON/i
(lbs
VON/gal)
of coating
(minus water
and any compounds which are
specifically exempted from the
definition of VOM).
d)
No owner or operator of
a heavy off-highway vehicle
products coating line subject to the limitations of
Section 219.204(k)
of this Part shall apply coatings to
heavy off-highway vehicle products on the subject
coating
line unless the requirements of subsection
(d) (1)
or
(d) (2) below are met.
-
1)
For each coating line which applies multiple
coatings,
all
of which are subject to the same
numerical emission limitation within Section
219.204(k)
above, during the same day
(e.g.,
all
coatings used on the line are subject to 0.42
kg/i
3.5
lbs/gal)),
the daily-weighted average VON
content shall not exceed the coating VON content
limit corresponding to the category of coating
used,
or

450
2)
For each coating line which applies coatings
-
subject to more than one numerical emission
limitation
in Section 219.204(k)
above, during the
same day,
the owner or operator shall have a site
specific proposal approved
by
the Agency and
approved
by
the USEPA as a SIP revision.
To
receive approval,
the requirements
of USEPA’s
Emissions Trading Policy Statement
(and related
policy)
51 Fed.
Req.
43814
(December
4,
1986)
must
be satisfied.
e)
No owner or operator of a wood furniture coating line
subject to the limitations of Section 219.204(1)
~
this Part shall apply coatings to wood furniture on the
subject coating line unless the requirements of
subsection
(e) (1)
or subsection
(e) (2)
below,
in
addition to the requirements specified
in the note to
Section 219.204(1)
of this Part,
are met.
1)
For each coating
line which applies multiple
coatings,
all
of which are subject to the same
numerical emission limitation within Section
219.204(1)
above,
during the same day
(e.g.,
all
coatings used on
the
line are subject to 0.67 kg/l
5.6
lbs/gal)),
the daily-weighted average VON
content shall not exceed the coating VON content
limit corresponding to the category of coating
used,
or
2)
For each coating
line which applies coatings
subject to more than one numerical emission
limitation
in Section 219.204(1)
above, during the
same day, the owner or operator shall have a site
specific proposal approved by the Agency and
approved by the USEPA as a SIP revision.
To
receive approval,
the requirements of USEPA’s
Emissions Trading Policy Statement
(and related
policy)
51 Fed.
Req.
43814
(December
4,
1986),
must be satisfied.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.206
Solids Basis Calculation
Limitations
in terms of kg
(lbs)
of VON emissions per
1
(gal)
of
solids
as applied at each coating applicator shall
be determined
by the following equation:
S=
C
1
-
(C/D)

451
-where:
S
=
The limitation on VON emissions
in terms of
kg VON/l
(lbs VON/gal)
of so1idsT~
C
=
The limitation on VON emissions
in terms of
kg/l
(lbs/gal)
of coating
(minus water and
any compounds which are specifically excluded
from the definition of VON)
specified
in
Section
219~204T~
D
=
The density of VON in the coating.
For the
purposes of calculating
5, the density is
0.882 kg VON/l VON
(7.36
lbs VON/gal VON).
(Source:
Amended at
_____
,
Ill.
Peg.
______
,
effective
Section 219.207
Alternative Emission Limitations
a)
Any owner or operator of
a coating line subject to
Section 219.204 of this Part may comply with this
Section, rather than with Section 219.204
of this Part,
if
a capture system and control device are operated at
all times the coating line is
in operation and the
owner or operator demonstrates compliance with
subsections
(c),
(d),
(e),
(f),
(g)
or
(h)
of this
Section
(depending upon the source category) through
the applicable coating analysis and capture system and
control device efficiency test methods and procedures
specified
in Section 219.105 of this Part and the
recordkeeping and reporting requirements specified in
Section 219.211(e)
-of this Part
and the control device
is equipped with the applicable monitoring equipment
specified
in Section 219.105(d)
of this Part and the
monitoring equipment
is installed,
calibrated,
operated
and maintained according to vendor specifications
at
all times the control device
is
in use.
A capture
system and control device, which does not demonstrate
compliance with subsection
(c)
,
(d)
,
(e),
(f),
(g)
or
(h)
of this Section may be used as an alternative to
compliance with Section 219.204
of this Part only
if
the alternative
is approved by the Agency and approved
by the USEPA as a SIP revision.
b)
Alternative Add-On Control Methodologies
1)
The coating line
is equipped with a capture system
and control device that provides 81 percent
reduction
in the overall emissions of VON from the
coating line and the control device has a
90
percent efficiency,
or

452
2)
The
system used to control VON from the coating
line
is demonstrated to have an overall efficiency
sufficient to limit VON emissions to no more than
what
is allowed under Section 219.204
of this
Part.
Use of any control system other than an
afterburner,
carbon adsorption,
condensation,
or
absorption scrubber system can be allowed only
if
approved by the Agency and approved by the USEPA
as a SIP revision.
The use of transfer efficiency
credits can be allowed only if approved by the
Agency and approved by the USEPA as
a SIP
revision.
Baseline transfer efficiencies and
transfer efficiency test methods must be approved
by the Agency and the USEPA.
Such overall efficiency
is to be determined as
follows:
A)
eObtain the emission limitation from the
appropriate subsection
in Section 219.204
of
this Part,
B)
e~alculate “S” according to the equation
in
Section 219.206 of this Part,
C)
ecalculate the overall efficiency required
according to Section
219.105(e)
of this Part.
For the purposes of calculating this value,
according to the equation
in Section
219.105(e) (2)
of this Part, VON~ is equal
to
the value of
“S”
as determined above
in
subsection
(b) (2) (B)
of this Section.
a)
No owner or operator of
a coating line subject to only
one of the emission limitations from among Section
219.204(a) (1),
(a) (2),
(a) (4),
(C),
(d),
(e),
(f),
(g),
(h)
or
(i)
of this Part and equipped with
a capture
system and control device shall operate the subject
coating line unless the requirements
in subsection
(b) (1)
or
(b) (2)
above are met.
No owner or operator
of
a coating
line subject to Section 219.204
(a) (2)
or
(a) (3)
of this Part and equipped with
a capture system
and control device shall operate the coating line
unless the owner or operator demonstrates compliance
with the topcoat such limitation
in accordance with the
topcoat protocol for automobile
or
light—duty truehs
referenced
in Section 219.105(b)
of this Part.
d)
No owner or operator of
a miscellaneous metal parts and
products coating line which applies one
or more
coatings during the same day,
all of which are subject

453
to the same numerical emission limitation within
Section 219.204(j)
of this Part
(e.g.,
all coatings
used on the line are subject to
0.42
kg/i
3.5
lbs/gal)), and which
is equipped with
a capture system
and control device shall operate the subject coating
line unless the requirements
in subsection
(b) (1)
or
(b) (2)
above are met.
e)
No owner or operator
cf
a heavy off-highway vehicle
products coating line which applies one or more
coatings during the same day,
all
of which are subject
to the same numerical emission limitation within
Section 219.204(k)
(e.g.,
all coatings used on the line
are subject to 0.42 kg/i
3.5
lbs/gal),
and which
is
equipped with a capture system and control device shall
operate the subject coating
line unless the
requirements
in subsection
(b) (1)
or
(b) (2)
above are
met.
f)
No owner or operator of a wood furniture coating line
which applies one or more coatings during the same day,
all of which are subject
to the same numerical emission
limitation within Section
219.204(1)
of this Part
(e.g.,
all
coatings used on the line are subject to
0.67 kg/l
5.6
lbs/gal)),
and which
is equipped with
a
capture system and control device shall operate the
subject coating line unless the requirements
in
subsection
(b) (1)
or
(b)
(2)
of this Section are met.
If compliance is achieved by meeting the requirements
in subsection
(b) (2)
of this Section, then the
provisions
in the note to Section 219.204(1)
of this
Part must also be met.
g)
No owner
or operator of a can coating facilityline and
equipped with
a capture system and control device shall
operate the subject coating facilityline unless the
requirements
in subsection
(h) (1)
or
(h) (2)
below are
met.
1)
An alternative daily emission limitation for the
can coating operation,
i.e.
for all the can
coating lines at the source,
shall be determined
according to Section
219.205(c) (2)
of this Part.
Actual daily emissions shall never exceed the
alternative daily emission limitation and shall be
calculated by use of the following equation:
n
Ed
=
E
VC1
(1—F1)
i=l

454
where:
Ed
=
Actual VON emissions for the day in
units
of kg/day (lbs/day)~~
i
=
Subscript denoting the specific
coating applied~.~
n
=
Total number of surface coatings as
applied in the can coating
operationy~
V,
=
Volume of each coating as applied
for the day in units of 1/day
(gal/day)
of coating
(minus water
and any compounds which are
specifically exempted from the
definition
of VON)-7-~
C~
=
The VON content
of each coating
as
applied in units of kg VON/l
(lbs
VON/gal)
of coating
(minus water
and any compounds which are
specifically
exempted
from the
definition of VON)~
-
F1
=
Fraction,
by weight,
of VON
emissions from the surface coating,
reduced or prevented from being
emitted to the ambient air.
This
is
the overall efficiency of the
capture system and control device.
2)
The coating line
is equipped with a capture system
and control device that provide 75 percent
reduction
in the overall emissions
of VON from the
coating line and the control device has
a 90
percent efficiency.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
____________
Section 219.208
Exemptions From Emission Limitations
a)
Exemptions for all s-ourcccoating categories except wOod
furniture coating.
The limitations of this Subpart
shall not apply to coating lines within a
facilitysource,
that otherwise would be subject
to the
same subsection
of Section 219.204
(because they belong
to the same sourcccoating category,
e.g.
can coating)
provided that combined actual emissions
of VON from all

455
lines at the facilitysource subject to that subsection
never exceed 6.8 kg/day
(15 lbs/day) before the
application of capture systems and control devices.
(For
example,
can coating lines within a plantsource
would not be subject to the limitations of Section
219.204(b)
of this Part
if the combined actual
emissions of VON from the can coating lines never
exceed 6.8 kg/day
(15 lbs/day)
before the application
of capture systems and control devices.)
Volatile
organic material emissions from heavy off—highway
vehicle products
coating lines must be combined with
VOM emissions from miscellaneous metal parts and
products coating
lines to determine applicability.
Any
owner or operator of a coating facilitysource shall
comply with the applicable coating analysis test
methods and procedures specified
in Section 219.105(a)
of this Part and the recordkeeping and reporting
requirements specified
in Section 219.211(a)
of this
Part
if total VON emissions from the subject coating
lines are always less than or equal to 6.8 kg/day
(15 lbs/day)
before the application of
capture systems
and control devices
and, therefore,
are not subject to
the limitations
of Section 219.204
of this Part.
Once
a category of coating
lines at
a facilitysource
is
subject to the limitations
in Section 219.204
of this
Part,
the coating lines are always subject to the
limitations
in Section 219.204
of this Part.
b)
Applicability for wood furniture coating
1)
The
limitations of this Subpart shall apply to
a
plant’ssource’s wood furniture coating lines
if
the plantsource contains process emission
sourccsunits, not regulated by Subparts
B,
E,
F
(excluding Section 219.204(1)
of this Part),
H
(excluding Section 219.405 Qf this Part),
Q,
R,
S,
T
(excluding
Section
219.486
of
this
Part)
,
V,
X,
Y, e~
Z
or
BE
of
this
Part,
which
as
a group both:
A)
~ave
maximum theoretical emissions
of
91 Mg
(100 tons)
or more per calendar year of VON
if no air pollution control
equipment were
used,
and
B)
BAre not limited to less than 91 Mg
(100 tons)
of VON per calendar year
if no air
pollution control equipment were used,
through production or capacity limitations
contained in
a federally enforceable
construction permit or SIP revision.

456
2)
If
a plantsource ceases to fulfill the criteria of
subsection
(b) (1)
of this Section, the limitations
of Section 219.204(1)
of this Part shall continue
to apply to any wood furniture coating line which
was ever subject to the limitations
of Section
219.204(1)
of this Part.
3)
For the purposes of subsection
(b)
of this
Section,
an emission sourceunit shall be
considered regul~ed by
a Subpart
if
it
is subject
to the limitations of that Subpart.
An emission
sourccunit
is not considered regulated by a
Subpart
if
it is not sublect to the limits of that
Subpart,
e.g.,
the emission unit
is covered by an
exemption
in the Subpart or the applicability
criteria
of the Subpart are not met. its emissions
-ar-c below the applicability cutoff level
or if the
source
is
covered by an exemption.
4)
Any owner or operator of
a wood furniture coating
line to which the limitations of this Subpart are
not applicable due to the criteria
in subsection
(b)
of this Section shall, upon request by the
Agency or the USEPA,
submit records to the Agency
and the USEPA within 30 calendar days from the
date of the request that document that the coating
line
is exempt from the limitations of this
Subpart.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
____________
Section 219.209
Exemption From General Rule on Use of Organic
Material
No owner or operator of a coating line subject to the limitations
of
Section
219.204
of
this
Part
is
required
to
meet
the
limitations of Subpart G
(Section 219.301
or 219.302)
of this
Part,
after the date by which the coating line
is required to
meet
Section
219.204
of
this
Part.
-
(Source:
Amended at
Ill. Peg.
______
,
effective
_____________
Section 219.210
Compliance Schedule
Every owner or operator of a coating line
(of a type included
within Section 219.204
of this Part)
shall comply with the
requirements
of
Section
219.204,
219.205,
219.207
or
219.208
and
Section 219.211 of this Part
in accordance with the appropriate
compliance schedule
as specified
in subsection
(a)
,
(b)
,
(c)
or
(0)
below:

457
a)
No owner or operator of
a coating line which
is exempt
from the limitations
of Section 219.204
of this Part
because of the criteria in Section 219.208(a)
of this
Part shall operate said coating line on or after a date
consistent with Section 219.106
of this Part, unless
the owner or operator has complied with,
and continues
to comply with,
Section 219.211(b)
of this Part.
Wood
furniture coating
lines are not subject to Section
219.211(b)
of this Part.
b)
No owner or operator of
a coating line complying by
means
of Section 219.204
of this Part shall
operate
said coating
line on or after
a date consistent with
Section 219.106
of this Part, unless the owner or
operator has complied with,
and continues to comply
with,
Sections 219.204 and 219.211(c)
of this Part.
c)
No owner or operator of a coating line complying by
means of Section 219.205 of this Part shall operate
said coating
line on or after
a date consistent with
Section 219.106
of this Part, unless the owner or
operator has complied with, and continues to comply
with,
Sections 219.205 and 219.211(d)
of this Part.
0)
No owner
or operator of
a coating line complying by
means of Section 219.207
of this Part shall operate
said coating
line on or after
a date consistent with
Section 219.106
of this Part,
unless the owner or
operator has complied with,
and continues to comply
with,
Sections 219.207 and 219.211(e)
of this Part.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
____________
Section 219.211
P.ecordkeeping and Reporting
a)
The
VON
content
of each coating and the efficiency of
each capture system and control device shall be
determined by the applicable test methods and
procedures specified in Section 219.105
of this Part to
establish the records required under this Section.
b)
Any owner or operator of
a coating line which
is
exempted from the limitations of
Section 219.204 ~
this Part because of Section 219.208(a)
of this Part
shall comply with the following:
1)
By
a
date consistent with Section 219.106 of
this
Part, the owner or operator of
a facilitycoatipg
line or group of coating lines referenced
in
t-hi-s
subsection
~J
of this Section shall certify to
the Agency that the facilitycoating
line
or gro~p

458
of coating lines
is exempt under the provisions
of
Section 219.208(a)
of this Part.
Such
certification shall include:
A)
A declaration that the facilitycoating
line
is exempt from the limitations of Section
219.204
of this Part because of Section
219.208(a)
of this Part
and
B)
Calculations which demonstrate that the
combined VON emissions from e-~the_coating
line
and- all other coating lines
in the same
category at the facility never exceed
6.8 kg
(15 lbs)
per day before the application of
capture systems and control devices.
The
following equation shall be used to calculate
total VON emissions:
m
n
T~
=
E
(A
B)~
j=l
i=1
-
where:
-
T~~=Total VON emissions from coating lines
at
a facility each day before the
application of capture systems and
control devices
in units of kg/day
(lbs/day)j
m
=
Number of coating lines at the
facilitysource that otherwise would
be subject to the same subsection
of Section 219.104
of this Part
(because they belong to the same
category,
e.g., can coating)
j
=
Subscript denoting an individual
coating
line.L
n
=
Number of different coatings as
applied each day on each coating
line at the facilityj
i
=
Subscript denoting an individual
coating~
A
=
Weight of VON per volume of each
coating
(minus water and any
compounds which are specifically
exempted from the definition
of

459
VON)
as applied each day on each
coating
line at the facility
in
units
of kg VON/i
(lbs VOM/gal).L
B,
=
Volume
of each coating
(minus water
and any compounds which are
specifically exempted from the
definition of VOM)
as applied each
d~-on each coating line at the
facility
in units
of 1/day
(gal/day).
The instrument or
method by which the owner
or
operator accurately measured or
calculated the volume of each
coating as applied on each coating
line each day shall be described in
the certification to the Agency.
2)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator of
a
facilitycoating
line or group of
lines referenced
in this subsection shall collect and record all
of
the following information each day for each
coating line and maintain the information at the
facilitysource for a period of three years:
A)
The name and identification number of each
coating as applied
on each coating line.
B)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating line.
3)
On and after a date consistent with Section
219.106 of this Part,
the owner or operator of
a
facilitycoating line or group of
coating lines
exempted from the limitations of
Section 219.204
of this Part because of Section 219.208(a)
of this
Part shall notify the Agency of any record showing
that total VON emissions from the coating
facilityline
or group of coating lines exceed
6.8 kg
(15
lbs)
in any day before the application
of capture systems and control devices
by sending
a copy of such record to the Agency within
30 days
after the exceedance occurs.
c)
Any owner or operator
of
a coating line subject to the
limitations
of Section 219.204
of this Part other than
Section
219.204(a)
(2)
and
(a) (3)
and complying
by
means

460
of Section 219.204 of this Part shall comply with the
following:
1)
By
a date consistent with Section 219.106
of this
Part,
or upon initial start—up of
a new coating
line,
or upon changing the method of compliance
from an existing subject coating line from Section
219.205
or Section 219.207
to Section 219.204 ~
this Part
the owner or operator of
a subject
coating line shall certify to the Agency that the
coating
line wil
be in compliance with Section
219.204
of this Part on and after a date
consistent with Section 219.106 of this Part,
or
on and after the initial start-up date.
Such
certification shall include:
A)
The name and identification number of each
coating as applied on each coating line.
B)
The weight of VON per volume of each coating
(minus water and any compounds which are
specifically exempted from the definition of
VON)
as applied each day on each coating
line.
?-)-
For coating lines subject to Section
219.204(a) (3)
certification shall include:
4-)-
inc
name
aria
iacnLiiicu~iOfl
numDcr
ci
coan coatinn
uric
wnucn wuu
“-‘~‘‘-‘
~
~
219.204 (a) (3),
44-)-
The name and identification numuer
oi
cacn coaL1nc~
~r~r~~1co
on cacn coati~~~~
line,
iii)
The weight of VON per volume of
each
coating as applied
on each coating line,
4-v-)-
The
instrument
or method
by
which
t-~e
owner or operator will accurately
measure or calculate the volume
of
each
coating as applied each day on each
coating line,
The
method
by
which
the
owner
or
operator
will
create
and
maintain
records each day as required
in
subsection
(a) (2)
below for coating
lines subject to Section 219.204(a)
(-n-,-

461
~4-)-An example format
in which the rccor~
required
in subsection
ow
i
coating
lines subject to Section
210.204(a) (3).
-
2)
On and after
a date consistent with Section
219.106 of this Part,
or on and after the initial
start-up date,
the owner or operator of a subiect
coating line oubjcct to the
limitations—e-f
&ect-i-en
219.204 and complying by means of Section
219.2-04
shall collect and record all of the following
information each day for each coating line and
maintain the information at the facility
source
for a period of three years:
A)
The name and identification number of each
coating as applied
on each coating line.
B)
The weight
of VON per volume
of each coating
(minus water and any compounds which are
specifically exempted from the definition of
VON)
as applied each day on each coating
line.
~or
coating
lines
subject
to
Section
218.204(a)
(3)
the owner or operator
shall
maintain all records necessary to calculate
the daily-weighted average VON content from
the coating
line
in accordance with the
proposal
submitted, and approved by the
USEPA, pursuant to Section 218.204(a) (3).
3)
On and after
a date consistent with Section
219.106 of this Part,
the owner or operator of
a
subject coating line shall notify the Agency in
the following instances:
month
in which the violation occurred.
B)
At least
30 calendar days before changing the
method of compliance with Section 210.2-04
from Section 219.204
to Section 219.205
or
Section 219.207
of this Part,
the owner or
operator shall comply with all requirements
A)
Any record showing violation of Section
219.204
of this Part shall be reported by
sending
a copy of such record to the Agency
within
30 days following the occurrence of
the violation,
except
that any record showi-~
a
violation
of
Section
210.204
(a)
(3)
shall
be
r~n~r~r~ by
~n~ing
a copy of
such record to
15 days from the end of
~

462
of subsection
(d) (1)
or
(e) (1)
below,
respectively.
Upon changing the method of
compliance with Section 210.204. from Section
219.204
to Section 219.205 or Section 219.207
of this Part,
the owner or operator shall
comply with all requirements of subsection
(d)
or
(e)
of this Section, respectively.
rur
euuLuny
uuncs
~UDjC~L
LO
~coLiOfl
219.204 (a) (i.
,
~nc owner or ~~ator
shall
notuy
tnc Agency
ci
any onange to the
topooating operation at least
30 days before
the change is effected.
The Agency chall
determine whether
or not determines that
r~eertification
testing
isrcqu~r~d
th-er
owner
or opcra~or~nuuu
~u~mut
propoaau
tu
the Agency to test within
30 days and retest
within
30 days of the Agency’s opproval
of
~-
‘-‘
.‘
ca
.k.
d)
Any owner or operator of
a coating
line subject to the
limitations of Section 219.204 of this Part and
complying by means of Section 219.205 of this Part
shall comply with the following:
1)
By a date consistent with Section 219.106 of this
Part,
or upon initial start—up of a new coating
line,
or upon changing the method of compliance
for an existing subject coating line from Section
219.204
or Section 219.207
to Section 219.205
of
-
this Part
the owner or operator of the subject
coating line shall certify to the Agency that the
coating line will be
in compliance with Section
219.205 on and after a date consistent with
Section 219.106
of this Part,
or on and after the
initial start—up date.
Such certification shall
include:
A)
The name and identification number
of each
coating line which will comply by means of
Section 219.205 of this Part.
B)
The name and identification number of each
coating
as applied on each coating
line.
C)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating
line.

463
D)
The instrument
or method by which the owner
or operator will accurately measure or
-
calculate the volume of each coating
as
applied each day on each coating
line.
E)
The method by which the owner or operator
will create and maintain records each day as
required in subsection
(d) (2)
of this
Section.
F)
An example of the format
in which the records
required in subsection
(d) (2)
of this Section
will be kept.
2)
On and after
a date consistent with Section
219.106
of this Part,
or on and after the initial
start-up date,
the owner or operator of
a subiect
coating line subject to the limitations
of gecti-e~
219.204 and complying by means of Section 210.205,
shall collect and record all of the following
information each day for each coating line and
maintain the information at the facilitysource for
a period of three years:
A)
The
name
and
identification
number
of
each
coating as applied on each coating line.
B)
The weight of VON per volume and the volume
of
each
coating
(minus
water
and
any
compounds which are specifically exempted
from the definition
of VON)
as applied each
day on each coating
line.
C)
The daily-weighted average VON content of all
coatings as applied on each coating line
as
defined
in Section 219.104
of this Part.
3)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator
of a
subject coating line shall notify the Agency
in
the following instances:
A)
Any record showing violation of Section
219.205
of this Part shall be reported by
sending
a
copy
of
such
record
to
the
Agency
within
30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with this subpart from
Section 219.205 to Section 219.204
or Section
219.207
of this Part,
the owner or operator

464
shall comply with all requirements
of
subsection
(a) (1)
or
(e) (1)
of this Secti~j1,
respectively.
Upon changing the method of
compliance with this subpart from Section
219.205 to Section 219.204
or Section 219.207
of this Part,
the owner or operator shall
comply with all requirements
of subsection
(a)
or
(e)
of this Section, respectively.
e)
Any owner or operator of a coating line subject to the
limitations of Section 219.207 and complying by means
of Section 219.207(c),
(d),
(e),
(f),
(g)
or
(h) ~
this Part shall comply with the following:
1)
By
a date consistent with Section 219.106 of this
Part,
or upon initial start—up of
a new coating
line,
or upon changing the method of compliance
for an existing coating line from Section 219.204
or Section 219.205 to Section 219.207
of this
Part, the owner or operator of the subject coating
line shall perform all tests and submit to the
Agency the results of all tests and calculations
necessary to demonstrate that the subject coating
line will be in compliance with Section 219.207 ~
this Part on and after
a date consistent with
Section
219.106
of this Part,
or on and after the
initial start-up date.
2)
On and after
a date consistent with Section
219.106 of this Part,
or on and after the initial
start-up date,
the owner or operator of
a coating
line subject to the limitations of
Section 219.207
subject and complying by means
of Section
210.207(c),
(d)
,
(a),
(f)
,
(g)
,
or
(h) shall
collect and record all of the following
information each day for each coating line and
maintain the information at the focilitysource for
a period
of three years:
A)
The weight of VON per volume
of coating
solids as applied each day on each coating
line,
if complying pursuant to Section
219.207(b) (2)
of this Part.
-
B)
Control device monitoring data.
C)
A log of operating time for the capture
system,
control device, monitoring equipment
and the associated coating
line.
D)
A maintenance log for the capture system,
control device and monitoring equipment

465
detailing all routine and non—routine
maintenance performed including dates and
duration of any outages.
3)
On and after a date consistent with Section
219.106
of this Part,
the owner or operator of
a
subject coating line shall notify the Agency
in
the following instances:
A)
Any record showing violation of Section
219.207
of this Part shall be reported by
sending
a copy of such record to the Agency
within
30 days following the occurrence of
the violation.
B)
At least 30 calendar days before changing the
method of compliance with this Subpart from
Section 219.207 to Section 219.204 or Section
219.205
of this Part,
the owner or operator
shall comply with all requirements of
subsection
(c) (1)
or
(d) (1)
of this Section,
respectively.
Upon changing the method of
compliance with this subpart from Section
219.207
to Section 219.204
or Section 219.205
of this Part, the owner or operator shall
comply with all requirements
of subsection
(c)
or
(d)
of this Section, respectively.
~
Any owner
or operator of
a primer surfacer operation or
topcoat operation subject to the limitations
of Section
219.204 (a) (2)
or
(a) (3)of this Part shall comply with
the following:
-
jj
By
a date consistent with Section 219.106
of this
Part,
or upon initial start—up of
a new coating
operation,
the owner or operator of
a subject
coating operation shall certify to the Agency that
the operation will be
in compliance with Section
219.204
of this Part
on and after
a date
consistent with Section 219.106 of this Part,
or
on and after the initial start-up date.
Such
certification shall include:
~j.
The name and identification number of each
coating omeration which will comply by means
of
Section 219.204 (a) (2) and
(a) (3)
of this
Part and the name and identification number
of each coating line
in each coating
operation.

466
~
The name and identification number of each
coating as applied on each coating line~in
the coating operation.
çj
The weight of VON per volume of each
coatin.g
(minus water and any compounds which are
specifically exempted from the definition
of
VON)
as applied each day on each coating
line.
QJ.
The transfe~ efficiency and control
efficiency measured for each coating line.
.~j.
Test reports,
including raw data and
calculations documenting the testing
performed to measure transfer efficiency and
control efficiency.
fi
The instrument or method by which the owner
or operator will accurately measure or
calculate the volume of each coating as
applied each day on each coating
line.
~
The method by which the owner or operator
will create and maintain records each day as
required in subsection
(f) (2)
below.
~j
An example format for presenting the records
required
in subsection
(f) (2)
below.
2.1
On and after
a date consistent with Section
219.106
of this Part,
or on and after the initial
start-up date,
the owner or operator of
a subject
coating operation shall collect and record all
of
the following information each day for each
topcoat or primer surfacer coating operation and
maintain the information at the source for
a
period of three years:
~Z~j
All information necessary to calculate the
daily-weighted average VON emissions from the
coating operations
in kg
(lbs)
per
I
(gal)
of
coating solids deposited
in accordance with
the proposal submitted,
and approved pursuant
to Section 219.204(a) (2)
or
(a) (3)
of this
Part
including:
~
The name and identification number of
each coating as applied on each coat4~p2
operation.

467
J~j)
The weight of VON per volume of each
coating
(minus water and any compoun~
which are specifically exempted from the
definition of
VOM)
as applied each d~y
on each coating operation.
~J.
If
a control device(s)
is used to control VON
emissions,
control device monitoring data;
a
log
of operating time for the capture system,
control device,
monitoring equipment and the
associated coating operation; and a
maintenance log for the capture system,
control device and monitoring
equipment,
detailing all routine and non-routine
maintenance performed including dates and
duration
of any outages.
~
On and after a date consistent with Section
219.106 of this Part or on and after the initial
start-up date,
the owner or operator of
a subject
coating operation shall determine and record the
daily VON emissions
in kg(lbs) per
1
(gal)
of
coating solids deposited
in accordance with the
proposal submitted and approved pursuant to
Section 219.204 (a) (2)
or
(a) (3)
of this Part
within 10 days from the end of the month and
maintain this information at the source for a
period of three years.
j)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator of
a
subject coating operation shall notify the Agency
in the following instances:
1~j
Any record showing
a violation of Section
219.204(a) (2)
or
(a)(3)
of this Part shall
be
reported by sending
a copy of
such record to
the Agency within
15 days from the end of the
month
in which the violation occurred.
~j
The owner or operator shall notify the Agency
of any change to the operation at least 30
days before the change
is effected.
The
Agency shall determine whether or not
-
compliance testing
is required.
If the
Agency determines that compliance testing
is
required,
then the owner or operator shall
submit
a testing proposal to the Agency
within 30
days
and test within
30
days
of
the
approval
of the proposal by the Agency and
USEPA

468
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
SUBPART G:
USE OF ORGANIC MATERIAL
Section 219.301
Use of Organic Material
No person shall cause or allow the discharge of more than 3.6
kg/hr
(8
lbs/hr)
of organic material
into the atmosphere from any
emission s-ourceunit, except as provided in Sections 219.302,
219.303,
219.304 of this Part and the following exception:
If
no
odor nuisance exists the limitation of this Subpart shall apply
only to photochernically reactive material.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.302
Alternative Standard
Emissions
of organic material
in excess of those permitted by
Section 219.301
of this Part are allowable
if such emissions are
controlled by one of the following methods:
a)
Flame,
thermal or catalytic incineration
so as either
to reduce such emissions to 10 ppm equivalent
methane
(molecular weight
16)
or
less,
or to convert 85 percent
of the hydrocarbons to carbon dioxide and water; or,
b)
A vapor recovery system which adsorbs and/or condenses
at least 85 percent
of the total uncontrolled organic
material that would otherwise
b-e emitted to the
atmosphere;
or,
c)
Any other air pollution control equipment approved by
the Agency and approved by the USEPA as
a SIP revision
capable of reducing by 85 percent or more the
uncontrolled organic material that would
be otherwise
emitted to the atmosphere.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.303
Fuel Combustion Emission EourccsUnits
The provisions
of Sections 219.301 and 219.302
of this Part shall
not apply to fuel
combustion emission s-ourcesunits.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.304
Operations with Compliance Program

469
The provisions
of Sections 219.301 and 219.302
of this Part shall
not apply to any owner, operator,
user or manufacturer
of paint,
varnish,
lacquer, coatings or printing ink whose compliance
program and project completion schedule,
as required by 35
Ill.
Adm.
Code 201, provided for the reduction of organic material
used in such process to 20 percent or less of total volume by May
30,
1977.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
SUBPART
H:
PRINTING
AND
PUBLISHING
Section 219.401
Flexographic and Rotogravure Printing
a)
No owner or operator of
a subject flexographic,
packaging rotogravure or publication rotogravure
-
printing line shall apply at any time any coating or
ink unless the VON content does not exceed the
limitation specified in either subsection
(a) (1)
or
(a) (2) below.
Compliance with this Section must be
demonstrated through the applicable coating or ink
analysis test methods and procedures specified
in
Section 219.105(a)
and the recordkeeping and reporting
requirements specified in Section 219.404(c)
of this
Part.
As an alternative to compliance with this
subsection,
a subject printing line may meet the
requirements
of subsection
(b)
or
(c) below.
1)
Forty percent VOM by volume of the coating and ink
-
(minus water and any compounds which are
specifically exempted from the definition of VON),
or
2)
Twenty-five percent VOM by volume of the volatile
content in the coating and ink.
b)
No owner or operator of a subject flexographic,
packaging
rotogravure
or
publication
rotogravure
printing line shall apply coatings or inks on the
subject
printing
line
unless
the
weighted
average,
by
volume,
VON
content
of
all
coatings
and
inks
as
applied
each day on the subject
printing
line
does
not
exceed
the limitation specified
in either subsection
(a) (1)
(as determined by subsection
(b) (1)j or subsection
(a)(~2)) (as determined by subsection
(b)(2)
of this
Section).
Compliance with this subsection must be
demonstrated through the applicable coating or ink
analysis test methods and procedures
specified in
Section 219.105(a)
of this Part and the recordkeeping

470
and reporting requirements specified in Section
219.404(d)
of this Part.
1)
The following equation shall be used to determine
if the weighted average VON content of all
coatings and inks as applied each day on the
subject printing line exceeds the limitation
specified in subsection
(a) (1)
of this Section.
n
E
Cj L~ (V~1
+
VVOM1)
i=4~1
VON(I)(A
=
n
L1 (V~
±
VVOM)
i
=~
1
Where:
=
The weighted average VON content
in
units of percent VON by volume of
all coatings and inks
(minus water
and any compounds which are
specifically exempted from the
definition of VON)
used each day~~
i
=
Subscript denoting a specific
coating or ink as applied-~-j.
n
=
The number of different coatings
and/or inks
as applied each day on
a printing lineT~
C
=
The VON content
in units
of percent
VON by volume of each coating or
ink as applied
(minus water and any
compounds which are specifically
exempted from the definition of
VON)T.L
L
=
The liquid volume of each coating
or ink as applied
in units of
1
(gal)T.z.
=
The volume fraction of solids
in each
coating
or ink as applied,
~nd.L
=
The volume fraction of VON in each
coating
or ink as applied.

471
2)
The following equation shall be used to determine
if the weighted average VON content of all
coatings and inks as applied each day on the
subject printing line exceeds the limitation
specified
in subsection
(a) (2)
of this Section.
n
C L~V~~1
VOM(~)~)
=
1=1
n
L,
VVM
i=l
where:
VOM(~)~
=
The weighted average VON content
in
units of percent VON by volume of
the volatile content of all
coatings and inks used each day~.~
i
=
Subscript denoting
a specific coating or
ink as applie8,.j
n
=
The number of different coatings and/or
inks as applied each day on each
printing lineT~
=
The VON content
in units of percent VON
by volume of the volatile matter
in each
coating or ink as
appliedT.L
L
=
The liquid volume of each coating or ink
as applied in units of
1
(gal)
,
and~
=
The volume fraction of volatile matter
in each coating
or ink as applied.
c)
No owner or operator
of
a subject flexographic,
packaging rotogravure or publication rotogravure
printing line equipped with a capture system and
control device shall operate the subject printing line
unless the owner or operator meets the requirements
in
subsection
(c) (1),
(c) (2)
or
(c) (3)
and subsections
(c)
(4)
/
(c)
(5)
and
(c) (6)
below.
1)
A carbon adsorption system is used which reduces
the captured VON emissions by at least
90 percent
by weight,
or

472
2)
An incineration system is used which reduces the
captured VON emissions by at least 90 percent by
weight,
or
3)
An alternative VON emission reduction system
is
used which is demonstrated to have at least a
90 percent control device efficiency,
approved by
the Agency and approved by USEPA
as a SIP
revision,
and
4)
The printing line
is equipped with
a capture
system and control device that provides an overall
reduction
in
VON
emissions
of
at
least:
A)
75 percent where a publication rotogravure
printing line
is employed,
or
B)
65 percent where
a packaging rotogravure
printing line is employed,
or
C)
60 percent where a flexographic printing line
is employed,
and
5)
The control device
is equipped with the applicable
monitoring equipment specified in Section
219.105(d) (2)
of this Part and,
except as provided
in
Section
219.105(d)
(3)
of
this
Part,
the
monitoring equipment
is installed,
calibrated,
operated and maintained according to vendor
specifications
at all times the control device
is
in use,
and
6)
The capture system and control device are operated
at all times when the subject printing line
is
in
operation.
The owner or operator shall
demonstrate compliance with this subsection by
using the applicable capture system and control
device test methods and procedures specified
in
Section 219.105(c)
of this Part through Section
219.105(f)
of this Part and by complying with the
recordkeeping and reporting requirements specified
in Section 219.404(e)
of this Part.
(Source:
Amended
at
Ill. Peg.
-
,
effective
____________
Section 219.402
Applicability
a)
The limitations of Section 219.401
of this Part apply
to all flexographic and rotogravure printing lines at
a
subject facilitysource.
All facilitiessources with

473
flexographic and/or rotogravure printing lines are
subject faciliticssources unless:
1)
Total maximum theoretical emissions of VOM from
all flexographic and rotogravure printing line(s)
(including solvents used for cleanup operations
associated with flexographic and rotogravure
printing line(s)),
at the focilitysource never
exceed
90.7
Mg
100
tons)
per
calendar year before
the application of capture systems and control
devices,
or
2)
A federally enforceable construction permit or SIP
revision for all flexographic and rotogravure
printing line(s)
at
a facilitysource requires the
owner or operator to limit production or capacity
of these printing line(s)
to reduce total VON
emissions from all flexographic and rotogravure
printing line(s)
to 90.7 Mg
(100 tons)
or less per
calendar year before the application of capture
systems and control devices.
b)
Upon achieving compliance with this Subpart,
the
source
isflexographic and rotogravure printing
lines are not required to meet Subpart
G- (Sections
219.301 or 219.302 of this Part).
Emission—s-ourccs
Flexographic and rotogravure printing lines exempt from
this Subpart are subject to Subpart G
(Sections
219.301
or
j~.?~02of this Part).
Rotogravure or
flexographic equipment used for both roll printing and
paper coating is subject to this Subpart.
c)
Once subject to the limitations of Section 219.401 ~
this Part,
a flexographic or rotogravure printing line
is always subject to the limitations of
Section 219.401
of this Part.
d)
Any owner or operator of any flexographic or
rotogravure printing line that
is exempt from the
limitations of Section 219.401 of this Part because of
the criteria
in this Section
is subject to the
recordkeeping and reporting requirements specified
in
Section 219.404(b)
of this Part.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.403
Compliance Schedule
Every owner or operator of
a flexographic and/or rotogravure
printing line shall comply with the applicable requirements of
Section 219.401 and Section 219.404
of this Part in accordance

474
with the applicable compliance schedule specified
in subsection
(a),
(b),
(c)
or
(d)
below:
a)
No owner or operator of
a flexographic or rotogravure
printing line which is exempt from the limitations of
Section 219.401
of this Part because of the criteria
in
Section 219.402
of this Part shall operate said
printing
line on or after a date consistent with
Section
219.106
of
this
Part,
unless
the
owner
or
operator has complied with,
and continues to comply
with,
Section 219.404(b)
of this Part.
b)
No owner or operator of
a flexographic or rotogravure
printing line complying by means of Section 219.401(a)
of this Part shall operate said printing line on or
after
a date consistent with Section 219.106 of this
Part,
unless the owner
or operator has complied with,
and continues to comply with,
Section 219.401(a)
~
this Part and Section 219.404(c)
of this Part.
c)
No owner or operator of
a flexographic or rotogravure
printing line complying by means
of Section 219.401(b)
of this Part shall operate said printing line on or
after a date consistent with Section 219.106 of this
Part,
unless the owner or operator has complied with,
and continues to comply with,
Section 219.401(b)
and
Section 219.404(d)
of this Part.
d)
No owner or operator of
a flexographic or rotogravure
printing line complying by means of Section 219.401(c)
of this Part shall operate said printing line on or
after a date consistent with Section 219.106 of this
Part,
unless the owner or operator has complied with,
and continues to comply with,
Section 219.401(c)
and
Section 219.404(e)
of this Part.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
___________
Section 219.404
Pecordkeeping and Reporting
a)
The VON content of each coating and ink and the
efficiency of each capture system and control device
shall
be determined by the applicable test methods and
procedures specified
in Section 219.105 of this Part to
establish the records required under this Section.
b)
Any owner or operator of
a printing line which
is
exempted from the limitations
of Section 219.401 ~
this Part because
of the criteria
in Section 219.402
of
this
Part
shall
comply
with
the
following:

475
-
1)
By
a date consistent with Section 219.106 of this
Part,
the owner or operator of
a
-f-a-cilityflexocraphic and rotogravure printing 1~p~
to which this subsection
is applicable shall
certify to the Agency that the -f-acuity
flexographic and rotogravure printing line is
exempt under the provisions of Section 219.402 Q~
this Part.
Such certification shall include:
A)
A declarati::i that the focilityf~excgrap~ig
and rotogravure printing line is exempt from
the limitations of the criteria
in Section
219.401
because of Section 219.402
of this
Part,
and
B)
Calculations which demonstrate that total
maximum theoretical emissions
of VON from all
flexographic and rotogravure printing lines
at the facilitysource never exceed 90.7 Mg
(100 tons)
per calendar year before the
application of capture systems and control
devices.
Total maximum theoretical emissions
of VON for a flexographic or rotogravure
printing facilitysource is the sum of maximum
theoretical emissions of VON from each
flexographic and rotogravure printing line at
the facilitysource.
The following equation
shall be used to calculate total maximum
theoretical emissions of VON per calendar
year before the application of capture
systems and control devices for each
flexographic and rotogravure printing line at
the facilitysource:
= A
x B
±
1095
(C x D
x
F)
where:
E~
=
Total maximum theoretical emissions
of VON from one flexographic or
rotogravure printing line in units
of kg/year
(lbs/year),-.~
A
=
Weight of VON per volume of solids
of the coating or ink with the
-
highest VON content as applied each
year on the printing line in units
of kg VON/i
(lbs VON/gal)
of
coating
or ink solidsT~

476
B
=
Total volume of solids for all
coatings and inks that can
potentially be applied each year on
the printing line in units
of
1/year
(gal/year).
The instrument
and/or method by which the owner or
operator
accurately
measured
or
calculated the volume of each
coating and ink as applied and the
amount that can potentially be
applied each year on the printing
line shall be described in the
certification to the Agency--.~
Weight
of VON per volume of
material for the cleanup material
or solvent with the highest VON
content
as used each year on the
printing line in units of Kg/l
(lbs
VON/gal)
of such material;
The greatest volume of cleanup
material or solvent used
in any
8-hour period
~
F
=
The highest fraction of cleanup
material or solvent which
is not
recycled or recovered for offsite
disposal during any 8—hour period.
2)
On and after a date consistent with Section
219.106
of this Part,
the owner or operator of a
facility referenced
in this subsection shall
collect and record all of the following
information each year for each printing line and
maintain the information at the facilitysource
for
a period of three years:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content and the volume of each
coating and ink as applied each year on each
-
printing line.
3)
On and after
a date consistent with Section
219.106 of this Part,
the owner or operator of a
facility exempted from the limitations of Section
219.401 of this Part because of the criteria
in
Section 219.402
of this Part shall notify the

477
Agency of any record showing that total maximum
theoretical emissions
of VON from all printing
lines exceed 90.7 Mg
(100 tons)
in any calendar
year before the application of capture systems and
control devices by sending
a copy of such record
to the Agency within
30
days
after
the
exceedance
occurs.
c)
Any owner or operator
of a printing line subject to the
limitations of
Sectior. 219.401
of this Part and
complying by means of Section 219.401(a)
of this Part
shall comply with the following:
1)
By a date consistent with Section 219.106
of this
Part,
or upon initial start-up of
a new printing
line,
or upon changing the method of compliance
from an existing subject printing line from
Section 219.401(b)
or Section 219.401(c)
to
Section 219.401(a)
of this Part,
the owner or
operator
of a subject printing line shall certify
to the Agency that the printing line will be
in
compliance with Section 219.401(a)
of this Part on
and after
a date consistent with Section 219.106
of
this
Part,
or
on
and
after
the
initial
start-up
date.
Such certification shall include:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content of each coating and ink as
applied each day on each printing
line.
2)
On and after
a date consistent with Section
219.106
of this Part,
or on and after the initial
start—up date,
the owner or operator of
a printing
line subject to the limitations of Section 219.401
of this Part and complying by means
of Section
219.401(a)
of this Part shall collect and record
all of the following information each day for each
coating line and maintain the information at the
facility source for a period of three years:
A)
The name and identification number of each
coating and ink as applied on each printing
line.
B)
The VON content of each coating and ink as
applied each day on each printing line.

478
3)
On and after
a date consistent with Section
219.106
of this Part,
the owner
or operator of
a
subject printing line shall notify the Agency
in
the following instances:
A)
Any record showing violation of Section
219.401(a)
of this Part shall
be reported
by
sending a copy of such record to the Agency
within
30 days following the occurrence
of
the violation.
B)
At least 30 calendar days before changing the
method
of compliance with Section 219.401 Q~I
this Part from Section
219.401(a)
to Section
219.401(b)
or
(c)
of this Part,
the owner or
operator shall comply with all requirements
of subsection
(b) (1)
or
(c) (1) (d) (1)
or
(e) (1)
of this Section, respectively.
Upon
changing the method
of compliance with
Section 219.401 of this Part from Section
219.401(a)
to Section 219.401(b)
or
(c)
of
this Part, the owner or operator shall comply
with all requirements of subsection
--~J
or
-fe-)-(e)
of this Section, respectively.
d)
Any owner or operator
of
a printing line subject to the
limitations of Section 219.401
of this Part and
complying by means of Section 219.401(b)
of this Part
shall comply with the following:
1)
By
a date consistent with Section 219.106 of this
Part,
or upon initial start-up
of
a new printing
line,
or upon changing the method of compliance
for an existing subject printing line from Section
219.401(a)
or
(c)
to Section 219.401(b)
of this
Part,
the owner or operator of the subject
printing line shall certify to the Agency that the
printing line will be
in compliance with Section
219.401(b)
of this Part on and after a date
consistent with Section 219.106 of this Part,
or
on and after the initial start-up date.
Such
certification shall include:
A)
The name and identification number of each
printing line which will comply by means
of
Section 219.401(b)
of this Part.
B)
The name and identification number of each
coating and ink available for use on each
printing line.

479
C)
The VON content of each coating and ink as
applied each day on each printing line.
D)
The instrument or method by which the owner
or
operator
will
accurately
measure
or
calculate
the
volume
of
each
coating
and
ink
as applied each day on each printing line.
E)
The method by which the owner or operator
will create and maintain records each day as
required
in
subsection
-fb)-j~J.j2) of this
Section.
F)
An example of the format in which the records
required
in subsection
-
*L~J~j2)of this
Section will be kept.
2)
On and after
a date consistent with Section
219.106
of this Part,
or on and after the initial
start—up date,
the owner or operator of
a printing
line subject to the limitations of
Section 219.401
and complying by means
of Section 219.401(b)
~
this Part shall collect and record all
of the
following information each day for each printing
line and maintain the information at the
facilitysource
for
a
period
of
three
years:
A)
The name and identification number of each
coating and ink as applied
on each printing
line.
B)
The VON content and the volume of each
coating and ink as applied each day on each
printing line.
C)
The daily-weighted average VON content of all
coatings and inks as applied on each printing
line.
3)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator of
a
subject printing line shall notify the Agency
in
the following instances:
A)
Any record showing violation of Section
219.401(b)
of this Part shall
be reported
by
sending
a copy of such record to the Agency
within 30 days following the occurrence of
the violation.
B)
At least
30 calendar days before changing the
method of compliance with Section 219.401 ~

480
this
Part
from
Section
219.401(b)
to
Section
219.401(a)
or 219.401(c)
of this Part,
the
owner or operator shall comply with all
requirements of subsection
(c) (1)
or
(e) (1)
of this Section, respectively.
Upon changing
the method of compliance with Section 219.401
of this Part from Section 219.401(b)
to
Section 219.401(a)
or
(a)
of this Part,
the
owner or operator shall comply with all
requirements of subsection
(c)
or
(e)
of this
Section, respectively.
e)
Any owner or operator of
a printing line subject to the
limitations of Section 219.401
of this Part and
complying by means of Section 219.401(c)
of this Part
shall comply with the following:
-
1)
By
a date consistent with Section 219.106 of this
Part,
or upon initial start—up of
a new printing
line,
or upon changing the method of compliance
for an existing printing line from Section
219.401(a)
or
(b)
to
Section
219.401(c)
of
this
Part, the owner
or operator of the subject
printing line shall perform all tests and submit
to
the
Agency
the
results
of
all
tests
and
calculations necessary to demonstrate that the
subject printing line will be in compliance with
Section 219.401(c)
of this Part on and after a
date consistent with Section 219.106 of this Part,
or on and after the initial start—up date.
2)
On and after a date consistent with Section
-
219.106
of this Part,
or on and after the initial
start-up date,
the owner or operator of a printing
line subject to the limitations of Section 219.401
of this Part
and. complying
by means
of Section
219.401(c)
of this Part shall collect and record
all
of the following information each day for each
printing line and maintain the information at the
facility for
a period of three years:
A)
Control device monitoring data.
B)
A log of operating time for the capture
system,
control device, monitoring equipment
and the associated printing
line.
C)
A maintenance log for the capture system,
control device and monitoring equipment
detailing all routine and non-routine

481
maintenance performed including dates and
duration of any outages.
3)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator of
a
subject printing line shall notify the Agency
in
the following instances:
A)
Any record showing violation of Section
219.401(c)
this Part,
shall be reported by
sending
a copy of such record to the Agency
within
30 days following the occurrence of
the
violation.
B)
At least
30 calendar days before changing the
method of compliance with Section 219.401 Q~
this Part from Section 219.401(c)
to Section
219.401(a)
or
(b)
of this Part,
the owner
or
operator shall comply with all requirements
of subsection
(c) (1)
or
(d) (1)
of this
Section, respectively.
Upon changing the
method
of compliance with Section 219.401 g~
this Part from Section 219.401(c)
to Section
219.401(a)
or
(b)
of this Part,
the owner
or
operator shall comply with all requirements
of subsection
(c)
or
(d)
of this Section,
respectively.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.405
Heatset-Web-Offset Lithographic Printing
a)
Applicability
1)
The limitations of subsection
(b) below apply to
all heatset-web—offset lithographic printing lines
at
a subject focilitysource.
All facilities
sources with heatset-web-offset lithographic
printing lines are subject facilities sources
unless:
A)
Total maximum theoretical emissions of VON
from all heatset-web-offset lithographic
printing lines j~pc1uding solvents used for
cleanup operations associated with the
heatset—web-offset lithographic printing
line(s))
at the facilitysource never exceed
90.7 Mg
(100 tons) per calendar year
in the
absence
of air pollution control equipment,
or
-

482
B)
A federally enforceable construction permit
or SIP revision for all heatset—web-offset
lithographic printing lines(s)
at a
facilitysource
requires
the
owner
or
operator
to limit production or capacity of these
printing line(s)
to reduce total VON
emissions from all heatset—web—offset
lithographic printing line(s)
to 90.7 Mg
(100 tons)
per calendar year or less
in the
absence
of
air
pollution
control
equipment,
and
2)
Any owner or operator of any heatset—web-offset
lithographic printing line that is exempt from the
limitations
in subsection
(b)
of this Section
because of the criteria
in subsection
(a) (1)
of
this Section
shall
be subject to the recordkeeping
and reporting requirements
in subsection
(c) (1)
~
this Section.
b)
Specific Provisions.
No owner or operator of
a subject
heatset—web-offset
printing
line
may
cause
or
allow
the
operation
of
the
subject
heatset—web-off
set
printing
line unless the owner or operator meets the
requirements
in
subsection
(b)
(1)
or
(b)
(2)
and
the
requirements
in
subsections
(b)
(3)
and
(b)
(4)
below.
1)
An afterburner system is installed and operated
that reduces 90 percent of the VOM emissions from
the dryer exhaust,
or
2)
The fountain solution contains no more than
8 percent,
by weight,
of VON and a
condensation
recovery system is installed and operated that
removes at least
75 percent
of the non—isopropyl
alcohol organic materials from the dryer exhaust,
and
3)
The control device
is equipped with the applicable
monitoring equipment specified
in Section
219.105(d) (2)
of this Part and the monitoring
equipment
is installed,
calibrated,
operated and
maintained according to vendor specifications at
all times the control device
is
in use,
and
4)
The control device
is operated at all times when
the subject printing line is in operation.
The
owner or operator shall demonstrate compliance
with this Section by using the applicable test
methods and procedures specified
in Section
219.105(a),
(d),
and
(f)
of this Part and
by

483
complying with the recordkeeping and reporting
requirements specified
in subsection
(c) below.
c)
Recordkeeping and Reporting.
The VON content of each
fountain solution and ink and the efficiency of each
control device shall be determined by the applicable
test methods and procedures specified in Section
219.105 of this Part to establish the records required
under this subsection.
1)
Any owner or operator of a printing line which
is
exempted from the limitations of subsection
(b) ?2~1
this Section because of the criteria in subsection
(a)
of this Section shall comply with the
following:
-
A)
By
a date consistent with Section 219.106
Qf
this Part,
the owner or operator of
a
facility
heatset—web-offset lithographic
printing line to which subsection
(c) (1)
of
this Section
is applicable shall certify to
the Agency that the facility is heatset-
web-offset lithographic printing line exempt
under the provisions of subsection
(a)
~
this Section.
Such certification shall
include:
i)
A declaration that the facility heatset-
web-offset lithographic printing line
is
exempt from the limitations of
subsection
(b)
of this Section because
-
of the criteria
in subsection
(a)
of
this Section, and
ii)
Calculations which demonstrate that
total maximum theoretical emissions
of
VON from all heatset—web-offset
lithographic printing lines at the
facilitysource never exceed 90.7 Mg
(100 tons)
per calendar year before the
application of air pollution control
equipment.
Total maximum theoretical
emissions of VON for a heatset—
web-offset lithographic printing
facility source
is the sum of maximum
theoretical emissions of VON from each
heatset-web—offset lithographic printing
line at the facility.
The following
equation shall be used to calculate
total maximum theoretical emissions
of
VON per calendar year
in the absence
of
air pollution control equipment for each

484
heatset-web-offset lithographic printing
line at the facilitysource.
=
(A
x B)
+
(C x D)+1095
(F x G x H)
100
where:
=
Total maximum theoretical
emissions
of VON from one
heatset-web-off
set
printing
line in units of kg/year
(lbs/year),-j
A
=
Weight of VON per volume of
solids of ink with the highest
VON content as applied each
year on the printing line
in
units of kg VOM/l
(lbs
VOM/gal)
of solidsT ~
B
=
Total volume of solids for all
inks that can potentially be
applied each year on the
printing line
in units of
1/year
(gal/year).
The
instrument or method by which
the owner or operator
accurately measured or
calculated the volume of each
ink
as applied and the amount
that can potentially be
applied each year on the
printing line shall
be
described
in the certification
to the Agency~-.~
C
=
The weight percent VON of the
fountain solution with the
highest VON content-~
D
=
The total volume of fountain
solution that can potentially
be used each year on the
printing line
in units
of
1/year
(gal/year).
The
instrument and/or method by
which the owner or operator
accurately measured or
calculated the volume of each
fountain solution used and the

485
amount that can potentially be
used
each
year
on
the
printing
line shall be described
in the
certification to the Agency-ri
F
=
Weight
of
VON
per
volume
of
material for the cleanup
material or solvent with the
~jghest
VON content
as used
each year on the printing line
in units of Kg/i
(lbs
VON/gaL)
of such material;
The greatest volume of cleanup
material or solvent used in
any 8—hour period
~nc~
The highest fraction of
cleanup material or solvent
which
is not recycled or
recovered for offsite disposal
during any 8-hour period.
B)
On and after a date consistent with Section
219.106 of this Part,
the owner or operator
of
a facility heatset-web-offset lithographic
printing line to which subsection
(a) (1)
~
this
Section is applicable shall collect and
record all of the following information each
year for each printing line and maintain the
information at the facilitysource for a
period of
three years:
i)
The name and identification of each
fountain solution and ink
as applied on
each printing line.
ii)
The VON content and the volume of each
fountain solution and ink as applied
each year on each printing line.
C)
On and after a date consistent with Section
219.106 of this Part,
the owner or operator
of a facilityheatset—web—offset lithographic
printing
line exempted from the limitations
of subsection
(b)
of this Section because
of
the criteria in subsection
(a)
of this
Section shall notify the Agency of any record
showing that total maximum theoretical
emissions of VON from all printing lines
exceed 90.7 Mg
(100 tons)
in any calendar
year
in the absence of
air
pollution control

486
equipment by sending a copy of such record to
the Agency within 30 days after the
exceedance occurs.
2)
Any owner
or operator of
a printing line subject
to the limitations of subsection
(b)
of this
Section and complying by means of subsection
(b) (1)
of this Section shall comply with the
following:
A)
By
a date consistent with Section 219.106
~
this Part,
or upon initial start—up of a new
printing
line,
or upon changing the method of
compliance
for an existing printing line from
subsection
(b) (2) to subsection
(b) (1)
of
this Section
the owner or operator of the
subject printing line shall perform all tests
and submit to the Agency the results of all
tests and calculations necessary to
demonstrate that the subject printing line
will be in compliance with subsection
(b) (1)
of this Section onand
after
a date
consistent with Section 219.106 of this Part,
or on and after the initial start-up date.
B)
On and after a date consistent with Section
219.106
of this Part,
or on and after the
initial
start-up date,
the owner
or operator
of
a printing line subject to the limitations
of
subsection
(b)
of
this
Section
and
complying by means of
subsection
(b) (1)
~
this Section shall collect and record the
following information each day for each
printing line and maintain the information at
the facilitysource for a period of three
years:
i)
Control device monitoring data.
ii)
A log of operating time for the control
device,
monitoring equipment and the
associated printing line.
iii) A maintenance log for the control device
and monitoring equipment detailing all
routine and nonroutine maintenance
performed including dates and duration
of any outages.
C)
On and after
a date consistent with Section
219.106
of this Part, the owner
or operator

487
of
a subject printing line shall notify the
Agency
in the following instances:
i)
Any record showing violation of
subsection
(b)
(1)
of this Section shall
be
reported
by
sending
a copy of such
record to the Agency within
30
days
following the occurrence of the
violation.
ii)
At least
30 calendar days before
changing the method of compliance with
subsection
(b)
of this Section from
subsection
(b) (1)
to
(b) (2)
of this
Section, the owner or operator shall
comply with all requirements of
subsection
(c) (3) (A)
of this Section.
Upon changing the method of compliance
with subsection
(b) from subsection
(b) (1)
to
(b) (2)
of this Section,
the
owner
or
operator shall comply with all
requirements
of subsection
(c) (3) ~
this Section.
3)
Any owner or operator
of
a printing line subject
to
the
limitations
of
subsection
(b)
of this
Section and complying by means of subsection
(b) (2). of this Section shall comply with the
following:
A)
By
a
date
consistent
with
Section
219.106
~
this Part,
or upon initial
start-up of
a new
printing line,
or upon changing the method of
compliance for an existing printing line from
subsection
(b) (1) to
(b) (2)
of this Section
the owner or operator of the subject printing
line shall perform all tests and submit to
the Agency and the USEPA the results of all
tests and calculations necessary to
demonstrate that the subject printing line
will be
in compliance with subsection
(b) (2)
of
this
Section
on
and after a date
consistent -with Section 219.106
of this Part,
or
on
and
after
the initial start-up date.
B)
On
and
after
a
date
consistent with Section
219.106
of this Part,
or
on
and
after
the
initial start-up date, the owner or operator
of
a printing line subject to the limitations
of subsection
(b)
of this Section and
complying by means
of subsection
(b) (2)
~
this Section shall collect and record the

488
following information each day for each
printing line and maintain the information at
the facilitysource for a period of three
years:
i)
The VON content of the fountain solution
used each day on each printing line.
ii)
A log of operating time for the control
device and the associated printing line.
iii)
A
maintenance
log
for
the
control
device
detailing all routine and non—routine
maintenance performed including dates
and duration of any outages.
C)
On and after
a date consistent with Section
219.106
of this Part,
the owner or operator
of
a
subject printing line shall notify the
Agency
in the following
instances:
i)
Any record showing violation of
subsection
(b) (2)
of this Section shall
be
reported
by
sending
a
copy
of
such
record to the Agency within 30 days
following the occurrence of the
violation.
ii)
At least 30 calendar days before
changing the method of compliance with
subsection
(b)
of this Section from
subsection
(b) (2)
to
(b) (1)
of this
Section, the owner or operator shall
comply with all requirements
of
subsection
(c) (2) (A)
of this Section.
Upon changing the method of compliance
with subsection
(b) from subsection
(b) (2)
to
(b) (1)
of this Section,
the
owner or operator shall
comply with all
requirements of subsection
(c) (2) ~
this Section.
d)
Compliance Schedule.
Every owner
or operator of a
heatset-web-offset lithographic printing line shall
comply with the applicable requirements
of subsections
-
(b)
and
(c)
of this Section
in accordance with the
applicable compliance schedule specified
in subsection
(d) (1)
,
(d) (2)
,
or
(d)
(3)
below:
1)
No owner or operator of
a heatset—web-offset
lithographic printing line which
is exempt from
the limitations of subsection
(b)
of this Section

489
because of the criteria
in subsection
(a)
of this
Section shall operate said printing line on or
after
a date consistent with Section 219.106 of
this Part,
unless the owner or operator has
complied with,
and continues to comply with,
subsection -(-b)-j~j~.(l)and
(a) (1)
of this Section.
2)
No owner or operator of
a heatset—web—offset
lithographic
printing
line
complying
by
means
of
subsection
(b)
(1)
of
this Section shall operate
said
printing
line
on
or
after
a
date
consistent
with Section 219.106 of this Part, unless the
owner
or
operator
has
complied
with,
and
continues
to
comply with,
subsection
(b) (2) (b) (1).
(b) (3)
(b) (4) and
(a) (2)
of this Section.
3)
No owner or operator of a heatset-web-offset
lithographic printing line complying by means
of
subsection
(b) (2)
of this Section shall operate
said printing line on or after a date consistent
with Section 219.106 of this Part,
unless the
owner or operator has complied with,
and continues
to comply with,
subsection
(b) (2)
,
(b) (3)
,
(b) (4)
and
(c) (3)
of this Section.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
SUBPART Q:
LEAKS FROM SYNTHETIC ORGANIC CHEMICAL AND POLYMER
MANUFACTURING EQUIPMENT PLANT
Section 219.421
General Requirements
The
owner
or
operator
of
a
plant
which
processes
more
than
3660
mg/yr
(4033 tons/year)
gaseous and light liquid VON,
and whose
components are used to manufacture the synthetic organic
chemicals or polymers listed in Appendix A,
shall comply with
this Subpart.
The provisions
of this Subpart are applicable to
components
containing
10
percent
or
more
by weight VON as
determined by ASTM method E-l68,
E-169 and E-260,
incorporated by
reference in Section 219.112 of this Part.
Those components that
are not process unit components are exempt from this Subpart.
A
component shall
be considered to be leaking
if the VON is equal
to,
or is greater than 10,000 ppmv as methane
or
hexane
as
determined by USEPA Reference Method
21, as specified at
40 CFR
60, Appendix A,
incorporated by reference
in Section 219.112 ~
this Part,
indication of liquids dripping,
or indication by a
sensor that
a seal or barrier fluid system has failed.
The
provisions of this Subpart are not applicable
if the equipment
components are used to produce heavy liquid chemicals only from
heavy liquid feed or raw materials.

490
(Source:
Amended
at
Ill.
Reg.
______
,
effective
____________
Section 219.422
Inspection Program Plan for Leaks
The owner or operator of
a synthetic organic chemical or polymer
manufacturing plant subject to Section 219.421 of this Part shall
prepare an inspection program plan which contains,
at a minimum:
a)
An
identification
of
all
components
and
the
period
in
which each will be monitored pursuant to Section
219.423
of this Part.
b)
The
format
for
the
monitoring
log
required
by
Section
219.425
of
this
Part.
c)
A description of the monitoring equipment to be used
when complying with Section 219.423
of this Part,
and
d)
A description of the methods to be used to identify all
pipeline
valves,
pressure
relief
valves
in
gaseous
service,
all leaking components,
and
components
exempted under Section
2l9.423-(4-)-jjj.. ~
this Part such
that they are obvious and can be located by both plant
personnel performing monitoring and Agency personnel
performing
inspections.
(Source:
Amended at
Ill. Peg.
______
,
effective
____________
Section
219.423
Inspection
Program
for
Leaks
The owner or operator of a synthetic organic chemical or polymer
manufacturing plant subject to this ~subpart
shall,
for the
purposes
of detecting leaks, conduct a component inspection
program using the test methods specified
in Method
21,
40 CFR 60,
Appendix A
(1986),
incorporated by reference
in Section 219.112
of
this
Part,
consistent
with
the
following
provisions:
a)
Test annually those components operated near extreme
temperature or pressure such that they would be unsafe
to routinely monitor and those components which would
require the elevation of monitoring personnel higher
than two meters above permanent worker access
structures or surfaces.
b)
Test quarterly all other pressure relief valves
in gas
service, pumps
in light liquid service, valves
in light
liquid service and in gas service,
and compressors.
c)
If
less
than
or
equal to
2
percent
of
the
valves
in
light
liquid service and
in gas service tested pursuant

491
to subsection
(b)
of this Section are found ~e-~to leak
for
five
consecutive
quarters,
no
leak
tests
shall
be
required for three consecutive quarters.
Thereafter,
leak tests shall resume for the next quarter.
If that
test shows less than or equal to
2 percent of the
valves
in
light
liquid
service
and
in
gas
service
are
leaking,
then
no
tests
are
required
for
the
next
three quarters.
If more than
2 percent are leaking,
then
tests
are
required
for
the
next
five
quarters.
d)
Observe visually all pump seals weekly.
e)
Test immediately any pump seal from which liquids are
observed dripping.
f)
Test any relief valve within 24 hours after
it has
vented to the atmosphere.
g)
Routine instrument monitoring of valves which are not
externally regulated,
flanges,
and equipment in heavy
liquid service,
is not required.
However,
any valve
which
is
not
externally
regulated,
flange
or
piece
of
equipment in heavy liquid service
tliat
is found to be
leaking on the basis of sight,
smell or sound shall
be
repaired
as
soon
as
practicable
but
no
later
than
30 days after the leak
is found.
-
h)
Test immediately after repair any component that was
found leaking.
i)
Within one hour of its detection,
a weatherproof,
readily visible tag,
in bright colors such as red or
yellow,
bearing an identification number and the date
on which the leak was detected must be affixed on the
leaking component and remain
in place until the leaking
component
is repaired.
j)
The following components are exempt from the monitoring
requirements
in this Section:
1)
Any component that is
in vacuum service,
and
2)
Any pressure relief valve that
is connected to an
operating flare header or vapor recovery device.
(Source:
Amended at
Ill. Peg.
______,
effective
___________

492
Section 219.424
Repairing Leaks
All leaking components must be repaired and
retested as soon as
practicable
but
no
later
than
15
days
after
the leak
is found
unless the leaking component cannot be repaired until the process
unit
is shut down.
Records of repairing and retesting must be
maintained
in accordance with Section 219.425 and 219.426
of this
Part.
(Source:
Amended
at
_____
,
Ill.
Peg.
-
,
effective
Section
219.425
Recordkeeping for Leaks
a)
The owner or operator of
a synthetic organic chemical
or.
polymer
manufacturing
plant
shall
maintain
a
leaking
components monitoring log which shall contain,
at a
minimum, the following information:
1)
The name of the process unit where the component
is located;
2)
The
type
of
component
(e.g.,
valve,
seal);
3)
The identification number of the component;
4)
The date on which a leaking component is
discovered;
5)
The date on which
a leaking component
is repaired;
6)
The date and instrument reading of the recheck
procedure after
a leaking component
is repaired;
7)
A record of the calibration of the monitoring
instrument;
8)
The identification number of leaking components
which cannot be repaired until process unit
shutdown;
and
9)
The total number of valves
in light liquid service
-
and in gas service inspected; the total number and
the percentage of these valves found leaking
during the monitoring period.
b)
Copies of the monitoring log shall be retained by the
owner
or
operator
for
a
minimum
of
two
years
after
the
date on which the record was made or the report was
prepared.

493
c)
Copies
of the monitoring log shall be made available to
the Agency~upon verbal
or written request~prior to or
at the time
of inspection pursuant to Section 4(d)
of
the Environmental Protection Act
(Act)
(Ill.
Rev.
Stat.
l98-9.~.i,
ch.
111½, pars.
1001
et
seq.)
1415
ILCS
5/1
et
seq.)
at any reasonable time.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
_____________
Section
219.426
Report for Leaks
The
owner
or
operator
of
a
synthetic
organic
chemical
or
polymer
manufacturing
plant
subject
to
Section
219.421
through
219.430
Q~.
this Part shall:
a)
Submit quarterly reports to the Agency on or before
March 31, June
30, September
30, and December
31 of
each
year,
listing all leaking components identified
pursuant to Section 219.423
of this Part but not
repaired within
15 days,
all leaking components
awaiting process unit shutdown,
the total number of
components
inspected,
the
type
of
components
inspected,
and the total number of components found leaking, the
total number of valves
in light liquid service and in
gas
service
inspected
and
the
number
and
percentage
of
valves
in light liquid service and
in gas service found
leaking.
b)
Submit
a
signed
statement
with
the
report
attesting
that all monitoring and repairs were performed as
required under Section 219.421 through 219.427 of this
Part.
(Source:
Amended
at
Ill.
Peg.
______
,
effective
_____________
Section 219.427
Alternative Program for Leaks
The Agency shall approve an alternative program of monitoring,
recordkeeping,
or reporting to that prescribed
in this Subpart
upon
a demonstration by the owner or operator of such plant that
the alternative program will provide plantsource personnel and
Agency
personnel
with
an
equivalent
ability
to
identify
and
repair leaking components.
Any alternative program can be
allowed when approved by the Agency and approved by the USEPA as
a SIP revision.
(Source:
Amended at
Ill.
Peg.
______
,
effective
_____________

494
Section
219.428
Open-Ended Valves
a)
Each open-ended valve shall be equipped with a cap,
blind flange, plug,
or a second valve,
except during
operations requiring fluid flow through the open-ended
valve.
b)
-Each open—ended valve equipped with a second valve
shall
be
operated
in
a
manner
such
that
the
valve
on
the process fluid end is closed before the second valve
is
closed.
c)
Components which are open—ended valves and which serve
as
a sampling connection shall be controlled
such that
they comply with subsection
(c) (1)
,
(c) (2)
or
(c) (3)
below.
This requirement does not apply to in-situ
sampling systems.÷
1)
A closed purge system or closed vent system shall
return purged process fluid to the process line
with no detectable volatile organic material
emissions to the atmosphere, or
2)
A closed purge system or closed vent system shall
collect
and
recycle
purged
process
fluid
to
the
process line with no detectable volatile organic
-
material emissions to the atmosphere,
or
3)
Purged
process
fluid shall be transported to a
control device that complies with the requirements
of Section 219.429
of this Part.
If
a container
is used to transport purged process fluid to the
control device, the container shall
be
a closed
container designed and used to reduce the VON
emissions vented from purged process fluid after
transfer to no detectable VON emissions as
determined by USEPA Reference Method 21,
as
specified
in
40 CFR
60, Appendix A (1990
or
1991)
incorporated by reference in Section 219.112
of
this Part.
For purposes of this Section,
the
phrase “after transfer” shall refer to the time at
which the entire amount of purged process fluid
resulting from a flushing or cleaning of the
sample line enters the container, provided,
however,
that purged process fluid may be
transferred from the initial container to another
closed container prior to disposal,
e.g.,
to
a
bulk waste storage container.
d)
In-situ sampling
syu~ems
are
exempt
from
subsectiofl
(c)

495
(Source:
Amended at
_____
,
Ill.
Peg.
______
,
effective
__________
Section 219.429
Standards
for Control Devices
Control devices used to comply with Section 219.428(c)
of this
Part shall comply with the following:
a)
If the control device is a vapor recovery system
(for
example,
condensers
and. adsorbers),
it shall be
designed
and
operated
to recover the volatile organic
material emissions vented to it with an efficiency of
95
percent
or
greater.
b)
If the control device is an enclosed combustion device,
it shall be designed and operated to reduce the
volatile organic material emissions vented to it with
an
efficiency
of
95
percent
or
greater,
or
to
provide
a
minimum residence time
of 0.75 seconds at a minimum
temperature of 816°C.
c)
If the control device is
a flare,
it shall:
1)
Be designed for and operated with no visible
emissions
as determined by USEPA Reference Method
22,
40 CFP 60, Appendix A (1986),
incorporated by
reference
in
Section
219.112
of this Part,
except
for periods not to exceed a total of
5 minutes
during any 2 consecutive hours.
2)
Be operated with
a pilot flame present at all
times -and shall be monitored with a thermocouple
or any other equivalent device to detect the
presence of the pilot flame.
3)
Be steam-assisted,
air—assisted,
or nonassisted.
4)
Be used only with the net heating value of the gas
being combusted being
11.2 NJ/scm
(300 Btu/scf)
or
greater
if
the
flare
is
steam—assisted
or
air-
assisted;
or
with
the
net
heating
value
of
the
gas
being combusted being 7.45 NJ/scm or greater
if
the flare
is nonassisted.
The net heating value
of the gas being combusted shall be calculated
using the following equation:
n
Hr
=
K
E
C1H
i=1

496
Where:
H1
=
Net heating value of the sample
in
NJ/scm;
where the net enthalpy per
mole of offgas
is based on
combustion
at
25°C
and
760
mm
Hg,
but the standard temperature for
determining
the
volume
corresponding to one mole
is 20°C~r.i
K
=
Constant,
1.740 x 10°
(1/ppm) (g-mole/scm) (NJ/Kcal)
where
standard
temperature
for (g-mole/scm)
is
Cl
=
Concentration
of sample component
i,
in ppm,
as measured by USEPA
Reference Method
18,
40 CFR 60,
Appendix A (1986),
and ASTM D
2504-83, both incorporated by
reference in Section 219.112 of
this Part-ri
H
=
Net heat of combustion of sample
component
i, kcal/g mole.
The
heats of combustion may be
determined using ASTN D 2382—83,
incorporated by reference
in
Section 219.112
of this Part,
if
published values are not available
or cannot be calculated.
5)
Steam-assisted and nonassisted flares shall
be
designed and operated with an exit velocity,
as
determined by dividing the volumetric flowrate
(in
units of standard temperature and pressure),
as
determined by USEPA Reference Method
2 or 2A,
40
CFR 60, Appendix A (1986)
incorporated by
reference
in
Section
219.112
of this Part,
as
appropriate;
by
the
unobstructed
(free)
cross
sectional area of the flare tip,
less than
18
m/sec
(60
ft/sea).
6)
Air—assisted
flares shall be designed and operated
with an exit velocity less than the maximum
permitted velocity,
~
as determined by the
following equation:

497
V~
8.706
+
0~7084(Hr)~.i
v~
Maximum permitted
velocity, m/sec--~
8.706
Constant--~j
0.7084
Constant~-.j
Hr
The
net
heating
value
as
determined
in
subsection
(a) (4)
of this section.
d)
If the control device
is a closed container,
it shall
be designed and operated to reduce the volatile organic
material emissions,
vented from purged process fluid
after transfer, to
no detectable volatile organic
material emissions as determined by UCEPA Reference
Method 21
as specified at 40 CFR 60, Appondi~A
(1986),
incorporated
by reference in Section 219.112.
For
purposes
of this Section, the phrase “after
transfer”
shall refer to the time at which the entire amount of
purged process fluid resulting from
a flushing or
cleaning of the -sample line enters the closed container
or containers including the final container(s) prior to
disposal.
The
following
information
pertaining
to
closed vent systems and control devices subject to
Section
219.429
shall
be
maintained
by
the
owner
or
operator.
These
records
shall
be
updated
as
necessary
to describe current operation and equipment.
The
records shall be retained as a readily accessible
location
at
the
source
for
a
minimum-
of
two
years
after
the
control
device
is
permanently
shutdown.
~J..
Detailed schematics, design specifications,
and
piping and instrumentation diagrams
21
The dates and description of any changes in design
s~pecifications
~J.
A description of the parameter or parameters
monitored and recorded as required
in subsection
(f) (1) to ensure that the control devices are
operated and maintained
in conformance with their
design and an explanation why that parameter
(or
parameters)
was selected for monitoring.
The owner or
rn-~r~-cpr
or
a control device shall monitor
tnc
controi
aevice
to
ensure tnat
it
is
opcr~cea
ana
m-aintaincd in conformance with the manufacturer’s
specifications,
modified
to
the
particular
process
design.
~e)
The control device shall
be operated at all times when
emissions may be vented to it.

498
~fj
Owners and operators of control devices used to comply
-
with this Subpart
shall monitor each control device to
ensure that the control device
is operated and
maintained
in conformance with its designs at all times
that emissions may be vented to
it.
This monitoring
shall be conducted in accordance with Section
2l9.429(d)(3).
The records prepared. as part of this
monitoring activity shall include the dates of startup
and shutdown of control devices and identify periods
when the devices are not operated as designed,
including periods when
a flare pilot light does not
have a flame.
gj~
The requirements
of subsections
(d)
,
(e) and
(f)
shall
not apply to
a combustion device located at the source
used for disposal
of purged process fluid which
is
subject to the Burning of Hazardous Waste in Boilers
and Industrials Furnaces
(BIF)
rules,
40 CFR Parts 260,
261,
264,
265,
266
and 270,
or which is subject to the
Resource Conservation and Recovery Act
(RCRA)
rules,
35
Ill.
Adm.
Code Parts 703,
720,
721,
724,
725 and 726.
-
The owner or operator of such combustion device shall
satisfy applicable provisions
of the PCPA or BIF rules.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 219.430
Compliance Date
(Repealed)
The owner or operator
of
a synthetic organic chemical or polymer
manufacturing plant subject to 35
Ill. Adm,
Code 215.430 through
215.438
as
of December
31
-
1987
shall
have
complied
with
the
standards and limitations
of those Sections no later than
December
31,
1087.
(Source:
Repealed at
Ill. Peg.
______
,
effective
___________
-SUBPART R:
PETROLEUM REFINING AND RELATED INDUSTRIES;
ASPHALT MATERIALS
Section 219.441
Petroleum Refinery Waste Gas Disposal
a)
Except as provided
in subsection
(b)
or
(C)
of this
Section,
no person shall cause or allow the discharge
of organic materials
in excess of 100 ppm equivalent
methane
(molecular weight
16.0)
into the atmosphere
from:
1)
Any catalyst regenerator of a petroleum cracking
system;
or

499
2)
Any petroleum fluid
coker; or
3)
Any other waste gas stream from any petroleum or
petrochemical manufacturing process.
b)
Exception.
Existing sources subject to subsection
(a) (3)
of this Section may, alternatively,
at their
election,
comply with the organic material emission
limitations
imposed
by
35
Ill.
Adm.
Code
21~.30l
or
21~.302; provided,
however, that there shall
be
no
increase
in
emissions
from
such
sources
above
the
level
of emissions in existence on May
3,
1979.
c)
New
Sources.
Sources
subject
to
subsection
(a)
(3)
~
this Section, construction
of which commenced on or
after January
1,
1977,
may,
at their election,
comply
with the following emission limitations:
1)
A maximum of eight pounds per hour of organic
material; or
2)
Emission of organic material
in excess of
the
limitation of subsection
(c) (1)
of this Section
is
allowable
if
such
emissions
are
controlled
by
air
pollution
control methods or equipment approved by
the Agency capable of reducing by 85 percent
or
more
the
uncontrolled
organic
material
that
would
otherwise be emitted to the atmosphere.
Such
methods or equipment must be approved by the
Agency
and. approved by the USEPA as
a SIP
revision.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.443
Wastewater
(Oil/Water)
Separator
No owner or operator of a petroleum refinery shall operate any
wastewater
(oil/water) separator at a petroleum refinery unless
the separator
is equipped with air pollution control equipment
capable of reducing by 85 percent or more the uncontrolled
organic material emitted to the atmosphere.
If no odor nuisance
exists, the limitation of this Section shall not apply
if the
vapor pressure of the organic material
is below 10.34 kPa
(1.5
psia)
at 2f~4.3°K(70°F) at all times.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.445
Leaks:
General Requirements
es-The
owner
or
operator
of
a
petroleum
refinery
shall:

500
.~-a)
Develop
a monitoring program plan consistent with the
provisions
of Section
219.446
of
this Part
2-b)
Conduct
a monitoring program consistent with the
provisions of Section 219.447
of this Part
~)
Record all leaking components which have a volatile
organic material concentration exceeding 10,000 ppm
consistent with the provisions of Section 219.448
~
this Part
4~)
Identify each component consistent with the monitoring
program plan submitted pursuant to Section 219.446 ~
this Part
S-e)
Repair and retest the leaking
components
as soon as
possible within 22 days after the leak
is found, but no
later than June
1 for the purposes of Section
219.447(a) (1) of this Part, unless the leaking
components cannot be repaired until the unit
is shut
down for turnaround; and
Gf)
Report to the Agency consistent with the provisions of
Section 219.449
of this Part.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.446
Monitoring Program Plan for Leaks
The owner or operator of a petroleum refinery shall prepare
a
monitoring program plan which contains, at a minimum:
a)
An identification of all refinery components
and. the
period
in
which each will be monitored pursuant to
Section 219.447
of this Part
b)
The format for the monitoring log required by Section
219.448
of this Part
a)
A description of the monitoring equipment to be used
pursuant to Section 219.447
of this Part
and
d)
A description of the methods to be used to identify all
pipeline valves,
pressure relief valves in gaseous
service and all leaking components
such that they are
obvious to both refinery personnel performing
monitoring and Agency personnel performing inspections.
(Source:
Amended. at
_____
,
Ill.
Peg.
______
,
effective

-
501
Section 219.447
Monitoring Program for Leaks
a)
The owner or operator of
a petroleum refinery subject
to Section 219.445 of this Part shall,
for the purpose
of detecting leaks,
conduct a component monitoring
program consistent with the following provisions:
1)
Test once between March
1 and June
1 of each year,
by methods referenced in Section 219.105(g)
~
this Part,
all pump seals, pipeline valves in
liquid service and process drains--;~
2)
Test once each quarter of each calendar year,
by
methods referenced
in Section 219.105(g)
of this
Part,
all pressure relief valve-s
in gaseous
service, pipeline valves
in gaseous service and
compressor seals--j
3)
Inaccessible valves may be tested once each
calendar year instead of once each quarter of each
calendar year~~-~j
4)
Observe visually all pump seals weekly---;
5)
Test immediately any pump seal from which liquids
are observed dripping-1j
6)
Test any relief valve within 24 hours after it has
vented to the atmosphereT.L and
7)
Test immediately after repair any component that
was found leaking.
-
b)
Storage tank valves and pressure relief devices
connected to an operating flare header or vapor
recovery device are exempt from the monitoring
requirements
in subsection
(a)
of this Section.
c)
The Agency may require more frequent monitoring than
would otherwise be required by subsection
(a)
of this
Section for components which are demonstrated to have a
history of leaking.
(Source:
Amended. at
Ill.
Peg.
______,
effective
____________
Section 219.449
Reporting for Leaks
The owner or operator of
a petroleum refinery shall:
a)
Submit
a report to the Agency prior to the 1st day of
both July and September listing all leaking components

502
identified. pursuant to Section 219.447
of this Part but
not repaired. within 22 days, all leaking components
awaiting unit turnaround, the total number of
components inspected and the total number of components
found
leaking;
b)
Submit a signed statement with the report attesting
that all monitoring and repairs were performed as
required under Sections 219.445 through 219.448
of this
Part.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.450
Alternative Program for Leaks
The Agency may approve an alternative program of monitoring,
recordkeeping or reporting to that prescribed in Sections 219.446
through 219.449 of this Part upon a demonstration by the owner
or
operator of
a petroleum refinery that the alternative program
will provide refinery, Agency and USEPA personnel with an
equivalent ability to identify and repair leaking components.
Any alternative program can be allowed only if approved by the
USEPA as a SIP revision.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.452
Compliance Schedule for Leaks
The owner or operator of a petroleum refinery shall adhere to the
increments of progress contained in the following schedule:
a)
Submit to the Agency a monitoring program consistent
with Section 219.446 of this Part prior to July
1,
1991
or a date consistent with Section 219.106
of this Part.
b)
Submit to the Agency the first monitoring report
pursuant to Section 219.449
of this Part prior to
August
1,
1991 or
a date consistent with Section
219.106 of this Part.
(Source:
Amended at
Ill. Peg.
______,
-effective
____________
Section 218.453
Compliance Dates (Repeal~I
every owner or operator
of
a ~tr~1.cum refinery subject to —3-i
Ill.
Adm.
Code
215,
Subpart P as of December
31,
1987 shall have
complied with its standards and limitations by ~eccmber
31, 19&~—-

503
(Source:
Repealed at
Ill. Peg.
______,
effective
___________
SUBPART
S:
RUBBER
AND
MISCELLANEOUS PLASTIC PRODUCTS
Section 219.461
Manufacture of Pneumatic Rubber Tires
The owner or operator of an undertread cementing, treadend
cementing or
bead. dipping operaoon
at a pneumatic rubber tire
manufacturing facili-tysource shall install
and. operate:
a)
A capture system, with minimum capture efficiency of 65
percent by weight of VON for treadend cementing or bead
dipping operations and a capture system with a minimum
capture efficiency of 55.5 percent by weight of VON for
undertread cementing;
and
b)
A control device that meets the requirements
of one of
the following:
1)
A carbon adsorption system designed and operated
in a manner such that there is at least a 90
percent removal of VON by weight from the gases
ducted to the control device;
-
2)
An afterburning system that oxidizes at least 90
percent of
the captured nonmethane VON
(VON
measured as total combustible carbon)
to carbon
dioxide and water; and
3)
An alternative VON emission reduction system
demonstrated to have at least a
90 percent overall
reduction efficiency and approved by the Agency
and approved by the USEPA.
(Source:
Amended at
Ill. Peg.
______
,
effective
____________
Section 219.462
Green Tire Spraying Operations
The owner or operator of a green tire spraying operation at a
pneumatic rubber tire manufacturing 4-a-e4-~-i--tysourceshall:
a)
Install and operate:
1)
A capture system with a minimum capture efficiency
of
90 percent by weight of VON; and
2)
A control device that meets the requirements of
one of the following:

504
A)
A carbon adsorption system designed and
operated in
a manner such that there
is at
least 90 percent removal
of VON by weight
from the bascsgases ducted to the control
device;
B)
An afterburning system that oxidizes at least
90
percent
of
the
captured
nonmethane
VON
(measured as total combustible carbon)
to
carbon
dioxide
and water; or
C)
An alternative VON emission reduction system
demonstrated to have at least a 90 percent
overall
reduction
efficiency
approved
by
the
Agency and approved by the USEPA as a SIP
revision.
b)
Substitute for the normal solvent—based mold release
compound water-based sprays containing:
1)
No more than five percent by volume of VOM as
-
applied for the inside of tires;
2)
No more than ten percent by volume of VOM as
applied for the outside of tires.
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 219.463
Alternative Emission Reduction Systems
In lieu of complying with Section 219.461 or 219.462
of this
Part,
the owner or operator of an emission source may utilize an
alternative volatile organic emission reduction system,
including
an alternative production process, which
is demonstrated to be
equivalent to Section 219.461 or 219.462
of this Part on the
basis of emissions
of volatile organic me-~t-e±~
material.
A
treadend cementing operation shall be considered equivalent to
Section 219.461
or 219.462
of this Part for the purposes of this
Section if the total volatile organic emission from such
operation
is 10 grams or less per tire.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.464
-ic~cinc~and MonitoringEmission Testing
a)
Upon a reasonable request by the Agency,
the owner or
operator of
a VON ee4-es-i-ee source required to comply
with
a limit of Sections 219.461 through 219.464
~f
this Part shall conduct emissions testing,
at such
person’s own expense,
to demonstrate compliance.

505
b)
A person planning to conduct a VON emission test to
demonstrate compliance shall notify the Agency of that
intent not less than 30 days before the planned
initiation
of
the
tests
so
the
Agency
may
observe
the
test.
(Source:
Amended. at
Ill. Peg.
______,
effective
___________
Section 218.465
Compliance Dates
(Repealed)
Every owner or operator of an emission source subject to
35
Ill.
Adm. Code 215, Subpart
C,
as of December
31,
1937 shall have
complied with its standards and limitations by December
31,
1987.
(Source:
Repealed at
Ill.
Peg.
______,
effective
Section
219.466
Compliance Plan
(Repealed)
The
owner
or
operator
of
an
emission
source
shall
have
submitted to
the
Agency a compliance plan, pursuant to
35
Ill.
Adin.
Code
201,
Subpart
H,
including
a
project
~-empletionschedule where applicable,
no later than
April
21,
1983.
Unless the submitted compliance plan or schedule ~as
disapproved by the Agency, the owner or operator of
a
facility or emission source may operate the emission
e-ou-rce according to the plan and
schedule as cubmittcd.
tPhc.
r~1r~
~
-~c~hr’rTh1r-‘~h~11
~t
thr’
~cquirc~mr’rif~
r~f
111.
Adm.
Code
201,
Subpart
H,
including specific
interim dates as required in 35
Ill.
Adm, Code
201.242.
(Source:
Repealed at
Ill. Peg.
______
,
effective
__________
SUBPART T:
PHARMACEUTICAL MANUFACTURING
Section 219.480
Applicability
a)
The rules of this Subpart,
except for Sections 219.483
through 219.485, apply to all emission sourcesunits
of
VON,
including but not limited to reactors,
distillation units, dryers,
storage tanks for VOL,
equipment for the transfer of VOL,
filters,
crystallizers,
washers, laboratory hoods,
pharmaceutical coating operations, mixing operations
and centrifuges used in manufacturing,
including
packaging,
of pharmaceuticals,
and emitting more than
6.8 kg/day
(15 lbs/day)
and more than 2,268 kg/year

506
(2.5 tons/year)
of VOM.
If suchee emission sourceunit
emits less than 2,268 kg/year
(2.5 tons/year)
of VON,
the requirements
of this Subpart still apply to the
emission sourccunit
if VOM emissions from the emission
sourceunit exceed 45.4
kg/day
(100 lbs/day).
~
Notwithstanding subsection
(a), the air suspension
ooater/dryer,
fluid bed dryers,
tunnel dryers,
and
Accelacotas located
in Libertyville Township,
Lake
County,
Illinois shall be exempt from the rules
of this
6ubpart, except for Sections 219.483 through 219.485,
if emissions of VON not vented to air nollution control
pp
not exceca tnc roiiow’~~icvcio:
4-~
for the air suspension coatcr/drycr: 2,268 k~/year
(2.5 tons/year)
~
for each fluid bed dryer:
4,535
kg/year
(5.0
tons/yca-~)--
s-)--
for each tunnel
dryer:
6,803 kg/year
(7.5
t-ons/ycar);
and
4—)--
icr
cuon
Acoclacota:
6-~1~ Kn,vcar
tons/year).
ef~j
Sections 219.483
through
219.485 of this Part apply to
a plantsource having one or more emission sourccsunits
that:
1)
Are used to manufacture pharmaceuticals,
and
2)
Emit more than 6.8 kg/day
(15 lbs/day)
of VOM and
more than 2,268 kg/year
(2.5 tons/year)
of VON,
or,
if less than 2,268 kg/year
(2.5 tons/year),
these Sections still apply
if emissions from one
or more sources exceed 45.4 kg/day
(100 lbs/day).
-
~~j
No owner or operator shall violate any condition in a
permit when the condition results
in exclusion of an
emission sourceunit from this Subpart.
e.)-d) Any pharmaceutical manufacturing source that becomes
subject to the provisions
of this Subpart at any time
shall remain subject to the provisions of this Subpart
at all times.
-)-~jEmissions subject to this Subpart shall be controlled
at all times consistent with the requirements
set forth
in this Subpart.

507
~-)-~
Any
control
device required pursuant to this Subpart
shall be operated at all times when the source
it
is
controlling is operated.
~--~flj.
Determinations
of
daily
and
annual
emissions
for
purposes
of
this
Section
shall
be
made
using
both
data
on the hourly emission rate
(or the emissions per unit
of throughput)
and appropriate daily and annual data
from records of emission sourceunit operation
(or
material
throughput or material consumption data)
.
In
the absence of representative test data pursuant to
Section 219.487
of this Part for
the
hourly
emission
rate
(or the emissions per unit of throughput),
such
items shall be calculated using engineering
calculations,
including
the
methods
described
in
Appendix
B
of
“Control
of
Volatile
Organic
Emissions
from Manufacturing of
Synthesized. Pharmaceutical
Products”
(EPA—450/2-78-029),
incorporated by reference
in
Section
219.112 of this Part.
(This subsection
shall not affect the Agency’s or the USEPA’s authority
to require emission tests to be performed pursuant to
Section 219.487
of this Part.)
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section
219.481
Control
of
Reactors,
Distillation
Units,
Crystallizers, Centrifuges and Vacuum Dryers
a)
The owner or operator shall equip all reactors,
distillation units,
crystallizers,
centrifuges and
vacuum dryers that are used to manufacture
pharmaceuticals with surface condensers
or other air
pollution control equipment listed
in subsection
(b)
gf
this Section.
If
a surface condenser
is used,
it shall
be operated such that the condenser outlet gas
temperature does not exceed:
1)
248.2°K (-13°F) when condensing VON of vapor
pressure greater than 40.0 kPa
(5.8 psi)
at
294.3°K (70°F), or
2)
258.2°K (5°F)when condensing VOM of vapor
pressure greater than 20.0 kPa
(2.9 psi)
at
294.3°K (70°F), or
3)
273.2°K (32°F)when condensing VON of vapor
pressure greater than 10.0 kPa
(1.5 psi)
at
294.3°K (70°F), or

508
4)
283.2°K (50°F) when condensing VON of vapor
pressure greater than 7.0 kPa
(1.0 psi)
at 294.3°I
(70°F)
,
or
5)
298.2°K (77°?) when condensing VOM of vapor
pressure greater than 3.45 kPa (0.5 psi)
at
294.3°K (70°F).
b)
If
a scrubber,
carbon adsorber,
thermal afterburner,
catalytic afterburner,
or other air pollution control
equipment other than a surface condenser is used,
such
equipment shall provide a reduction in the emissions of
VON of 90 percent or more.
a)
The owner or operator shall enclose all centrifuges
used to manufacture pharmaceuticals and that have an
exposed VOL surface, where the VOM
in the VOL has a
vapor pressure of 3.45 kPa
(0.5 psi)
or more at 294.3°K
(70°?), except as production,
sampling, maintenance,
or
inspection procedures require operator access.
(Source:
Amended at
_____,
Ill. Peg.
______,
effective
Section 219.482
Control
of Air Dryers,
Production Equipment
Exhaust Systems and Filters
a)
The owner or operator of an air dryer or production
equipment exhaust system used to manufacture
pharmaceuticals shall control the emissions of VON from
such emissi-on &o-urccsunits by air pollution control
equipment which reduces by 90
percent or more the VON
that would. otherwise be emitted. into the atmosphere.
b)
The owner or operator shall enclose all rotary vacuum
filters and other filters used to manufacture
pharmaceuticals and that have an exposed VOL surface,
-
where the VON in the VOL has a vapor pressure of 3.45
kPa
(0.5 psi)
or more at 294.3°K (70°F), except as
production,
sampling,
maintenance,
or inspection
procedures require operator access.
(Source:
Amended at
Ill.
Peg.
______,
-effective
____________
Section
219.483
Material Storage and Transfer
The owner or operator of
a pharmaceutical manufacturing
plantsource shall:
a)
Provide
a vapor balance system that
is at least
90 percent effective in reducing VON emissions from

509
truck or railcar deliveries to storage tanks with
capacities equal
to or greater than 7.57
m3
(2,000 gal)
that store VOL with vapor pressures greater than
28.0 kPa
(4.1 psi)
at 294.3°K (70°F), and
b)
Install, operate,
and. maintain pressure/vacuum
conservation vents set at 0.2 kPa
(0.03
psi)
or greater
on all storage tanks that store VOL with vapor
pressures greater tha:~10 kPa
(1.5 psi)
at 294.3°K
(70°?)
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.485
Leaks
The owner
or operator of a pharmaceutical manufacturing
plantsource shall repair any component from which a leak of VOL
can be observed.
The repair shall be completed as soon as
practicable but no later than 15 days after the leak
is found.
If the leaking component cannot be repaired until the process
unit is shut down, the leaking component must then be repaired
before the unit
is restarted.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.486
Other Emission Sources Units
The owner or operator of a washer,
laboratory hood,
tablet
coating
operation,
mixing
operation
or
any
other
process
emission
sourceunit not subject to Sections 219.481 through 219.485 ~
this Part,
and used to manufacture pharmaceuticals
shall control
the emissions
of VON from such emission sourcesunits
by:
a)
Air pollution control equipment which reduces by
81 percent or more the VON that would otherwise be
emitted to the atmosphere,
or
b)
A surface condenser which captures all the VON which
would otherwise be emitted to the atmosphere
and. which
meets the requirements of Section 219.481(a)
of this
Part and
(b).
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.487
Testing
a)
Upon request by the Agency or the USEPA,
the owner or
operator of any VON e~-i-es-i-eesource subject to this

509
truck or railcar deliveries to storage tanks with
capacities equal to or greater than 7.57
m3
(2,000 gal)
that store VOL with vapor pressures greater than
28.0 kPa
(4.1 psi)
at 294.3°K (70°F), and
b)
Install, operate,
and maintain pressure/vacuum
conservation vents set at 0.2 kPa
(0.03 psi)
or greater
on all storage tanks that store VOL with vapor
pressures greater than
10 kPa
(1.5 psi)
at 294.3°K
(70°?)
(Source:
Amended at
Ill. Peg.
______,
effective
____________
Section 219.485
Leaks
The owner or operator of a pharmaceutical manufacturing
plantsource shall repair any component from which a leak of VOL
can be observed.
The repair shall be completed as soon as
practicable but no later than 15
days
after
the
leak
is
found.
If the leaking component cannot be repaired until the process
unit is -shut down, the leaking component must then be
repaired.
before the unit is restarted.
(Source:
Amended at
Ill.
Peg.
______,
effective
____________
Section 219.486
Other Emission Sources Units
The owner or operator of
a washer,
laboratory hood,
tablet
coating operation,
mixing operation or any other process emission
sourceunit not subject to Sections 219.481 through 219.485 Qf
this Part,
and used to manufacture pharmaceuticals
shall control
the
emissions
of
VON
from
such
emission
sourcesunits
by:
a)
Air pollution control equipment which reduces
by
81 percent or more the VON that would otherwise be
emitted. to the atmosphere,
or
b)
A surface condenser which captures all the VOM which
would otherwise be emitted to the atmosphere and which
meets the requirements of Section 219.481(a)
of this
Part and
(b).
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.487
Testing
a)
Upon request by the Agency or the USEPA, the owner or
operator of any VOM emission source subject to this

510
-
Subpart or exempt from this Subpart by virtue of the
provisions of Section 219.480 of this Part shall,
at
his own expense, demonstrate compliance to the Agency
and the USEPA by the methods or procedures
listed in
Section 219.105(f) (1) of this Part.
b)
A person planning to conduct a VON emissions test to
demonstrate compliance with this Subpart shall notify
the Agency and the USEPA of that intent not less than
30 calendar days before the planned initiation of the
test.
(Source:
Amended at
_____,
Ill.
Peg.
______,
effective
__________
Section 219.489
Recordkeeping for Air Pollution Control
Equipment
a)
The owner or operator of a pharmaceutical manufacturing
facilitysource shall maintain the following records:
1)
Parameters listed
in Section 219.488(a)
of this
Part
-(4-)- shall be recorded.
2)
For zour-c-e-semission units subject to Section
219.481
of this Part,
the vapor pressure of VON
being controlled shall be recorded for every
process.
-
b)
For any leak subject to Section 219.485 of this Part
which cannot be readily repaired within one hour after
detection,
the following records shall be kept:
1)
The name of the leaking equipment,
2)
The date and time the leak is detected,
3)
The action taken to repair the leak, and
4)
The d.atee and time the leak
is repaired.
c)
The following records shall
be kept for emission
se~-eesunits subject to Section 219.484
of this Part
which contain VOL:
1)
For maintenance and inspection:
A)
The date and time each cover
is opened,
B)
The length of time the cover remains open,
and

511
C)
The reason why the cover
is opened.
2)
For production and sampling,
detailed written
procedures or manufacturing directions specifying
the circumstances under which covers may be opened
and the procedures for opening covers.
d)
For each emission sourceunit used
in the manufacture of
pharmaceuticals for which the owner or operator of a
pharmaceutical
manufacturing
plantsource
claims
emission
standards
are
not
applicable,
because
the
emissions are below the applicability cutoffs
in
Section 219.480(a)
or 219.480(b)
of this Part,
the
owner or operator shall:
1)
Maintain a demonstration including detailed
engineering calculations of the maximum daily and
annual emissions for each such emission source
unit showing that the emissions are below the
applicability cutoffs
in Section 219.480(a)
or
219.480(b)
of this Part,
as appropriate,
for the
current
and
prior
calendar
years;
2)
Maintain appropriate operating records for each
such emission source to identify whether the
applicability
cutoffs
in
Section
219.480(a)
or
219.480(b)
of this Part,
as appropriate,
are ever
exceeded;
and
3)
Provide written notification to the Agency and the
USEPA within 30 days of
a determination that such
an emission sourceunit has exceeded the
applicability cutoffs
in Section 219.480(a)
or
219.480(b)
of this Part,
as appropriate.
e)
Records required under subsection
(a)
of this Section
shall be maintained by the owner
or operator for a
minimum of two years after the date on which they are
made.
f)
Copies of the records shall be made available to the
Agency or the USEPA upon verbal or written request.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
SUBPART
V:
AIR OXIDATION PROCESSES
Section 219.521
Definitions
(Repealed)
In addition to the~—definitionsof
35
Ill.
Adm.
Code
211,
the
following definitions apply
to this Subpart:

512
“Flow
(F)”:
Vent
stream flowrate (scm/mm)
at
a
~-tandard t~mneraturc of 20°C.
“Full Operating F1owrate”~
Maximum operating capacity
of the facility.
-“-Hourly
Emissions
(E)”:
Hourly emissions reported in
kg/hr measured at full operating flowratc.
“Net Heating Value
(H)”:
Vent stream net heating value
-(NJ/scm), where the net cnthalpy per mole
of offgas
is
based on combustion at 25°Cand 760 mm Hg,
but the
standard temperature for determining the volume
corresponding to one mole is 20°C, as
in the definition
of “F1ow.~’
11-Prooess
Vent
Stream”:
An
emission
stream
resulting
-from an air oxidation process.
“Total
Resource
Effectiveness
Index
(TRE)”:
Cost
effoctiw~nt-’~
in
11~-~-nr’r
mr~ri.~n~mof
controlling
any gaseous stream vented to the atmosphere trom
cxidation process divided by $1600/Hg,
using the
criteria and methods set forth in this Subpart and
Appendices
C
and
D.
(Source:
Repealed at
Section 219.525
Ill.
Peg.
______
,
effective
Emission Limitations for Air Oxidation
Processes
a)
No person
shall
cause
or
allow
the
emission
of
volatile
organic material
(VON)
from any process vent stream
unless the process vent stream
is vented to
a
combustion device which
is designed and. operated
either:
1)
To reduce the volatile organic emissions vented to
it with an efficiency-of at least ninety eight
percent
(98)
by weight;
or
11-Air Oxidation Process”:
any unit process including
ammoxidation
and
oxychlorination
which
uses air or—a
combination of air and oxygen as an oxidant
i-n
combination with one or more organic reactants to
produce -one or more organic compounds.
“Cost Effectiveness”:
the annual expense for
cost
c-f-
control
given
process
stream
divided
by the reduction
4~...~issionsof
.~..4cmaterial
of that stream

513
2)
To emit VON at a concentration less than twenty
parts per million by volume, dry basis.
b)
~
oxidation -f-a-eilitiesprocess vent stream for
which an existing combustion device is employed to
control process VON emissions ~ej~
not required to
meet the 98 percent emissions limit until the
combustion device is replaced for other reasons, which
shall be considered to include, but not be limited to,
normal maintenance, malfunction,
accident,
and
obsolescence.
The combustion device
is considered to
be
replaced
when:
1)
All
of the device
is replaced.;
or
2)
When the cost of the repair of the device or the
cost
of
replacement
of
part
of
the
device
exceeds
50
of the cost of replacing the entire device
with
a device which complies.
C)
The limitations of subsection
(a) above do not apply to
any process vent stream or combination of process vent
streams which has a Total Resource Effectiveness Index
(TRE)
greater than 1.0,
as determined by the following
methods:
1)
If an air oxidation process has more than one
process vent stream, TRE shall be based upon a
combination of the process vent streams.
2)
TRE of
a process vent stream shall be determined
according to the following equation:
TRE
=
E1
a
+
bF°
+
a?
+
dFH
+
e(FH)°
+
f?°-5
where:
n
=
0.88k
TRE
=
Total resource effectiveness
index--.L
F
=
Vent stream flowrate (scm/mm),
at
a standard temperature of 20°C--j
E
=
Hourly measured emissions
in
kg/hr~-;
H
=
Net heating value
of vent stream
(NJ/scm), where the net enthalpy
per mole of offgas
is based on

514
combustion at 25°Cand. 760 mm Hg,
but the standard. temperature for
determining
the
volume
corresponding to one mole
is 20°C,
as
in
the
definition
of
“FlOW”-r~
a,b,c,
d,e
and f
=
Coefficients obtained by use
of
Appendix
~
3)
For nonchlorinated process vent streams,
if the
net
heating
value,
H,
is greater than 3.6 MJ/scm,
F shall be replaced by ~!~f or purposes of
calculating
TRE.
~L
is
computed
as
follows:
=
FH
/
3.6
where F and H are as defined.
in subsection
(c) (2).
4)
The actual numerical values used in the equation
described in subsection
(C)
(2)
above shall
be
determined as follows:
A)
All reference methods and procedures
for
determining the flow,
(F), hourly emissions,
(E)
,
and
net
heating,
(H),
value
shall
be
in
accordance with Appendix
C.
B)
All coefficients described
in subsection
(c) (2)
of this Section shall be
in accordance
with Appendix
D.
(Source:
Amended at
Ill.
Peg.
______
,
effective
____________
Section 219.527
Compliance Date
(Repealed)
Each owner or operator of an emission source subject
to 35
Ill.
Adm.
Code
215,
Subpart
V,
as of December 31,
1987 shall have
1~c’ri
tjith
thr’
~tandards
and 1irnitaf~r~~
of
~
T~1
Z~
~~-_
(Source:
Repealed. at
Ill.
Reg.
______
,
effective
~-15, Subpar~
~
~y
December
31,
1007

515
SUBPART
W:
AGRICULTURE
Section 219.541
Pesticide Exception
The provisions of Sections 219.301 and 219.302
of this Part shall
not apply to the spraying or use of insecticides, herbicides
or
other pesticides.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
SUBPART
X:
CONSTRUCTION
Section 219.562
Paving Operations
The provisions of Sections 219.301 and 219.302
of this Part shall
not apply to the application of paving asphalt and pavement
marking paint from sunrise to sunset.
(Source:
Amended at
Ill. Reg.
______,
effective
___________
SUBPART
Y:
GASOLINE DISTRIBUTION
Section 219.581
Bulk Gasoline Plants
a)
Subject to S~ubsection (e)
of this Section, no person
may cause or allow the transfer of gasoline from a
delivery vessel into a stationary storage tank located
at a bulk gasoline plant unless÷~
1)
The delivery vessel and the stationary
storage tank are each equipped with a vapor
collection system that meets the requirements of
subsection
(d) (4)
of this SectionT~
2)
Each vapor collection system
is operating-~
3)
The delivery vessel displays the appropriate
sticker pursuant to the requirements of Sections
219.584
(b) or
(d)
of this Part-~
4)
The pressure relief valve(s)
on the stationary
storage tank and the delivery vessel are set to
release at no less than 0.7 psi or the highest
pressure allowed by state
or local fire codes or
the guidelines of the National Fire Prevention
AssociationT~ and
5)
The stationary storage tank
is equipped with
a
subnerged loading pipe.

516
b)
Subject to subsection
(f)
of this Section,
no person
may cause or allow the transfer of gasoline from a
stationary storage tank located at a bulk gasoline
plant into a delivery vessel unless:
1)
The requirements set forth in subsections
(a) (1)
through
(a) (4)
of this Section are metTi and
2)
Equipment is available at the bulk gasoline plant
to provide for the submerged filling of the
delivery vessel or the delivery vessel
is equipped
for bottom loading.
c)
Subject to subsection
(e)
of this Section, each owner
of
a stationary storage tank
located at a bulk gasoline
plant shall:
1)
Equip each stationary storage tank with a vapor
control system that meets the requirements of
subsection
(a)
or
(b)
of this Section, whichever
is applicable~~
2)
Provide instructions to the operator of the bulk
gasoline plant describing necessary maintenance
operations and procedures for prompt notification
of the owner
in case of any malfunction of
a vapor
control systemT~and
3)
Repair, replace or modify any worn out or
malfunctioning component or element of design.
d)
Subject to subsection
(e)
of this Section,
each
operator of
a bulk gasoline plant shall:
1)
Maintain and operate each vapor control system in
accordance with the owner’s instructionsT~
2)
Promptly notify the owner of any scheduled
maintenance
or
malfunction requiring replacement
or repair of
a
major component of
a
vapor control
system~~and
3)
Maintain gauges, meters or other specified testing
devices
in proper working orderT~
4)
Operate the bulk plant vapor collection system and
gasoline loading equipment
in a manner that
prevents:
A)
Gauge
pressure
from
exceeding
45.7
cm
(18
in.)
of water and vacuum from exceeding 15.2

517
cm
(6
in.)
of water, as measured as close as
possible to the vapor hose connectionT~and
B)
A reading equal to or greater than 100
percent of the lower explosive limit
(LEL
measured as propane) when tested
in
accordance with the procedure described
in
“Control of Volatile Organic Compound Leaks
from Gasoline Tank Trucks and Vapor
Collection Systems”,
Appendix B,
EPA 450/
2—78—051,
(incorporated by reference
in
Section 219.112
of this Part)T~and
C)
Avoidable leaks of
liquid during loading or
unloading operations.
5)
Provide
a pressure tap or equivalent on the bulk
plant vapor collection systen in order to allow
the determination of compliance with subsection
(d) (4) (A)
of this SectionT~and
6)
Within 15 business days after discovery
of any
leak by the owner, the operator, the Agency or the
USEPA, repair and retest
a vapor collection system
which exceeds the limits
of subsection
(d) (4) (A)
or
(B) of this Section.
e)
The requirements of subsections
(a),
(c) and
(d) g~f~
this Section shall not apply to:
1)
Any stationary storage tank with a capacity of
less than 2,177
1
(575
gal)-7-j or
2)
Any bulk gasoline plant whose daily gasoline
throughput
is less than 15,140
1
(4,000 gal/day)
on
a thirty-day rolling average.
f)
The requirements of subsection
(b)
shall apply only to
bulk gasoline plants whose daily gasoline throughput
is
greater than or equal
to 15,140
1
(4,000 gal/day)
on
a
thirty-day rolling average.
g)
Any bulk gasoline plant which
is ever subject to
subsections
(a)
,
(b),
(c)
,
or
(d)
of this Section shall
always be subject to these paragraphs.
(Source:
Amended at
Ill.
Reg.
______
,
effective
____________
Section 219.582
Bulk Gasoline Terminals

518
a)
No person shall cause or allow the transfer of gasoline
into any delivery vessel from any bulk gasoline
terminal unless:
1)
The bulk gasoline terminal
is equipped with
a
vapor control system that limits emission of VON
to 80 mg/l
(0.00067
lbs/gal)
of gasoline loaded;
2)
The vapor control system is operating and all
vapors displaced in the loading of gasoline to the
delivery vessel are vented only to the vapor
control system;
3)
There
is no liquid drainage from the loading
device when it
is not in use;
4)
All loading and vapor return lines are equipped
with fittings which are vapor tight; and
5)
The delivery vessel displays the appropriate
sticker pursuant to the requirements of Section
219.584(b)
or
(d)
of this Part
or,
if the
terminal
is driver-loaded, the terminal owner
or
operator shall be deemed to be in compliance with
this Section when terminal access authorization
is
limited to those owners and/or operators of
delivery vessels who have provided
a current
certification as required by Section 219.584(c) (3)
of this Part.
s-)-
Bulk gacolinc terminalo were rcquircd to take ocrt3in
octionG
to achicvc compliancc which arc 3ummarizcd
in
35
Ill. Adm.
Code
215, Appendix
C.
eb)
The operator of
a bulk gasoline terminal shall:
1)
Operate the terminal vapor collection system and
gasoline loading equipment
in a manner that
prevents:
A)
Gauge pressure from exceeding
18 inches
of
water and vacuum from exceeding
6 inches of
water as measured as close as possible to the
vapor hose connection; and
B)
A reading equal to or greater than 100
percent of the lower explosive limit
(LEL
measured as propane) when tested
in
accordance with the procedure described in
EPA 450/2-78-051 Appendix B~incorporated by
reference
in Section 219.112
of
this Part
and

519
C)
Avoidable leaks of liquid during loading or
unloading operations.
2)
Provide a pressure tap or equivalent on the
terminal vapor collection system in order to allow
the determination of compliance with Section
219.582(d) (1) (A)
of this Part
and
3)
Within
15 business days after discovery of the
leak by the owner,
operator,
or the Agency repair
and retest a vapor collection system which exceeds
the limits of subsection
(c) (1) (A)
or
(B)
of this
Section.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.583
Gasoline Dispensing Facilities
Storage Tank
Filling Operations
a)
Subject to subsection
(b)
below,
no person shall cause
or allow the transfer of gasoline from any delivery
vessel into any stationary storage tank at a gasoline
dispensing facilityoperation unless:
1)
The tank is equipped with a submerged loading
pipe;
and
2)
The vapors displaced from the storage tank during
filling are processed by a vapor control system
that includes one or more of the following:
A)
A vapor collection system that meets the
requirements
of subsection
(d) (4) below;
or
B)
A refrigeration—condensation system or any
other system approved by the Agency and
approved by the USEPA as
a SIP revision,
that
recovers at least 90 percent by weight of all
vaporized organic material from the equipment
being controlled; and
C)
The delivery vessel displays the appropriate
sticker pursuant to the requirements of
Section 219.584(b)
or
(d)
of this Part.
b)
The requirements of subsection
(a) (2)
above shall not
apply to transfers of gasoline to a stationary storage
tank at a gasoline dispensing facilityoperation
if:
I)
The tank is equipped with a floating roof,
or
other system of equal or better emission control

520
as approved by the Agency and approved by the
USEPA as
a SIP revision;
2)
The tank has a capacity of less than 2000 gallons
and was
in place and operating before January
1,
1979; or
3)
The tank has a capacity of less than 575 gallons.
c)
Subject to subsection
t)
above, each owner of a
gasoline dispensing
e~4~yoperationshall:
1)
Install all control systems and make all process
modifications required by subsection
(a) above;
2)
Provide instructions to the operator of the
gasoline dispensing facilityoperation describing
necessary maintenance operations and procedures
for prompt notification
of the owner in case of
any malfunction of a vapor control system;
and
3)
Repair,
replace or modify any worn out or
malfunctioning component or element of design.
d)
Subject to subsection
(b)
above,
each operator of a
gasoline dispensing facility operation shall:
1)
Maintain and operate each vapor control system in
accordance with the owner’s instructions;
2)
Promptly notify the owner of any scheduled
maintenance or malfunction requiring replacement
or repair of a major component of a vapor control
system;
3)
Maintain gauges,
meters or other specified testing
devices
in proper working order;
4)
Operate the vapor collection system and delivery
vessel unloading points
in a manner that prevents:
A)
A reading equal to or greater than 100
percent of the lower explosive limit
(LEL
measured as propane) when tested
in
accordance with the procedure described in
EPA 450/2-78-05? Appendix B, and
B)
Avoidable leaks of liquid during the filling
of
storage tanks;
and
5)
Within 15 business days after discovery of the
leak by the owner,
operator,
or the Agency,
repair

521
and retest a vapor collection system which exceeds
the limits of subsection
(d) (4) (A)
above.
~nr’
n1~
rrL~nc1
Tfl
£..L~LLJ~CG
were r~r~uircu
~O
LW~C
~
~~cve
compliance which are
~ummarizcd
in
35
Ill.
Adm.
Code 215.Appcndix
C.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.584
Gasoline Delivery Vessels
a)
Any delivery vessel equipped for vapor control by use
of vapor collection
equipment:
1)
Shall have a vapor space connection that
is
equipped with fittings which are vapor tight;
2)
Shall have its hatches closed at all times during
loading or unloading operations, unless a top
loading vapor recovery system
is used;
3)
Shall not internally exceed a gauge pressure of
18
inches of water or a vacuum of
6 inches of water;
4)
Shall
be designed and maintained to be vapor tight
at all times during normal operations;
5)
Shall not be refilled in Illinois at other than:
A)
A bulk gasoline terminal that complies with
the requirements of Section 219.582
of this
Part or
B)
A bulk gasoline plant that complies with the
requirements of Section 219.581(b)
of this
Part.
6)
Shall
be tested annually in accordance with Method
27,
40 CFR 60, Appendix A,
incorporated by
reference
in Section 219.105 of this Part.
Each
vessel must be repaired and retested within 15
business days after discovery of the leak by the
owner,
operator,
or the Agency, when it fails to
sustain:
A)
A pressure drop of no more than three inches
of water
in five minutes; and
B)
A vacuum drop
of
no more than three inches of
water
in five minutes.

522
b)
Any delivery vessel meeting the requirements
of
subsection
(a)
of this Section shall have a sticker
affixed to the tank adjacent to the tank manufacturer’s
data plate which contains the tester’s name,
the tank
identification number and the date of the test.
The
sticker shall be
in a form prescribed by the Agency,
and,
for those delivery vessels subject to 35
Ill.
Adrn.
Code 215 as of December
31,
1987 shall have been
displayed no later than December
31,
1987.
c)
The owner or operator of a delivery vessel shall:
1)
Maintain copies of any test required under
subsection
(a) (6)
of this Section for a period of
3 years;
2)
Provide copies of these tests to the Agency upon
request; and
3)
Provide annual test result certification to bulk
gasoline plants and terminals where the delivery
vessel
is loaded.
d)
Any delivery vessel which has undergone and passed a
test in another state which has a USEPA—approved leak
testing and certification program will satisfy the
requirements of subsection
(a)
of this Section.
Delivery vessels must display a sticker,
decal or
stencil approved by the state where tested or comply
with the requirements of subsection
(b)
of this
Section.
All such stickers, decalsor stencils shall
have been displayed no later than December 31,
1987,
for delivery vessels subject to 35 Ill. Adm.
Code 215
as of December 31,
1987.
(Source:
Amended at
Ill.
Reg.
______
,
effective
____________
Section 219.585
Gasoline Volatility Standards
a)
No person shall
sell, offer for sale,
dispense,
supply,
offer for supply,
or transport for use in Illinois
gasoline whose Reid vapor pressure exceeds the
applicable limitations set forth
in subsections
(b)
and
(c)
of this Section during the regulatory control
periods, which shall be July ~
1 to Auguot
31
September 15 for retail outlets, wholesale
purchaser—consumer facilities,
and all other
facilities.
b)
The Reid vapor pressure of gasoline,
a measure of its
volatility,
shall not exceed 9.~Qpsi
(65.562.07 kPa)

523
during the regulatory control period in 1990 and each
year thereafter.
c)
The Reid vapor pressure of ethanol blend gasolines
shall not exceed the limitations for gasoline set forth
in subsection
(b)
of this Section by more than 1.0 psi
(6.9 kPa).
Notwithstanding this limitation, blenders
of ethanol blend gasolines whose Reid vapor pressure is
less than 1.0 psi above the base stock gasoline
immediately after blending with ethanol are prohibited
from adding butane or any product that will increase
the Reid vapor pressure of the blended gasoline.
d)
All sampling of gasoline required pursuant to the
provisions of this Section shall be conducted by one or
more of the following approved methods or procedures
which are incorporated by reference in Section 215.105.
1)
For manual sampling, ASTM D4057;
2)
For automatic sampling, ASTM D4l77;
3)
Sampling procedures for Fuel Volatility,
40 CFR 80
Appendix D.
e)
The Reid vapor pressure of gasoline shall be measured
in accordance with either test method ASTM D323 or a
modification of ASTM D323 known as the “dry method”
as
set forth in 40 CFR 80, Appendix E,
incorporated by
reference in
35
Ill.
Admn.
Code ~5219.4~112
of this
Part.
For gasoline
-
oxygenate blends which contain
water—extractable oxygenates, the Reid vapor pressure
shall be measured using the dry method test.
f)
The ethanol content of ethanol blend gasOlines shall be
determined by use of one of the approved testing
methodologies specified
in 40 CFR 80, Appendix F,
incorporated by reference in 35
Ill.
Adm,
Code
-24-~2l9
.
4-G-8112 of this Part.
g)
Any alternate to the sampling or testing methods
or
procedures contained
in subsections
(d),
(e),
and
(f)
of this Section must be approved by the Agency, which
shall consider data comparing the performance of the
proposed alternative to the performance
of one or more
approved test methods or procedures.
Such data shall
accompany any request for Agency approval
of any
alternate test procedure.
If the Agency determines
that such data demonstrates that the proposed
alternative will achieve results equivalent to the
approved test methods or will achieve results

524
equivalent to the approved test methods or procedures,
the Agency shall approve the proposed alternative.
h)
Each refiner or supplier that distributes gasoline or
ethanol blends shall:
1)
During the regulatory control period,
state that
the Reid vapor pressure of all gasoline or ethanol
blends leaving the refinery or distribution
facility for use in Illinois complies with the
Reid vapor pressure limitations set forth in 35
Ill.
Admn. Code ~24~219.585(b) and
(c)
of this Part.
Any facilitysource receiving this gasoline shall
be provided with
a copy of an invoice, bill of
lading,
or other documentation used in normal
business practice stating that the Reid vapor
pressure of the gasoline complies with the State
Reid vapor pressure standard.
2)
Maintain records for a period of one year on the
Reid vapor pressure, quantity shipped and date of
delivery of any gasoline or ethanol blends leaving
the refinery or distribution facility for use in
Illinois.
The Agency shall be provided with
copies of such records
if requested.
(Source:
Amended at
Ill. Reg.
______
,
effective
____________
Section 219.586
Gasoline Dispensing Facilitic~Operations
Motor Vehicle Fueling Operations
a)
For the purposes of this sSection,
the following
definitions apply.
1)
Average M~onthly~olume÷
means tThe amount of
motor vehicle fuel dispensed per month from a
gasoline dispensing facility operation based upon
a monthly average for the 2—year period of
November,
1990 through October,
1992
or,
if not
available,
the monthly average for the most recent
twelve calendar months.
Monthly averages are to
include only those months when the facility
operation was operating.
2)
Certified÷means aAny vapor collection and control
system which has been tested and approved by CARE
as having a vapor recovery and removal efficiency
of at least 95
(by weight)
shall constitute a
certified vapor collection and control system.
CARE testing and approval
is pursuant to the CARE
manual, hereby incorporated by reference ~

525
219.112
of this Part -(California Air flesourcea
Board,
Compliance Divisien,
Compliance Assistance
Program:
Facilities Phase I ~ II
(October 1988,
rev. March
1991 CARE Manual).
This incorporation
includes no later additions
or amendments.
3)
Completion of installation÷means tThe successful
passing of one or more of the following tests
applicable to the installed vapor collection and
control system:
Dynamic Backpressure Test,
Pressure Decay/Leak Test,
and Liquid Blockage
Test~ (United States Environmental Protection
Agency,
Washington D.C.,
EPA—450/3-9l- 002b).
These tests
arc
hereby incorporated by reference
at 219.112
of this Part.
This incorporation
includes no later additions or amendments.)
4)
Constructed~means f~abricated, erected or
installed; refers to any facility,
emission source
or air pollution control equipment.
5)
CARB÷means California Air Resources Board,
P.O.
Box 2815,
Sacramento,
CA 95812.
6)
Employee÷means aAny person who performs work for
an employer.
7)
FacilityOperation÷means aAny building,
structure,
installation, operation or combination thereof
located on contiguous properties and under common
ownership that provides for the dispensing of
motor vehicle fuel.
8)
Gasoline ~dispensing
Facilityoperation÷means aAny
facility operation where motor vehicle fuel
is
dispensed into motor vehicle fuel tanks
or
portable containers from a storage tank with
a
capacity of 2176 liters
(575 gallons)
or more.
9)
Modification÷means aAny change,
removal or
addition, other than an identical replacement,
of
any component contained within the vapor
collection and control system.
10)
Motor ~vehicle~
means aAny self—propelled vehicle
powered by an internal combustion engine
including,
but not limited to, automobiles and
trucks.
Specifically excluded from this
definition are watercraft and aircraft.
11)
Motor
Zvehicle ~fuel÷
means aAny petroleum
distillate having
a Reid vapor pressure of more

526
than 27.6 kilopascals
(kPa)
(four pounds per
square
inch)
and which
is used to power motor
vehicles.
12)
Owner or ~Qperator÷
means aAny person who owns,
leases,
operates, manages, supervises or controls
(directly or indirectly)
a gasoline dispensing
facilityoperation.
13)
Reid ~apor
Ppres~ure+~Por
gasoline, 4~shall be
measured in accordance with either the method ASTM
D323 or a modification of ASTM D323 known as the
“dry method”
as set forth in
40 CFR 80, Appendix
E,
incorporated by references
in 35
Ill. Adm. Code
215.105219.112
of this Part.
14)
Vapor ?~ollection and ~ontrol
~ystem÷
means aAny
system certified by CARB which limits the
discharge to the atmosphere of motor vehicle fuel
vapors displaced during the dispensing of motor
vehicle fuel into motor vehicle fuel tanks.
b)
The provisions of subsection
(c) below shall apply to
any gasoline dispensing facilityoperation which
dispenses an average monthly volume of more than 10,000
gallons of motor vehicle fuel per month.
Compliance
shall be demonstrated
in accordance with the schedule
provided in subsection
(d)
below.
c)
No owner or operator of a gasoline dispensing facility
operation subject to the requirements
of subsection
(b)
above shall cause or allow the dispensing of motor
vehicle fuel at any time from a motor fuel dispenser
unless the dispenser is equipped with and utilizes a
vapor collection and control system which
is properly
installed and operated as provided below:
1)
Any vapor collection and control system installed,
used or maintained has been CARE certified.
2)
Any vapor collection and control system utilized
is maintained
in accordance with the
manufacturer’s specifications and the
certification.
3)
No elements or components of a vapor collection
and control system are modified,
removed, replaced
or otherwise rendered inoperative
in a manner
which prevents the system from performing in
accordance with its certification and design
specifications.

527
4)
A vapor collection and control system has no
defective, malfunctioning or missing components.
5)
Operators and employees of the gasoline dispensing
facilityoperation are trained and instructed
in
the proper operation and maintenance of
a vapor
collection and control system.
6)
Instructions are posted
in a conspicuous and
visible place within the motor fuel dispensing
area and describe the proper method of dispensing
motor vehicle fuel with the use of the vapor
collection and control system.
d)
In conjunction with the compliance provisions of
Section 219.105 of this Part,
faciliticsgperations
subject to the requirements of subsection
(c) above
shall demonstrate compliance according to the
following:
1)
FaciliticoOperations that commenced construction
after November
1,
1990,
must comply by May
1,
1993.
IBOARD NOTE:
The Board adopted an emergency rule
in R93-l2,
extending the compliance date in
Section 219.586(d) (1)from May
1,
1993 to October
15,
1993.
This emergency rule became effective on
May 24,
1993 and will expire on October
21,
1993.)
2)
FacilitiesOperations
that commenced construction
before November
1,
1990,
and dispense an ave~~age
monthly volume of more than 100,000 gallons of
motor fuel per month must comply by November
1,
1993.
3)
FaciliticcOperations
that commenced construction
before November
1,
1990,
and dispense an average
monthly volume of less than 100,000 gallons
of
motor fuel per month must comply by November
1,
1994.
4)
New faciliticcoperations constructed after the
adoption of this Section shall comply with the
requirements of subsection
(c) above upon startup
of the facilityoperation.
5)
Existing facilitiesoperations previously exempted
from but which become subject to the requirements
of subsection
(c) above after May
1,
1993
shall
comply with the requirements
of subsection
(c)

528
above within six calendar months of the date from
which the facilityoperation becomes subject.
e)
Any gasoline dispensing facility~perationthat becomes
subject to the provisions of subsection
(c) above at
any time shall remain subject to the provisions of
subsection
(c)
above at all times.
f)
Upon request by the A’iency, the owner or operator of a
gasoline dispensing 4e4~4~yoperationwhich claims to
be exempt from the requirements of this
Section
shall
submit records to the Agency within 30 calendar days
from the date of the request which demonstrate that the
gasoline dispensing facilityoperation
is
in fact
exempt.
g)
Recordkeeping and reporting:
1)
Any gasoline dispensing facilityoperation subject
to subsection
(c) above shall retain at the
f-acilityoperation copies of the registration
information required at subsection
(h) below.
2)
Records and reports required pursuant to this
subsection shall be made available to the Agency
upon request.
Records and reports which shall be
maintained by the owner or operator of the
gasoline dispensing facility operation shall
clearly demonstrate:
A)
That a certified vapor collection and control
system has been installed and tested to
verify its performance according to its
specifications.
B)
That proper maintenance has been conducted in
accordance with the manufacturer’s
specifications and requirements.
C)
The
time period and duration of all
malfunctions
of the vapor collection and
control system.
D)
The motor vehicle fuel throughput of the
-f--acilityoperation for each calendar month of
the previous
year.
E)
That operators and employees are trained and
instructed in the proper operation and
maintenance of the vapor collection and
control system and informed as to the

529
potential penalties associated with the
violation of any provision of this Section.
h)
Any gasoline dispensing #ae~4~yoperationsubject to
subsection
(c) above shall be exempt from the permit
requirements specified under 35
Ill. Adm. Code 201.142,
201.143 and 201.144 for its vapor collection and
control systems, provided that:
1)
Upon the installation of
a vapor collection and
control system,
the owner or operator of the
gasoline dispensing facilityoperation submits to
the Agency a registration which provides at
minimum the facilityoperation name and address,
signature of the owner or operator,
the CARE
Executive Order Number for the vapor collection
and control system to be utilized, the number of
nozzles
(excluding diesel or kerosene)
used for
motor vehicle refueling,
the monthly average
volume of motor vehicle fuel dispensed,
the
location
(including contact person’s name,
address, and telephone number)
of records and
reports required by this Section,
and the date of
completion of installation of the vapor collection
and control system.
2)
The registration
is submitted to the Agency within
30 days of completion of such installation.
3)
A copy of the registration information
is
maintained at the gasoline dispensing
#ae-i-~yoperation.
4)
Upon the~modification of an existing vapor
collection and control system, the owner or
operator of the gasoline dispensing facility
operation submits to the Agency a registration
that details the changes to the information
provided
in the previous registration of the vapor
collection and control system and which includes
the signature of the owner or operator.
The
registration must be submitted to the Agency
within 30 days of completion of such modification.
(Source:
Amended at
Ill. Reg.
________,
effective October
21,
1993

530
SUBPART
Z:
DRY CLEANERS
Section 219.601
Perchioroethylene Dry Cleaners
The owner or operator of a dry cleaning fpcility operation which
uses perchioroethylene shall:
a)
Vent the entire dryer exhaust through a properly
designed and functioning carbon adsorption system or
equally effective control device; and
b)
Emit no more than 100 ppmv of VOM from the dryer
control device before dilution,
or achieve
a
90 percent
average reduction before dilution;
and
c)
Immediately repair all components found to be leaking
liquid VOM; and
d)
Cook or treat all diatomaceous earth filters
so that
the residue contains 25 kg
(55
lb)
or less of volatile
organic material per 100 kg
(220 lb)
of wet waste
material;
and
e)
Reduce the vVOM from all solvent stills to
60 kg
(132
lb)
or less per 100 kg
(220
lb)
of wet waste material;
and
f)
Drain all filtration cartridges
in the filter housing
or other sealed container for at least 24 hours before
discarding the cartridges; and
g)
Dry all drained filtration cartridges
in equipment
connected to an emission reduction system or
in a
manner that will eliminate emission of volatile organic
material to the atmosphere.
(Source:
Amended at
Ill.
Peg.
______,
effective
_____________
Section 219.602
Exemptions
The provisions of Section 219.601 are not applicable to
perchioroethylene dry cleaning operations which are coin—operated
or to dry cleaning facilitic~operations consuming less than
30
gal per month
(360 gal per year)
of perchloroethylene.
(Source:
Amended at
Ill. Peg.
______,
effective
____________

531
Section 219.603
Leaks
The presence of leaks shall be determined for purposes of Section
219.601(c)
of this Part by
a visual inspection of the following:
hose connections, unions,
couplings and valves; machine door
gaskets and seatings;
filter head gasket and seating; pumps; base
tanks and storage containers; water separators;
filter sludge
recovery;
distillation unit; diverter valves; saturated lint from
lint baskets;
and cartridge filters.
(Source:
Amended at
______________________
)
Ill.
Reg.
______,
effective
Section 219.604
Compliance Dates
(Repealed)
Every owner or operator
of an emission source previously subject
to 35
Ill,
Adm.
Code 215,
Subpart
Z,
shall have complied with
i-t-s
standards and limitations
in accordance with the applicable dates
set forth
in
35
Ill. Adm.
Code 215.604.
(Source:
Repealed
at
Ill. Reg.
effective
Section 219.605
Compliance Plan
(Repealed)
e-)--
The owner or operator of an emission source subject to
this Subpart shall have submitted to the Agency
a
ee~plianccplan, pursuant to 35 Ill. Adm.
Code
201,
?-u-bpart H,
including a project completion schedule
where applicable,
no later than,
for Section
2l9.601(-a-)-
and
(b), April 21,
1983.
è
Unless the submitted compliance plan or schedule was
disapproved
by
the
Agency,
the
owner
or
operator
of
a
facility
or emission source may operate the
emission
source according to the plan and schedule as submitted.
e
The plan and schedule shall meet the requirements of
35
Ill.
Adm.
Code
201,
Subpart
H,
including specific
interim dates as required in
35
Ill.
Adm.
Code 201.242.
(Source:
Repealed at
Ill.
Reg.
effective
Section 219.606
Exception to Compliance Plan
(Repealed)
Coin-operated
dry
cleaning
operations
and
dry
cleaning
facilities
1
-~
~onsumi~~
~.
than 30 gal per month
(360
~
~
perchloroethylcnc arc not
required to submit or obtain an Agency
approved compliance plan or project completion schedule.

532
(Source:
Repealed at
Ill. Reg.
______,
effective
___________
_____________________)
Section 219.608
Operating Practices for Petroleum Solvent Dry
Cleaners
In order to minimize fugitive solvent emissions, the owner or
operator of a petroleum solvent
dry
cleaning.#a4Mtysource shall
employ good housekeeping practices including the following:
a)
General Housekeeping Requirements
1)
Equipment containing solvent (washers, dryers,
extractors and filters) shall remain closed at all
times except during load transfer and maintenance.
Lint filter and button trap covers shall remain
closed except when solvent-laden material is being
removed.
2)
Cans, buckets, barrels and other containers of
solvent or of solvent—laden material shall be
covered except when in use.
3)
Solvent—laden material shall be exposed to the
atmosphere only for the minimum tinS necessary for
load transfer.
b)
.
Installation and operation of equipment:
1)
All cartridge filters shall be enclosed and
operated
in
accordance
with
the
procedures
and
specifications
recommended
by
the
manufacturer
for
the cartridge filter.
After installation, the
cartridges shall be inspected, monitored and
maintained in accordance with the manufacturer’s
recommendations; and
2)
Vents on containers for new solvent and for
solvent-containing waste shall be constructed and
maintained so as to minimize solvent vapor
emissions.
Criteria for the minimization of
solvent vapor emissions include the elimination of
solvent buckets and barrels standing open to the
atmosphere, and the repair of gaskets and seals
that expose solvent—rich environments to the
atmosphere, to be determined through visual
inspection.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_____)
Section 219.609
Program for Inspection and Repair of
Leaks

533
a)
The owner or operator of a petroleum solvent dry
cleaning facilitysource shall conduct the following
visual inspections on a weekly basis:
1)
Washers, dryers,
solvent filters, settling tanks,
vacuum stills and containers and conveyors of
petroleum solvent shall be inspected for visible
leaks of solvent liquid.
2)
Pipes, hoses and fittings shall be inspected for
active dripping or dampness.
3)
Pumps and filters shall be inspected for leaks
around seals and access covers.
4)
Gaskets and seals shall be inspected for wear and
defects.
b)
Leaks of petroleum solvent liquid and vapors shall be
repaired within three working days of detection,
unless
necessary replacement parts are not on site.
1)
If necessary,
repair parts shall be ordered within
three working days of detection of the leak.
2)
The leak shall be repaired within three days of
delivery of necessary parts.
(Source:
Amended at
Ill.
Req.
______,
effective
____________
Section 219.610
Testing and Monitoring
a)
Compliance with Sections 219.607(b) (2),
219.608 and
219.609
of this Part shall
be determined by visual
inspection; and
b)
Compliance with Sections 219.607(a) (2) and
(b)(l)
ç~f
this Part shall be determined by methods described
in
EPA—450/3-82-009
(1982) incorporated by reference in
Section 219.112
of this Part.
c)
If a control device
is used to comply with Section
219.607 (a) (1)
of this Part, then compliance shall be
determined using 40 CFR 60 Appendix
A, Method
25
(1984)
incorporated by reference
in Section 219.112
of this
Part.
(Source:
Amended at
Ill. Req.
______
,
effective
____________
Section 219.611
Exemption for Petroleum Solvent Dry Cleaners

534
The provisions
of Sections 219.607 through 219.610 of this Part
shall not apply to petroleum solvent dry cleaning faci1itie~
sources whose emissions of volatile organic material do not
exceed 91 Mg
(100 tons)
per year
in the absence of pollution
control equipment or whose emissions of VON,
as limited by the
operating permit, will not exceed 91 Mg
(100 tons)
per year
in
the absence of pollution control equipment.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.612
Compliance Dates
(Repealed)
~
a~
~
~
ssion sources subject to
35
Ill.
Adm.
Code 215.607 through 215.60~as
of December
31,
1987 shall have
complied with the requirements set forth therein
no later than
December
31,
1087.
(Source:
Repealed at
Ill.
Reg.
______
,
effective
___________
Section 219.613
Compliance Plan
(Repealed)
&)-
The owner or operator of an emission source formerly
subject to
35 Ill.
Adm.
Code 215.610(a)
as of May
31,
1987 shall have submitted to the Agency
a compliance
plan,
including
a project completion schedule where
applicable,
no later than
M~v
~
-
h-)-
The plan and schedule shall meet the requirements
of
35
Ill. Adm.
Code 201.
(Source:
Repealed at
Ill.
Reg.
______
,
effective
___________
SUBPART AA:
PAINT AND INK MANUFACTURING
Section 219.620
Applicability
a)
This s~ubpartshall apply to all paint and ink
manufacturing plantssources which:
1)
Include process emission sourcesunits not subject
to Subparts
B,
E,
F
(excluding Section 219.204(1)
of this Part),
H (excluding Section 219.405
g~f.
this Part),
Q,
R,
5,
T (excluding Section 219.486
of this Part),
V,
X,
Y~
e-~Z
or BE of this Part;
and which as
a group
both:
A)
~Have
maximum theoretical emissions
of
91 Mg
(100 tons)
or more per calendar year of VON

535
if no air pollution control equipment were
used,
and
B)
a~renot limited to less than 91 Mg
(100
tons)
of VON emissions per calendar year
in
the absence of air pollution control
equipment, through production or capacity
limitations contained
in a federally
enforceable construction permit or a SIP
revision,
or
2)
Produce more than 7,570,820 1(2,000,000 gal)
per
calendar year of paint or ink formulations, which
contain less than 10 percent
(by weight)
water,
and ink formulations not containing as the primary
solvents water, Magie oil or glycol.
b)
For the purposes of this Subpart, uncontrolled VON
emissions are the emissions
of VON which would result
if no air pollution control equipment were used.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.621
Exemption for Waterbase Material and
Heatset-Offset Ink
The requirements of Sections 219.624 and 219.625 and Section
219.628(a)
of this Part shall not apply to equipment while
it
is
being used to produce either:
a)
p~aintor ink formulations which contain
10 percent or
more
(by weight)
water,
or
b)
.~Inkscontaining Magie oil and glycol as the primary
solvent.
(Source:
Amended at
Ill.
Req.
______
,
effective
____________
Section 219.623
Permit Conditions
No person shall violate any condition
in a permit when the
condition results
in exclusion of the p-1-a~sourceor an emission
sourceunit from this Subpart.
(Source:
Amended at
Ill.
Req.
______,
effective
______
Section 219.624
Open—~TopMills,
Tanks, Vats or Vessels

536
No person shall operate an open-top mill,
tank,
vat or vessel
with a volume of more than
45
1
(12 gal)
for the production
of
paint or ink unless:
a)
The mill,
tank, vat or vessel
is equipped with a cover
which completely covers the mill,
tank,
vat or vessel
opening except for an opening no larger than necessary
to allow for safe clearance for a mixer shaft.
Such
cover shall extend at least
1.27 cm
(0.5
in.)
beyond
the outer rim of the opening or be attached to the rim.
b)
The cover remains closed except when production,
sampling,
maintenance or inspection procedures require
access.
c)
The cover is maintained
in good condition such that,
when
in place,
it maintains contact with the rim of the
opening for at least
90 percent of the circumference of
the rim.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.628
Leaks
The owner or operator of
a paint or ink manufacturing plantsource
shall,
for the purpose of detecting leaks, conduct an equipment
monitoring program as set forth below:
a)
Each pump shall
be checked by visual inspection each
calendar week for indications of leaks,
that is,
liquids dripping from the pump seal.
If there are
indications of
liquids dripping from the pump seal,
the
pump shall
be repaired as soon as practicable,
but no
later than 15 calendar days after the leak
is detected.
b)
Any pump,
valve, pressure relief valve, sampling
connection,
open-ended valve and flange or connector
containing a fluid which
is at least 10 percent VON by
weight which appears to be leaking on the basis of
sight,
smell
or sound shall be repaired as soon as
practicable,
but no later than
15 calendar days after
the leak is detected.
c)
A weather proof, readily visible tag,
in bright colors
such as red or yellow,
bearing an identification number
and the date on which the leak was detected shall be
attached to leaking equipment.
The tag may be removed
upon repair,
that
is, when the equipment
is adjusted or
otherwise altered to allow operation without leaking.

537
d)
When a leak is detected,
the owner or operator shall
record the date of detection and repair and the record
shall be retained at the plantsource for at least two
years from the date of each detection or each repair
attempt.
The record shall be made available to any
person upon verbal or written request during business
hours.
(Source:
Amended at
Ill. Reg.
______
,
effective
____________
Section 219.636
Compliance Schedule
Every owner or operator of an emission source subject to the
control
requirements of this Subpart shall comply with the
requirements thereof on and after a date consistent with Section
219.106
of this Part.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.637
Recordkeeping and Reporting
a)
Upon request by the Agency,
the owner or operator of an
emission source which claims to be exempt from the
requirements of this Subpart shall submit records to
the Agency within
30 calendar days from the date of the
request which document that the emission source
is
in fact exempt from this Subpart.
These records
shall
include
(but are not limited to) the percent
water
(by weight)
in the paint
or ink being produced
and the quantity of Magie oil, glycol
and other
solvents in the ink being produced.
b)
Every owner or operator of an emission source which
is
subject to the requirements of this Subpart shall
maintain all records necessary to demonstrate
compliance with those requirements at the
facilitysource for three years.
(Source:
Amended at
Ill.
Reg.
______
,
effective
____________
SUBPART EB:
POLYSTYRENE PLANTS
Section 219.875219.640
Applicability of Subpart B~B
The provisions of this Subpart shall apply to polystyrene plants:
a)
Which use continuous processes to manufacture
polystyrene
-
polybutadiene co-polymer;
and

538
b)
Which fall within Standard Industrial Classification
Group No.
282,
Industry No.
2821,
except that the
manufacture of polystyrene resins need not be the
primary manufacturing process at the plant.
(Source:
Renumbered from Section 219.875 and amended at
____
Ill.
Reg.
_____
,
effective
______________________)
Section
2-l-9-.8-7-3-219.642
Emissior~Limitation at Polystyrene
Plants
No person shall cause or allow the emissions of VOM from the
material recovery section to exceed 0.12 kg of VON per 1000 kg of
polystyrene resin produced.
(Source:
Renumbered from Section 219.877
at
Ill. Reg.
effective ____________________________
Section -24-9--8-&62l9.644
Emissions Testing
a)
Upon
a reasonable request by the Agency,
the owner
or
operator of a polystyrene plant subject to this Subpart
shall at his own expense demonstrate compliance by use
of the following method:
40 CFR 60, Appendix A, Method
25
Determination of Total Gaseous Non-Methane Organic
Emissions as Carbon
(1984),
incorporated by reference
in Section 219.112
of this Part.
b)
A person planning to conduct
a VOM emissions test to
demonstrate compliance with this Subpart shall notify
the Agency of that intent not less than 30 days before
the planned initiation of the tests
so the Agency may
observe the test.
(Source:
Renumbered from Section 219.886 and amended at
____
Ill. Req.
_____,
effective _______________________
Section 219.875
Applicability of Subpart BE
(Renumbered)
(Source:
Renumbered to Section 219.640 at
____
Ill.
Req.
effective
_______________)
Section 219.877
Emissions Limitation at Polystyrene Plants
(Renumbered)
(Source:
Renumbered to Section 219.642
at
Ill. Reg.
effective
_______________________________)

Section 219.879
539
Compliance Date
(Repealed)
Every
owner
and
operator
of
an
emission
source
subject
to
35
Ill.
Adm.
Code
215,
Subpart
BE,
as
of
December
31,
1987,
shall
have
complied
with
its
standards
and
limitations
by
December
31,
1987.
(Source:
Repealed
at
Ill.
Reg.
______,
effective
___________
Section 219.881
Compliance
Plan
(Repealed)
subject to the requirements
of
35 Ill.
Adm. Cod~
~ubpart
BE shall have submitted to the Agency
a
~omp1iance
plan in accordance with
35
Ill.
Adm.
201,
Subpar~-
“-i-
~Eluding
proj~
omple~
-~
LLl~
(1
(~_
I
Ciii
~(~Ilf~(1Ll
I
i~
on
or
~c~orc
vccembcr
~,
~
Unless
the
submitted
compliance
plan
or
schedule
was
disapproved
by
the
Agency,
the
owner
or
operator
of
a
facility
or
emission
source
subject
to
this
Subpart
may
operate the emission source according to the plan and
schedule as submitted.
The plan and schedule shall meet the requirements
of 35
Ill.
Adm.
Code 201,
Subpart H and Section 219.883.
______
effective
Special
Requirements
for
Compliance
Plan
(Repealed)
For
sources
subject
to
this
Subpart,
an
approvable
compliance
plan
shall
include:
~a-)~
A
description
of
each
process
which
is
subject
to
an
emissions
limitation
~-~-
Quantification
of
the
emissions
from
each
process;
A
description
of
the
procedures
and
methods
used--t-e
determine
the
emissions
of
VON
~-
A
description
of
the
methods
which
will
be
used
to
demonstrate
compliance
with
the
allowable
plantwidc
emission
limitation
(Section
215.877),
including
a
method
of
inventory,
rccordkeeping
and
emission
calculation or measurement.
(Source:
Repealed at
Ill.
Reg.
______
,
effective
________
-
Code
(Source:
Repealed at
Ill.
Reg
Section 219.883

540
Section 219.886
Emissions Testing
(Renumbered)
(Source:
Renumbered to Section 219.644
at
____
Ill.
Req.
effective _____________________________
SUBPART PP:
MISCELLANEOUS FABRICATED PRODUCT
MANUFACTURING PROCESSES
Section 219.920
Applicability
a)
The
requirements
of
this
Subpart
shall
apply
to
a
plant’ssource’s miscellaneous fabricated product
manufacturing process emission sourcesunits which are
not included within any of the source categories
specified in Subparts
B,
E,
F,
H,
Q,
R,
S, ~
V,
X, Y~
e~Z
or BE if the plantsource is subject to this
Subpart.
A plantsource
is subject to this Subpart
if
it contains process emission sources units,
not
regulated by Subparts
B,
E,
F
(excluding Section
219.204(1)
of this Part), H
(excluding Section 219.405
of this Part),
Q,
R,
5,
T,
(excluding Section 219.486
of this Part),
V,
X, Y~e±~
Z
or BE of this Part; which
as a group both:
1)
Mlave maximum theoretical emissions of 91 Mg
(100
tons)
or more per calendar year of VOM if no air
pollution control equipment were used,
and
2)
a~renot limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment, through
production or capacity limitations contained in
a
federally enforceable construction permit or a SII
revision.
b)
If a plantsource ceases to fulfill the criteria of
subsection
(a)
above, the requirements of this Subpart
shall continue to apply to a miscellaneous fabricated
products manufacturing process emission sourccunit
which was ever subject to the control requirements
of
Section 219.926 of this Part.
c)
No
limits
under
this
Subpart
shall
apply
to
emission
sourcesunits
with
emissions
of
VOM
to
the
atmosphere
less
than
or
equal
to
0.91
Mg
(1.0
ton)
per
calendar
year if the total emissions from such sources emission
units not complying with Section 219.926
of this Part
does not exceed 4.5/Mg
(5.0 tons)
per calendar year.
d)
For the purposes of this Subpart,
an emission
s-e~eeunitshall be considered regulated by a Subpart
if
it
is subject to the limits of that Subpart.
An

541
emission sourccunit
is not considered regulated by
a
Subpart
if
it is not subject
to the limits of that
Subpart,
e.g., the emission unit
is covered by an
exemption in the Subpart
or the applicability criteria
of the Subpart are not met.
its emissions arc below
the applicability cutoff
level
or
if
the
source
is
covered
by—an
exemption.
e)
For the purposes of this Subpart, uncontrolled VON
emissions are the emissions
of VOM which would result
if no air pollution control equipment were used.
~j.
The control reguirments in Subrart PP shall not apply
to
sewage treatment plants; vegetable oil extractign
and processing; coke ovens
(including by—product
recovery plants)
;
fuel combustion units; bakeries;
barge loading facilities;
iet engine test cells;
production of polystyrene foam insulation board
including storage and extrusion of scrap where blowing
agent
is added to the polystyrene resin at the source,
but not including blending and preliminary expansion of
resin prior to molding where blowing agent
is
incorporated into the polystyrene resin by the producer
of the resin; production of polystyrene foam packaging
not including blending and preliminary expansion of
resin prior to molding where blowing agent
is
incorporated into the polystyrene resin by the producer
of the resin and not including storage and extrusion of
scrap where blowing agent
is added to the polystyrene
resin at the source; and iron and steel production.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.923
Permit Conditions
No person shall violate any condition
in
a permit when the
condition results
in exclusion of the p-1-antsource or an emission
sourceunit from this Subpart~
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.926
Control Requirements
Every owner or operator of an emission sourcemiscellaneous
fabricated product manufacturing process emission unit subject to
this Subpart shall comply with the requirements of subsection
(a)
,
(b)
or
(c)
of this Section:

542
a)
Emission capture and control techniques which achieve
an
overall
reduction
in
uncontrolled
VOM
emissions
of
at least
81
percent
from
each
emission
unit,
or
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at a source of
a
type that by itself
is subiect to control requirements
in other Subparts of thisPart
or 40 CFR 60,
incorporated bY reference in Section 219.112,
e.g.,
a
coating
line,
a printing line,
a process unit,
a
wastewater system,
or other equipment.
or
is otherwise
any part or activity at a source.)
b)
For coating lines, the daily-weighted average VON
content shall not exceed 0.42 kg VOM/1
(3.5
lbs
VON/gal)
of coating as applied
(minus water and any
compounds which are specifically exempted from the
definition of VON)
during any day.
Owners and
operators complying with this Section are not required
to comply with Section 219.301 of this Part,
or
c)
An alternative control plan which has been approved by
the Agency and app~-e~ed--bythe USEPA in a federally
enforceable permit or as a SIP revision.
(Source:
Amended at
Ill.
Req.
______,
effective
_____________
Section 219.927
Compliance Schedule
Every owner or operator of an emission sour-e-eunit subject to the
control requirements of this Subpart shall comply with the
requirements thereof on and after a date consistent with Section
219.106 of this Part.
(Source:
Amended at
Ill. Req.
,
effective
_____________
Section 219.928
Testing
a)
When in the opinion of the Agency it is necessary to
conduct testing to demonstrate compliance with Section
219.926 of this Part,
the owner or operator of a VON
emission sourceunit subject to the requirements of this
Subpart shall,
at his own expense, conduct such tests
in accordance with the applicable test methods and
procedures specified in Section 219.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act,
as amended,
to
require testing.

543
(Source:
Amended at
Ill. Req.
______
,
effective
_____________
SUBPART QQ:
MISCELLANEOUS FORMULATION MANUFACTURING PROCESSES
Section 219.940
Applicability
a)
The requirements of this Subpart shall apply to a
pp~Lssourcels miscellaneous formulation manufacturing
process emission sourcesunits, which are not included
within any of the source categories specified in
Subparts
B,
E,
F,
H,
Q,
R,
5, ~
V,
X, Y~
e~
Z or BE of
this Part
if the p-1-antsource is subject to this
Subpart.
A plantsource is subject to this Subpart
if
it contains process emission sourcesunits, not
regulated
by
Subparts
B,
E,
F (excluding Section
219.204(1)
of
this
Part),
H (excluding Section 219.405
of
this
Part),
Q,
R,
5,
T
(excluding
Section
219.486
of
this
Part),
V,
X,
Y~
e~
Z
or
BB
of
this
Part;
which
as
a
group
both:
1)
~j~ave
maximum
theoretical
emissions
of
91
Mg
(100
tons)
or
more
per calendar year of VON if
no
air
pollution control equipment were used,
and
2)
a~renot limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment, through
production or capacity limitations contained
in a
federally enforceable construction permit or a SIP
revision.
b)
If a plantsource ceases to fulfill the criteria of
subsection
(a)
of this Section,
the requirements of
this Subpart shall continue to apply to a miscellaneous
formulation manufacturing process emission source unit
which was ever subject to the control requirements
of
Section 219.946 of this Part.
c)
No limits under this Subpart shall apply to emission
s-e~eesunitswith emissions of VOM to the atmosphere
less than or equal to 2.3 Mg
(2.5 tons)
per calendar
year if the total emissions from such sources emission
units not complying with this Section does not exceed
4.5 Mg
(5.0 tons) per calendar year.
d)
For the purposes of this Subpart, an emi~sion
sourceunit shall
be considered regulated by a Subpart
if it
is subject to the limits
of that Subpart.
An
emission sourceunit
is not considered regulated by
a
Subpart if
it
is not subject to the limits of that
Subpart,
e.g.,
the emission unit
is covered
by an

544
exemption in the Subpart
or the applicability criteria
of the Subpart are not met.
its emissions are below the
applicability cutoff level
or if the source
is covered
-by
an i~vc’mr~tion.
e)
For the purposes of this Subpart, uncontrolled VON
emissions are the emissions of VOM which would result
if no air pollution control equipment were used.
~j
The control requiremen:s
in Subpart 00 shall not apply
to sewage treatment plants; vegetable oil extraction
and processing;
coke ovens
(including by—product
recovery plants);
fuel combustion units; bakeries;
barge loading facilities;
jet engine test cells;
production of polystyrene foam insulation board
including storage and extrusion of scrap where blowing
agent
is added to the polystyrene resin at the source,
but not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin; production of polystyrene foam packaging
not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin and not including storage and extrusion of
scrap where blowing agent is added to the polystyrene
resin at the source; and iron and steel production.
(Source:
Amended at
Ill. Req.
______,
effective
____________
Section 219.943
Permit Conditions
No person shall violate any condition in a permit when the
condition results in exclusion of the plantsource or an emission
sourc-cunit from this Subpart.
(Source:
Amended at
Ill.
Req.
______
,
effective
__________
Section 219.946
Control Requirements
Every owner or operator of an emission sourcea miscellaneous
formulation manufacturing process emission unit subject to this
Subpart shall comply with the requirements of subsection
(a)
or
(b)
below.
a)
Emission capture and control techniques which achieve
an overall reduction in uncontrolled VON emissions of
at least 81 percent from each emission unit,
or

545
(Board Note:
For the purpose of this provision,
an
emission unit is any part or activity at
a source of
a
type that by itself
is subject to control requirements
in other Subparts
of this Part or 40 CFR 60,
incorporated by reference in Section 219.112,
e.g.,
a
coating line,
a printing line,
a process
unit,
a
-
wastewater
system,
or other eguipment,
or
is otherwise
any part or activity at a source,)
b)
An alternative control plan which has been approved by
the Agency and ~-pprovcd by the USEPA in a federally
enforceable permit or as a SIP revision.
(Source:
Amended at
Ill.
Req.
______,
effective
____________
Section 219.947
Compliance Schedule
Every owner or operator of an emission courceunit subject to the
control requirements of this Subpart shall comply with the
requirements thereof on and after a date consistent with Section
219.106 -of this Part.
(Source:
Amended at
Ill. Req.
______,
effective
____________
Section 219.948
Testing
a)
When in the opinion of the Agency
it
is necessary to
conduct testing to demonstrate compliance with Section
219.946 of-this Part,
the owner or operator of a VON
emission seurceunit subject to the requirements of this
Subpart shall,
at his own expense, conduct such tests
in accordance with the applicable test methods and
procedures specified in Section 219.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act, as amended, to
require testing.
(Source:
Amended at
Ill.
Req.
______,
effective
____________
SUBPART RR:
MISCELLANEOUS ORGANIC CHEMICAL
MANUFACTURING PROCESSES
Section 219.960
Applicability
a)
The requirements of this Subpart shall apply to a
plant’ssource’s miscellaneous organic chemical
manufacturing process emission sourcesunits which are

546
not included within any of the source categories
specified in Subparts
B,
E,
F,
H,
Q,
R,
5, ~
V,
X, Y~
e±~
Z
or
BE
of
this
Part,
if
the
plantsource
is
subject
to
this Subpart.
A p-1-an-t~source is subject to this
Subpart
if
it
contains
process
emission
sourcesunits,
not regulated by Subparts
B,
E,
F (excluding Section
219.204(1)
of this Part), H
(excluding Section 219.405
of this Part),
Q,
R,
5, ~
(excluding Section 219.486
of
this Part)
V,
X, Y~er
Z or BE of this Part; which as
a
group both:
1)
èl~avemaximum theoretical emissions of 91 Mg
(100
tons)
or more per calendar year of VON if no air
pollution control equipment were used,
and
2)
&~renot limited to less than 91 Mg
(100 tons)
of
VON emissions per calendar year in the absence of
air pollution control equipment,
through
production or capacity limitations contained
in a
federally enforceable construction permit or a SIP
revision.
b)
If a plantsource ceases to fulfill the criteria of
Subsection
(a)
of this Section, the requirements of
this Subpart shall continue to apply to a miscellaneous
organic chemical manufacturing process emission source
unit which was ever subject to the control requirements
of Section 219.966 of this-Part.
c)
No limits under this Subpart shall apply to emission
sourcesunits with emissions of VON to the atmosphere
less than or equal to 0.91 Mg
(1.0
ton)
per calendar
year
if the total emissions from such sour-c-es emission
units not complying with Section 219.966 of this Part
does not exceed 4.5 Mg
(5.0 tons)
per calendar year.
d)
For the purposes of this Subpart, an emission se~ee
unit shall be considered regulated by a Subpart
if
it
is subject to the limits of that Subpart.
An emission
sourceunit
is not considered regulated by a Subpart if
it
is not subject to the limits of that Subpart,
e.g.,
the emission unit is covered by an exemption in the
Subpart or the applicability-criteria
of the Subpart
are not met.
-its emissions arc below the applicability
cutoff level
or if the source is covered by an
exemption.
e)
For the purposes of this Subpart, uncontrolled VON
emissions are the emissions of VON which would result
if no air pollution control equipment were used.

547
Q
The control requirements
in Subpart RR shall not apply
to sewage treatment plants; vegetable oil extraction
and processing;
coke ovens
(including by—product
recovery plants);
fuel combustion units; bakeries;
barge loading facilities; let engine test cells;
production
of polystyrene foam insulation board
including storage and extrusion of scrap where blowing
agent is added to the polystyrene resin at the source,
but not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin; production of polystyrene foam packaging
not including blending and preliminary expansion of
resin prior to molding where blowing agent is
incorporated into the polystyrene resin by the producer
of the resin and not including storage and extrusion of
scrap where blowing agent is added to the polystyrene
resin at the source; and iron and steel production.
(Source:
Amended at
Ill. Req.
______,
effective
____________
Section 219.963
Permit Conditions
No person shall violate any condition
in a permit when the
condition results
in exclusion of the plantsource or an emission
sourccunit from this Subpart.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
_________________________
)
Section 219.966
Control Requirements
Every owner or operator of an emission sourcemiscellaneous
organic chemical manufacturing process emission unit,
subject to
this Subpart shall comply with the requirements
of subsection
(a)~e~ (b)
,
or
(c)
below.
-
a)
Emission capture and control techniques which achieve
an overall reduction
in uncontrolled VON emissions of
at least 81 percent -from each emission unit,
or
(Board Note:
For the purpose of this provision,
an
emission unit
is any part or activity at a source of
a
type that by itself is subject to control requirements
in other Subparts of this Part or 40 CFR 60,
incorporated by reference
in Section 219.112,
e.g.,
a
coating
line,
a printing line,
a process unit,
a
wastewater system,
or other equipment,
or is otherwise
any part or activity at
a source.)

548
b)
An
alternative
control
plan
which
has
been
approved
by
the Agency and approved by the USEPA
in
a federally
enforceable
permit
or
as
a
SIP
revision.
£1
Any leaks from components subject to the control
requirements
of
this
Subpart
shall
be
subject
to
the
following
control
measures
by
March
15,
1995:
~j.
Repair any component from which
a leak of VOL can
be observed.
The repair shall be completed
as soon
as practicable but no later than
15 days after the
leak is found, unless the leaking component cannot
be repaired until the next process unit shutdown,
in which case the leaking component must be
repaired before the unit
is restarted.
21
For any leak which cannot be readily repaired
within one hour after detection, the following
records,
as set forth in this subsection,
shall be
kept.
These records shall be maintained by the
owner or operator for a minimum of two years after
the date on which they are made.
Copies of the
records shall
be made available to the Agency or
USEPA upon verbal or written request.
~j
The name and identification
of the leaking
component
~J
The date and time the leak
is detected
~j
The action taken to repair the leak;
and
Qj
The date and time the leak
is repaired.
(Source:
Amended at
Ill. Reg.
______,
effective
____________
Section 219.967
Compliance Schedule
Every owner or operator of an emission sourceunit subject to the
control requirements ofthis Subpart shall comply with the
requirements of this Subpart on and after a date consistent with
Section 219.106
of this Part.
(Source:
Amended
at
Ill.
Reg.
______,
effective
____________
Section 219.968
Testing
a)
When In the opinion of the Agency it
is necessary to
conduct testing to demonstrate compliance with Section
219.966 of this Part,
the owner or operator of
a VON

549
emission sourccunit subject to the requirements of this
Subpart shall,
at his own expense, conduct such tests
In accordance with the applicable test methods and
procedures specified
in Section 219.105 of this Part.
b)
Nothing in this Section shall limit the authority of
the USEPA pursuant to the Clean Air Act,
as amended, to
require testing.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
SUBPART TT:
OTHER EMISSION SOURCES UNITS
Section 219.980
Applicability
a)
The requirements of this Subpart shall apply to a
plant’csource’s VOM emission sourccsunits, which are
not included within any of the source categories
specified
in Subparts
B,
E,
F,
H,
Q,
R,
5,
L.
V,
X,
Y,
Z, AA,
~
PP,
QQ,
or RR of this Part,
or are not
exempted from permitting requirements pursuant to 35
Ill. Adm.
Code 201.146,
if the plantsource is subject
to this Subpart.
A plantsource is subject to this
Subpart
if
it contains process emission sourccsunits,
not regulated by Subparts
B,
E,
F (excluding Section
219.204(1)
of this Part),
H (excluding Section 219.405
of this Part),
Q,
R,
5,
T,
(excluding Section 218.486
of this Part),
V,
X,
Y ~
Z or BE of this Part, which
as a group both:
-
1)
~iHave maximum theoretical emissions of
91 Mg
(100
tons)
or more per calendar year of VOM if no air
pollution control equipment were used,
and
2)
a~renot limited to less than 91 Mg
(100 tons)
of
VOM emissions per calendar year in the absence of
air pollution control equipment,
through
production or capacity limitations contained in a
federally enforceable construction or operating
permit or a SIP revision.
b)
If a p-1-antsource ceases to fulfill the criteria of
subsection
(a)
of this Section, the requirements of
this Subpart shall continue to apply to an emission
sour—e-eunit which was ever subject to the control
requirements of Section 219.986 of this Part.
c)
No limits under this Subpart shall apply to emission
sourcesunits with emissions of VON to the atmosphere
less than or equal to 2.3 Mg
(2.5 tons)
per calendar
year
if the total emissions from such sources emission

550
unit not complying with Section
219.986
of
this
Part
does not exceed 4.5 Mg
(5.0 tons) per calendar year.
d)
For the purposes of this Subpart,
an emission c-ouree
unit shall
be considered regulated by a Subpart
if
it
is subject to the limits of that Subpart.
An emission
sourceunit
is not considered regulated by a Subpart if
it is not subject to t~elimits of that Subpart,
e.g.,
the emission unit
is e~veredby an exemption
in the
Subpart or the applicability criteria of the Subpart
are not met.
-ts emissions arc below
the
applicabili-t-y
cutoff level or
if the source is covered
by
an
exemption.
e)
The control requirements
in Subparts
-QQ,
RR,
SE and TT
shall not apply to sewage treatment plants-~-j.vegetable
oil extraction and processing plants,~coke ovens
(including by—product recovery plants)~jfuel
combustion sourcesTunits; bakeriesT~barge loading
facilitIes-a jet engine test cellsTl pharmaceutical
manufacturing, production of polystyrene foam
insulation board -~includingstorage and extrusion of
scrap where blowing agent is added to the polystyrene
resin at the plantsource-)-,
but not including blending
and preliminary expansion of resin prior to molding
where
a blowing agent is incorporated into the
polystyrene resin by the producer of the resin
production of polystyrene foam packaging -?not including
blending and preliminary expansion of resin prior to
molding where blowing agent
is incorporated into the
polystyrene resin bY the producer of the resin:
and
not
including storage and extrusion of scrap where blowing
agent is added to the polystyrene resin at the
plantsource)T.j and iron and steel production.
(Source:
Amended
at
Ill.
Req.
______,
effective
____________
Section
219.983
Permit Conditions
No person shall violate any condition In a permit when the
condition results
in exclusion of the plantsource or an emission
sourccunit from this Subpart.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section
219.986
Control Requirements
Every owner or operator of an emission sourceunit subject to this
Subpart shall comply with the requirements of subsection
(a),
(b)~e~(c),
(d)
or
(e)
below.

551
a)
Emission capture and control equipment which achieve
ar
overall reduction
in uncontrolled VON emissions of at
least 81 percent from each emission unit,
or
(Board Note:_ For the purpose of this provision,
an
emission unit is any part or activity at a source of a
type that by itself
is subject to control requirements
in other Subparts of this Part or 40 CFR 60,
incorporated by reference In Section 219.112,
e.g.,
a
coating line,
a printing line,
a process unit,
a
wastewater system,
or other equipment,
or
is otherwise
any part or activity at
a source.)
b)
For coating lines,
the daily-weighted average VON
content shall not exceed 0.42
kg VOM/l
(3.5
lbs
VON/gal)
of coating
(minus water and any compounds
which are specifically exempted from the definition of
VON)
as applied during any day.
Owners and operators
complying with this Section are not required to comply
with Section 219.301 of this Part,
or
c)
-
An alternative control plan which has been approved by
the Agency and approved by the USEPA in a federally
enforceable permit or as
a SIP revision.
~
Non—contact process water cooling towers which are
subject to the control requirements
of this Subpart
shall comply with the following control measures no
later than March
15,
1995 or upon initial startup:
~j.
The owner or operator of
a non—contact process
water cooling tower shall perform the following
actions to control emissions of volatile organic
material
(VON)
from such
a tower:
~j
Inspect and monitor such tower to identify
leaks of VOM into the water,
as further
specified
in subsection
(d) (3) below
-
~
When
a leak is identifled,
initiate and carry
out steps to identify the specific leaking
component or components as soon as
practicable,
as further specified In
subsection
(d) (4) below.
~j
When
a leaking component
is identified which:
Jj
Can be removed from service without
disrupting production, remove the
component from service

552
-
jjj
Cannot be removed from service without
disrupting production, undertake repair
of the component at the next reasonable
opportunity to do so including any
period when the component is out of
service for scheduled maintenance, as
further specified in subsection
(d) (4)
below:
Qj
Maintain records of
inspection
and monitoring
activities,
identification of leaks and
leaking components,
elimination and repair of
leaks,
and operation of equipment as related
to these activities,
as further specified in
subsection
(d) (5)
below.
21
A VON leak shall be considered to exist
in
a non-
contact process water cooling water system
if the
VON emissions or VON content exceed background
levels as determined by monitoring conducted in
accordance with subsection
(d) (3) (A)
below.
.~j
The owner or operator of an non—contact process
water cooling tower shall carry out an inspection
and monitoring program to identify VON leaks in
the cooling water system.
~j
The owner or operator of a non—contact
process water cooling tower shall submit to
the Agency
a proposed monitoring program,
accompanied by
technical justification for
the program,
including justification for the
sampling location(s), parameter(s) selected
for measurement, monitoring and inspection
frequency,
and the criteria used relative to
the monitored parameters to determine whether
a
leak exists
as specified in subsection
(d) (2) above.
~j
This inspection and monitoring program for
non—contact process water cooling towers
shall include, but shall not be limited to:
j)
Monitoring of each such tower with
a
water flow rate of 25,000 gallons per
minute or more at a petroleum refinery
at least weekly and monitoring of other
-
towers at least monthly
jjj
Inspection of each such tower
at least
weekly
if monitoring
is -not performed at
-
least weekly~

553
~j
This inspection and monitoring program shall
be carried out in accordance with written
procedures which the
Agency shall specify as
a condition in
a federally enforceable
operating permit. These procedures shall
include the VOM background levels for the
cooling tower
as established by
the owner or
operator through monitoring; describe the
locations at which samples will be taken;
identify the parameter(s)
to be measured,
the
freguency of measurements,
and the procedures
for monitoring each such tower,
that is,
taking of samples and other subsequent
handling and analyzing of samples; provide
the criteria used to determine that
a leak
exists as specified
in subsection
(d) (2)
above;
and describe the records which will be
maintained.
~
A non—contact process water cooling tower
is
exempt from the requirements of subsections
(d) (3) (B)
and
(d) (3) (C)
above,
if all
equipment, where leaks of VON into cooling
water may occur,
is operated at a minimum
pressure
in the cooling water of at least 35
kPa greater than the maximum pressure in the
process fluid.
il
The repair of a leak in a non—contact process
water cooling tower shall be considered to be
completed in an acceptable manner as follows:
~j
Efforts to identify
and locate the leaking
components are initiated as soon as
practicable,
but
in no event later than three
days after detection of the leak in the
cooling water tower:
~j
Leaking components shall be repaired or
removed from service as soon as possible but
no later than 30 days after the leak in the
cooling water tower
is detected, unless the
leaking components cannot be repaired until
the next scheduled shutdown for maintenance.
~j
The owner or operator of a non—contact process
water cooling tower shall keep records
as set
forth below in this subsection.
These records
shall be retained at a readily accessible location
at the source and shall be available for
inspection and copying by the Agency for at least
3 years:

-
554
j~j
Records of inspection and monitoring
activity
~J
Records of each leak identified in such
tower,
with date, time and nature of
observation or measured level of parameter
çj.
Records of activity to identify leaking
components, with date initiated,
summary of
components inspected with dates,
and method
of inspection and observations
Qj
Records of activity to remove
a leaking
component from service or repair
a leaking
component, with date initiated and completed,
description of actions taken and the basis
for determining the leak in such tower has
been eliminated.
If
the leaking component
is
not identified, repaired or eliminated within
30 days
of initial identification of a leak
in such tower,
this report shall
include
specific reasons why the leak could not be
eliminated sooner including all other
intervening periods when the process unit was
out of service, actions taken to minimize VON
losses prior to elimination of the leak and
any actions taken to prevent the recurrence
of
a leak of this type.
~QJ
The owner or
operator of
a non—contact process
water cooling tower shall submit an annual report
to the Agency which provides:
~j.
The number of leaks identified in each
cooling tower
~j.
A general description of activity to repair
or eliminate leaks which were identified
çj
Identification of each leak which was not
repaired
in
30 days from the date of
identification of a leak in such a tower,
with description of the leaks, explanation
why the leak was not repaired
in 30 days:
pj.
Identification of any periods when required
inspection and monitoring activities were not
carried out.
~j
Any leaks from components subject to the control
requirements of this Subpart shall
be subject to the
following control measures by March 15,
1995:

555
,~j.
Repair any component from which
a leak of VOL can
be
observed.
The
repair
shall
be
completed
as
soon
as practicable but no later than 15 days after the
leak is found, unless the leaking component cannot
be repaired until the next process unit shutdown,
-
in which case
the leaking component must be
repaired before the unit
is restarted.
21
For any leak which cannot be readily repaired
within one hour after detection,
the following
records,
as set forth below in this subsection,
shall be kept.
These records shall be maintained
by the owner or operator for
a minimum of two
years after the date on which they are made.
Copies of the records shall be made available to
the Agency or USEPA upon verbal or written
request.
Al
The name and identification of the leaking
component
~J.
The date and time the leak is detected
Qj
The action taken to repair the leak;
and
Qj
The date and time the leak is repaired.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
Section 219.987
Compliance Schedule
Every owner or operator of an emissions sourccunit which is
subject to this Subpart shall comply with the requirements of
this Subpart on and after a date consistent with Section 219.106
of this Part.
(Source:
Amended at
Ill. Req.
______,
effective
____________
Section 219.988
Testing
a)
When in the opinion of the Agency it is necessary to
conduct testing to demonstrate compliance with Section
219.986 of this Part,
the owner or operator of
a VON
emission sourceunit subject to the requirements of this
Subpart shall, at his own expense,
conduct such tests
in accordance with the applicable test methods and
procedures specified in Section 219.105.

556
b)
Nothing in this Section shall
limit the authority of
the USEPA pursuant to the Clean Air Act,
as amended,
to
require testing.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________
SUBPART
tJU:
RECORDKEEPING AND REPORTING FOR NON-ci~SOURCES
Section 219.990
Exempt Emission SeurcesUnits
Upon request by the Agency,
the owner or operator of an emission
unit source which
is exempt from the requirements of Subparts PP,
QQ,
RR,
TT
or
Section
219.208(b)
of
this
Part
shall
submit
records
to the Agency within
30 calendar days from the date of
the request that document that the emission unit source is exempt
from those requirements.
(Source:
Amended at
Ill.
Req.
______,
effective
____________
Section
219.991
Subject
Emission
CourcesUnits
a)
Any owner or operator of
a VON emission
sourceunit
which
is subject to the requirements of Subpart PP, QQ,
PR or TT and complying by the use of emission capture
and control equipment shall comply with the following:
1)
By
a date consistent with Section 219.106
of this
Part,
or upon initIal start—up of a new emission
&e~eeunit, the owner or operator of the subject
VON emission sourceunit shall demonstrate to the
Agency ~e
that the subject emission courceunit
will be in compliance on and after a date
consistent with Section 219.106
of this Part,
or
on and after the initial start-up date by
submitting to the Agency all calculations and
other supporting data,
including descriptions and
results of any tests the owner or operator may
have performed.
2)
On and after a date consistent with Section
219.106 of this Part,
or on and after the initial
start—up date, the owner or operator of a subject
VON em4s-s-i-en source shall collect and record all
of the following information each day and maintain
the information at the facilitysource for a period
of three years:
A)
Control device monitoring data.

557
B)
A log of operating time for the capture
system,
control device, monitoring equipment
and the associated emission source.
C)
A maintenance log for the capture system,
control device and monitoring equipment
detailing all routine
and non—routine
maintenance performed including dates
and
duration of any outages.
3)
On and after a date consistent with Section
219.106
of this Part,
the owner or operator of
a
subject VON emission source shall notify the
Agency in the following instances:
A)
Any record showing a violation of the
requirements of Subpart PP, QQ, PR
or TT
shall
be
reported
by
sending
a
copy
of
such
record
to
the
Agency
within
30
days
following
the occurrence of the violation.
B)
At least 30 calendar days before changing the
method of compliance with Subpart PP or TT
from the use of capture systems and control
devices to the use of complying coatings, the
owner or operator shall comply with all
requirements of subsection
(b) (1)
of this
Section.
Upon changing the method of
compliance with Subpart PP or TT from the use
of capture systems and control devices to the
use of complying coatings,
the owner
or
operator shall comply with all requirements
of subsection
(b)
of this Section.
4)
Testing
A)
When in the opinion of the Agency It is
necessary to conduct testing to demonstrate
compliance with this Subpart, the owner
or
operator of a VON emission source subject to
the requirements
of this Subpart shall, at
his own expense,
conduct such tests
in
accordance with the applicable test methods
and procedures specified in Section 219.105
of this Part.
B)
Nothing in this Section shall
limit the
authority of the USEPA pursuant to the Clean
Air Act,
as amended, to require testing.

558
b)
Any owner or operator of a coating line which
is
subject to the requirements of Subpart PP or TT and
complying by means of the daily—weighted average VON
content limitation shall comply with the following:
1)
By
a date consistent with Section 219.106 of this
Part,
or upon initial start-up of a coating line
subject to Subpart PP or TT, the owner or operator
of the subject coating line shall certify to the
Agency that the coating line will be in compliance
on
and
after
a
date
consistent
with
Section
219.106
of this Part,
or on and after the initial
start-up date.
Such certification shall include:
A)
The name and identification number of each
coating line which will comply by means of
the daily-weighted average VON content
limitation.
B)
The name and identification number of each
coating
as
applied
on
each
coating
line.
C)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating
line.
D)
The instrument or method by which the owner
or operator will accurately measure or
calculate the volume of each coating as
applied
each
day
on
each
coating
line.
E)
The method by which the owner or operator
will create and maintain records each day as
required in subsection
(b) (2).
F)
An example of the format in which the records
required in subsection
(b) (2)
of this Section
will be kept.
2)
On and after a date consistent with Section
219.106 of this Part,
or on and after the initial
start—up date,
the owner or operator of a subject
coating line shall collect and record all of the
following information each day for each coating
line and maintain the information at the
#a-e-i-l-i#ysource for a period of three years:
A)
The name and identification number of each
coating as applied on each coating line.

559
B)
The weight of VON per volume and the volume
of each coating
(minus water and any
compounds which are specifically exempted
from the definition of VON)
as applied each
day on each coating line.
C)
The daily-weighted average VON content of all
coatings as applied on each coating line as
defined in Section 219.104
of this Part.
3)
On and after a date consistent with Section
219.106 of this Part, the owner or operator of a
subject coating line shall notify the Agency in
the following instances:
A)
Any record showing violation of the
requirements of Subpart PP or TT shall be
reported by sending
a copy of such record to
the Agency within 30 days following the
occurrence of the violation.
B)
At least 30 calendar days before changing the
method of compliance with Subpart PP or TT
from the use of complying coatings to the use
capture systems and control devices, the
owner or operator shall comply with all
requirements of subsection
(a) (1)
of this
Section.
Upon changing the method of
compliance with Subpart PP or TT from the use
of complying coatings to the use capture
systems and control devices, the owner or
operator shall comply with all requirements
of subsection
(a)
of this Section.
c)
Any owner or operator of
a VON emission source which
is
subject to the requirements of Subpart PP,
QQ, RR or TT
and complying by means of an alternative control plan
which has been approved by the Agency and approved by
the USEPA as a SIP revision shall comply with the
recordkeepinq and reporting requirements specified
in
the alternative control plan.
(Source:
Amended at
Ill. Req.
______,
effective
____________

-
560
Section 219.Appendix A
List of Chemicals Defining Synthetic
Organic Chemical and
Polymer Manufacturing
CAS No.
a
105—57—7
75—07—0
107—89—1
60—35—5.
103—84—4
64-~.l9—7
108—24—7
67—64—1
75—86—5
75—05—8
98—86—2
75—36—5
74—86—2
107—02—8
79—06—1
79—10—7
107—13—1
124—04—9
111—69—3
(b)
107—18—6
107—05—1
1321—il—S
111—4
1—1
123—30—8
628—63—7,
123—92—2
71—4l—0~
110—58—7
543—59—9
llO—68—7
1322—06—1
62—53—3
142—04—1
29191—52—4
100—66—3
118—92—3
84—65—1
100—52—7
55—21—0
71—43—2
98—48—6
98—11—3
134—81—6
76—93—7
Chemical
Acetal
Acetaldehyde
Acetaidol
Acetamide
Acetanilide
Acetic acid
Acetic anhydride
Acetone
Acetone cyanohydrin
Acetonitrile
Acetophenone
Acetyl chloride
Acetylene
Acrolein
Acrylamide
Acrylic acid
&
esters
Acrylonitrile
Adipic acid
Adiponitrile
Alkyl
naphthalenes
Ally?
alcohol
Ally? chloride
Aminobenzoic acid
Aminoethylethanolamine
p—aminophenol
Amyl acetates
Amyl alcohols
Amyl amine
Amy? chloride
Amy? mercaptans
Amyl phenol
Aniline
Aniline hydrochloride
Anisidine
Anisole
Anthranilic acid
Anthraquinone
Benzaldehyde
Benzamide
Benzene
Benzenedisulfonic acid
Benzenesulfonic acid
Benzil
Benzilic acid

561
65-85-0
Benzoic acid
119—53—9
Benzoin
100-47-0
Benzonitrile
119-61-9
Benzophenone
98-07-7
Benzotrichloride
98—88-4
Benzoyl chloride
100-51-6
Benzyl alcohol
100—46—9
Benzylamine
120-51—4
Benzyl benzoate
100—44-7
Benzyl chloride
98-87-3
Benzyl dichloride
92-’52-4
Biphenyl
80-05-7
Bisphenol A
10-86-1
Bromobenzene
27497—51—4
Bromonaphthalene
106—99-0
Butadiene
106—98—9
1—butene
123-86-4
n—butyl acetate
141-32-2
n-butyl acrylate
71-36-3
n-butyl alcohol
78-92-2
s-butyl alcohol
75-65-0
t—butyl
alcohol
109-73-9
n-butylamine
13952-84-6
s-butylamine
-
75-64-9
t-butylamine
98-73-7
p-tert—butyl benzoic acid
107-88-0
i,3—butylene glycol
123-72-8
n-butyraldehyde
107-92-6
Butyric acid
106-31-0
Butyric anhydride
109-74-0
Butyronitrile
105-60-2
Caprolactam
75-1-SO
Carbon disulfide
558-13-4
Carbon tetrabromide
55-23-S
Carbon tetrachloride
9004—35-7
Cellulose acetate
79-11-8
Chioroacetic
acid
108—42—9
m—chloroaniline
95-Sl-2
o-chloroaniline
106-47-8
p—chloroaniline
35913-09-8
Chlorobenzaldehyde
108—90-7
-
Chlorobenzene
118-91-2,
Chlorobenzoic acid
535—80—8,
-
74_11_3c
-
2136-81-4,
Chlorobenzotrichloride
2136—89—2,
52l6_25_1c
1321-03-5
Chlorobenzoyl chloride
75-45-6
Chlorodifluoroethane
25497-29-4
Chlorodifluoromethane

562
67—66—3
25586—43—0
88—73—3
100—00—S
25167—80—0
126—99—8
7790—94—5
108—41—8
95—49—8
106—43—4
75—72—9
-
10
a—
39—4
95—48—7
106—44—S
1319—77—3
1319—77—3
4170—30—0
3724—65—0
98—82—8
80—15—9
372—09—8
506—77—4
108—80—S
108—77—0
110—82—7
108—93—0
108—94—1
110—83—8
-
108—91—8
111—78—4
112—30—1
123—42—2
27576—04—1
95—76—1,
95—82—9,
554—00—7,
608—27—5,
608—31—1,
626—43—7,
27134—27—6,
57311_92_9c
541—73—1
95—50—1
106—46—7
75—71—8
111—44—4
107—06—2
96—23—1
269S2—23—8
101—83—7
109—89—7
Chloroform
Chloronaphthalene
o—chloronitrobenzene
p-chloronitrobenzene
Chlorophenols
Chloroprene
Chlorosulfonic acid
m—chlorotoluene
o-chlorotoluene
p—chlorotoluene
Chiorotrifluoromethane
in—cresol
o—cresol
p-cresol
Mixed cresols
Cresylic acid
Crotonaldehyde
Crontonic acid
Cumene
Curnene hydroperoxide
Cyanoacetic
acid
Cyanogen chloride
Cyanuric
acid
Cyanuric chloride
Cyclohexane
Cyclohexanol
Cyclohexanone
Cyclohexene
Cyclohexylamine
Cyclooctadiene
Decanol
Diacetone alcohol
Diaminobenzoic acid
Dichloroaniline
m—dichlorobenzene
o—dichlorobenzene
p—dichlorobenzene
Dichlorodifluoromethane
Dichloroethyl ether
1, 2—dichloroethane
(EDC)
Dichlorohydrin
Dichloropropene
Dicyclohexylamine
Diethylamine

563
111—46—6
112—36—7
111—96—6
112—34—5
124—17—7
111—90—0
112’—15—2
111—77—3
64—67—S
75—37—6
25167—70—8
26761—40—0
27S54—26—3
674—82—8
124—40—3
121—69—7
115—10—6
68—12—2
57—14—7
77—78—1
75—18—3
67—68—5
120—61—6
99—34—3
51—28—5
123—91—1
646—06—0
122—39—4
101—84—4
102—08—9
25265—71—8
25378—22—7
28675—17—4
27193—86—8
106—89—8
64—17—5
l4l_43_5c
141—78—6
141—97—9
140—88—S
75—04—7
100—41—4
74—96—4
Diethylene glycol
Diethylene glycol
ether
ether
Diethylene glycol
ether
ether acetate
Diethylene glycol
ether
Diethylene glycol
ether acetate
Diethylene
glycol
ether
Diethyl sulfate
Difluoroethane
Diisobutylene
Diisodecyl phthalate
Diisooctyl phthalate
Diketene
Dimethylamine
N,N-dimethylaniline
N,N-dimethyl ether
N,
N-dimethylformamide
Dimethylhydrazme
Dimethyl sulfate
Dimethyl sulfide
Dimethyl sulfoxide
Dimethyl terephthalate
3 ,5—dinitrobenzoic acid
Dinitrophenol
Dinitrotolyene
Dioxane
Dioxilane
Diphenylamine
Diphenyl oxide
Diphenyl thiourea
Dipropylene glycol
Dodecene
Dodecylanilme
Dodecyiphenol
Epichiorohydrin
Ethanol
Ethanolamines
Ethyl acetate
Ethyl acetoacetate
Ethyl acrylate
Ethylamine
Ethylbenz
ene
diethyl
Diethylene glycol dimethyl
monobutyl
Diethylene glycol mnononbutyl
monoethy1
monoethy1
monomethyl
Ethyl bromide

564
9004-57-3
Ethylcellulose
75-00-3
Ethyl chloride
105-39-5
Ethyl chloroacetate
105-56-6
Ethylcyanoacetate
74-85-1
Ethylene
96-49-1
Ethylene carbonate
107-07-3
Ethylene chlorohydrin
107-15-3
Ethylenediamine
106-93-4
Ethylene dibromide
107-21-1
Ethylene glycol
111-55-7
Ethylene glycol diacetate
110,-71-4
Ethylene glycol dimethyl ether
111-76-2
Ethylene glycol monobutyl
ether
112-07-2
Ethylene glycol monobutyl
ether acetate
110-80-S
Ethylene glycol monoethyl
ether
111-15-9
Ethylene glycol monoethyl
ether acetate
109-86-4
Ethylene glycol monoethyl
ether
110-49-6
Ethylene glycol monomethyl
ether acetate
122-99-6
Ethylene glycol monophenyl
ether
2807-30-9
Ethylene glycol xnonopropyl
ether
7S-21-8
Ethylene oxide
60-29-7
Ethyl ether
104-76-7
2-ethylhexanol
122-51-0
Ethyl orthoformate
95-92-1
Ethyl oxalate
41892-71-1
Ethyl sodium oxaloacetate
50000
Formaldehyde
75127
Formamide
64-18-6
Formic acid
110-17-8
Fumaric acid
98—01—1
Furfural
56-81-S
Glycerol
(Synthetic)
2654S-73-7
Glycerol dichlorohydrin
2S79l-96-2
Glycerol triether
56—40—6
Glycine
107—22—2
Glyoxal
118-74-1
Hexachlorobenzene
67-72-1
Hexachloroethane
36653-82—4
Hexadecyl alcohol
124—09-4
Hexamethylenediamine
629-11-8
Hexamethylene glycol
100-97-0
Hexamethylenetetramine
74-90-8
Hydrogen cyanide
123-31-9
Hydroquinone

565
99-96-7
p-hydroxybenzoic acid
26760-64—5
Isoamylene
78-83-1
Isobutanol
110-19-0
Isobutyl acetate
115-11-7
Isobutylene
78-84-2
Isobutyraldehyde
79-31-2
Isobutyric acid
25339-17—7
Isodecanol
26952-21-6
Isooctyl alcohol
78-78-4
Isopentane
78-59-1
Isophorone
121-91-5
Isophthalic acid
78-’79-5
Isoprene
67-63-0
Isopropanol
108-21-4
Isopropyl acetate
75-31-0
Isopropylamine
75-29-6
Isopropyl chloride
25168-06-3
Isopropylphenol
463-51-4
Ketene
Linear alkyl sulfonate*
123-01-3
Linear alkylbenzene
110—16—7
Maleic acid
108-31—6
Maleic anhydride
6915—15—7
Malic acid
141-79-7
Mesityl oxide
121-47-1
Metanilic acid
79-41-4
Nethacrylic acid
563-47-3
Nethallyl chloride
67—56—1
Methanol
79-20-9
Methyl acetate
105-45-3
Methyl acetoacetate
74-89-5
Methylamine
100-61—8
n—methylaniline
74-83-9
Methyl bromide
37365-71-2
Methyl butynol
7487-3
Methyl chloride
108-87-2
Methyl cyclohexane
1331-22-2
Methyl cyclohexanone
75-09-2
Nethylene
chloride
101-77—9
Methylene dianiline
101-68-8
Nethylene diphenyl
diisocyanate
78-93-3
Methyl ethyl ketone
107-31-3
Methyl formate
108-11—2
Methyl isobutyl carbinol
108-10-1
Methyl isobutyl ketone
80626
Methyl xnethacrylate
77-75-8
Methylpentynol
98-83-9
B-methylstyrene
110918
Norpholine
85-47-2
a—riaphthalene
sulfonic
acid

-566
120-18-3
B—naphthalene sulfonic acid
90153
a—naphthol
135193
B—naphthol
75-98-9
Neopentanoic acid
88—74—4
o—nitroaniline
100—01—6
p—nitroaniline
91—23—6
o—nitroanisole
100—17—4
p—nitroanisole
98-95-3
Nitrobenzene
27178_83_2c
Nitrobenzoic acid
(0,
m
&
p)
79-24-3
Nitroethane
75-52-5
Nitromnethane
88-75-5
-
Nitrophenol
25322-01-4
Nitropropane
1321-12-6
Nitrotoluene
27215—95—8
Nonene
25154-52-3
Nonyiphenol
27193-28—8
Octylphenol
123-63-7
Paraldehyde
115-77-S
Pentaerythritol
109—66—0
n—pentane
109—67—1
1—pentene
127-18-4
Perchloroethylene
594-42-3
Perchloromethyl
mnercaptan
94-70-2
o-phenetidine
156-43-4
p—phenetidine
108—95—2
Phenol
98-67-9,
Phénolsulfonic acids
585—38—6,
609—46—1,
133_39_7c
91-40-7
Phenyl anthranilic acid
Phenylenediamine
75-44-S
Phosgene
8544-9
Phthalic anhydride
85416
Phthalimide
108-99-6
b—picoline
110—85—0
Piperazine
9003—29-6,
Polybutenes
25036_29_7c
25322-68-3
Polyethylene glycol
25322-69-4
Polypropylene glycol
123-38-6
Propionaldehyde
79-09-4
Propionic acid
71-23-8
n-propyl alcohol
107-10-8
Propylamine
540—54-5
Propyl chloride
115-07-1
Propylene
127-00-4
Propylene chiorohydrin
78-87-S
Propylene dichioride
57-SS-6
Propylene glycol

567
75—S6—9
110—86—1
106—51—4
108—46—3
27138—S7—4
69—72—7
127—09—3
532—32—1
9004—32—4
3926—62—3
141—53—7
139’—02—6
110—44—1
100—42—S
110—15—6
110—61—2
121—57—3
126—33—0
1401—55—4
100—21—0
7934_5C
117—08—8
78—00—2
119—64—2
8S—43—8
75—74—1
110—60—1
110—18—9
108—88—3
95—80—7
S84—84—9
26471—62—S
1333—07—9
l04_15_4c
98—59—9
26915—12—8
87—61—6,
108—70—3,
l20_82_lc
71—55—6
79—00—S
79—01—6
75—69—4
96—18—4
76—13—1
121—44—8
112—27—6
112—49—2
Propylene oxide
Pyridine
Quinone
Resorcinol
Resorcylic acid
Salicylic acid
Sodium acetate
Sodium benzoate
Sodium carboxymethyl cellulose
Sodium chloroacetate
Sodium formate
Sodium phenate
Sorbic acid
Styrene
Succinic acid
Succinitrile
Sulfanilic acid
Sulfolane
Tannic acid
Terephthalic acid
Tetrach
loroethanes
Tetrachlorophthalic anhydride
Tetraethyllead
-
Tetrahydronaphthalene
Tetrahydrophthalie anhydride
Tetramethyllead
Tetramethy1enediamine
Tetramethy
lethylenediamine
Toluene
Toluene-2
,
4-diamine
Toluene—2
,
4—diisocyanate
Toluene diisocyanates
(mixture)
Toluene sulfonamide
Toluenesulfonic acids
Toluene sulfonyl chloride
Toluidines
Trichlorobenzenes
1, 1, 1—trichloroethane
1,
1
,2—trichloroethane
Trichloroethylene
Trichlorofluoromethane
1,2, 3—trichloropropane
1,1, 2—trichloro-l, 2, 2-trifluor
oethane
Triethylamine
Triethylene glycol
Triethylene
glycoldimethyl
ether

S68
7756—94-7
Trlisobutylene
75-50-3
Trimethylamine
57—13—6
Urea
108-05—4
Vinyl acetate
7S—01-4
Vinyl chloride
7S-3S-4
Vinylidene chloride
2S0l3—1S—4
Vinyl toluene
1330—20—7
Xylenes
(mixed)
95—47—6
o-xylene
106-42-3
p—xylene
1300—71—6
Xylenol
130,0—73—8
Xylidine
methyl tert-butyl ether
9002-88-4
Polyethylene
Polypropylene
9009—53-6
Polystyrene
-
a)
CAS
numbers
refer
to
the
Chemical
Abstracts
Registery
numbers assigned to specific chemicals,
isomers
or
mixtures of chemicals.
Some isomers or mixtures that
are covered by the standards
do not have CAS numbers
assigned to them.
The standards apply to all of the
chemicals listed, whether CAS numbers have been
assigned or not.
b)
No CAS number(s) have been assigned to this chemical,
to its isomers,
or mixtures containing these chemicals.
c)
-CAS numbers for some of the isomers are listed:
the
standards apply to all of the Isomers and mixtures,
even if CAS numbers have not been assigned.
(Source:
Amended at
Ill.
Req.
______,
effective
_________

569
Section 219.Appendix B
VOM Measurement Techniques for Capture Efficiency
Procedure G.1
-
Captured VO
Emissions
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for
determining
the volatile organic compoundsm~terials (VO~) content of
captured gas streams.
It is intended to be used as a segment
in
the development
of liquid/gas or gas/gas protocols for
determining
Vc~Gr.j capture efficiency
(CE)
for surface coating and
printing operations.
The procedure may not be acceptable
in
certain site-specific situations,
e.g.,
when:
(1) direct fired
heateçs or other circumstances affect the quantity of VOGM at the
control device inlet;
and
(2) particulate organic aerosols are
formed in the process and are present
in the captured emissions.
1.2
Principle.
The amount of VOGM captured
(G)
is calculated as
the sum of the products of the VOGrj content
(CGJ),
the flow rate
(QG~)’
and the sample time
(To)
from each captured emissions
point.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each captured or fugitive
emissions point as follows:
Q~
=
5.5 percent and
CGJ
=
~5.0 percent.
Based on these numbers,
the probable
uncertainty for G is estimated
at about L7.4 percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least t~ireesampling runs.
The sampling time for
each run should be at least 8 hours, unless otherwise approved.
1.5
Notes.
Because this procedure
is often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations
(percent, ppm)
are by
volume,
unless otherwise noted.
2.
APPARATUS AND REAGENTS
2.1
Gas VO?N Concentration.
A schematic of the measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1
Sample Probe.
Stainless steel,
or equivalent.
The probe
shall
be
heated
to
prevent
VGGM
condensation.
2.1.2
Calibration
Valve
Assembly.
Three-way
valve
assembly
at
the outlet of sample probe to direct the zero and calibration

570
gases to the analyzer.
Other methods,
such as quick—connect
lines, to route calibration gases to the outlet of the sample
probe
are
acceptable.
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport
the
sample
gas
to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak-free pump,
to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components of the
pump that contact the gas stream shall be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent
condensation.
2.1.S
Sample Flow Rate Control.
A sample flow rate control
valve and rotameter,
or equivalent, to maintain a constant
sampling rate within
10. percent.
The flow rate control valve and
rotameter must be heated to prevent condensation.
A control
valve may also be located on the sample pump bypass loop to
assist in controlling the sample pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion of
the sample gas stream to the flame ionization analyzer
(FIA), and
the remainder to the bypass discharge
vent.
The manifold
components shall
be constructed of stainless steel or Teflon.
If
captured or fugitive emissions
are
to be measured at multiple
locations,
the measurement system shall be designed to use
separate sampling probes,
lines,
and pumps for each measurement
location and
a common sample gas manifold and FIA.
The sample
gas manifold and connecting
lines to the FIA must be heated to
prevent condensation.
2.1.7
Organic
Concentration
Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however,
other span values may be used if it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than
±3.0percent of the span value.
2.1.7.2
Calibration
Drift.
Less
than
±3.0
percent
of the span
value.
-
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.1.7.4
Response Time.
Less than
30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record

571
measurement data.
The minimum data sampling frequency for
computing average or integrated values is one measurement value
every
S seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required)
are contained in
compressed gas cylinders.
All calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer
of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration ‘does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtu~es, such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent H2/60 percent He or 40 percent H2/60
percent
N2 gas mixture
is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from
a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material
(as propane or carbon equivalent)
or less than
0.1 percent of the span value, whichever
is greater.
-
2.1.9.3
FIA Linearity Calibration Gases.
Low-, mid—,
and
high—range gas mixture standards with nominal propane
concentrations
of 20-30,
45-55, and 70-80 percent of the span
value
in air,
respectively.
Other calibration values and other
span values may be used if
it can be shown that more accurate
measuremer~ts
would
be
achieved.
2.1.10
Particulate
Filter.
An
in-stack
or
an out-of-stack glass
fiber filter is recommended
if exhaust gas particulate loading is
significant.
An out-of—stack filter must be heated to prevent
any condensation unless
it can be demonstrated that no
condensation occurs.
2.2
Captured Emissions Volumetric Flow Rate.
2.2.1
Method
2 or 2A Apparatus.
For
determining
volumetric
flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used
if it can be justified.
2.2.3
Method
4
Apparatus
and
Reagents.
For
determining
moisture
content,
if necessary.

572
3.
DETERMINATION OF VOLUMETRIC FLOW RATE OF CAPTURED EMISSIONS
3.1
Locate all points where emissions are captured from the
affected
facilityemission
unit.
Using
Method
1,
determine
the
sampling
points.
Be
sure
to
check
each
site
for
cyclonic
or
swirling flow.
3.2
Measure the velocity at each sampling site at least once
every
hour
during
each
sampling
run
using
Method
2
or
2A.
4.
DETERMINATION OF VOG~,j
CONTENT
OF CAPTURED EMISSIONS
4.1
Analysis Duration.
Measure the VOGN responses at each
captured emissions point during the entire test run or,
if
applicable, while the process
is operating.
If there are
multiple captured emission locations,
design
a sampling system to
allow a single FIA to be used to determine the VO~ responses at
all
sampling
locations.
4.2
Gas
VO~j
Concentration.
4.2.1
Assemble the sample train as shown in Figure
1.
Calibrate
the FIA according to the procedure in Section 5.1.
4.2.2
Conduct a system check according to the procedure
in
Section 5.3.
4.2.3
Install the sample probe so that the probe
is centrally
located in the stack, pipe,
or duct, and is sealed tightly at the
stack port connection.
-
4.2.4
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach
zero.
Measure
the
system response time as the time required for the system to reach
the effluent concentration after the calibration valve has been
returned
to
the
effluent
sampling
position.
4.2.5
Conduct
a system check before and a system drift check
after each sampling run according to the procedures in Sections
5.2 and 5.3.
If the drift check following a run indicates
unacceptable
performance,
the
run
is not valid.
The tester may
elect
to
perform
system drift checks during the run not to exceed
one drift check per hour.
4.2.6
Verify that the sample lines,
filter, and pump
temperatures are 120 ±5°C.
4.2.7
Begin
sampling
at
the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
appropriate.
If multiple captured emission locations are sampled
using
a single FIA,
sample at each location for the same amount

-
573
of time
(e.g.,
2 minutes)
and continue to switch from one
location to another for the entire test run.
Be sure that total
sampling time at each location is the same at the end of the test
run.
Collect at least
4 separate measurements from each sample
point during each hour of testing.
Disregard the measurements at
each sampling location until two times the response time of the
measurement system has elapsed.
Continue sampling for at least
1
minute and record the concentration measurements.
4.3
Background Concentration.
4.3.1
Locate ~ll NDO’s of the TTE.
A sampling point shall be
centrally located outside of the TTE at
4 equivalent diameters
from each NDO,
if
possible.
If there are more than
6 NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.2
Assemble the sample train as shown in Figure
2.
Calibrate
the FIA and conduct a system check according to the procedures in
Sections 5.1 and 5.3.
NOTE:
This sample train shall be a
-
separate sampling train from the one
to
measure
the
captured
emissions.
4.3.3
Position the probe at the sampling location.
4.3.4
Determine the response time,
conduct the system check and
sample according to the procedures described in Sections 4.2.4 to
4.2.7.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described
in Section 7.2 of Method 18 may be
used to determine the
gas VO~jconcentration.
The system must be designed to collect
and analyze at least one sample every 10 minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air ~and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero— and the high—range calibration
gases and adjust the analyzer calibration to provide the proper
responses.
Inject the low— and mid—range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable
if the responses for all
four
gases
are
within
5 percent of the respective gas values.
If
the performance of the system
is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct a calibration
and linearity check after assembling the analysis system and
after
a
major
change
is
made
to
the
system.

574
5.2
Systems Drift Checks.
Select the calibration gas that most
closely approximates the concentration of the captured emissions
for conducting the drift checks.
Introduce the zero and
calibration gas at the calibration valve assembly and verify that
the appropriate gas flow rate and pressure are present at the
FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained in Section 5.1 is less than 3 percent of the span
value.
Conduct the system drift checks at the end of each run.
5.3
System Check.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
The
performance of the system is acceptable
if the measurement system
response
is within 5 percent of the value obtained in Section 5.1
for the high range calibration gas.
Conduct a system check
before and after each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described
in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
-
6.
NOMENCLATURE
A~
=
area of NDO
1, ft2-~
AN
=
total area of all NDO’s in the enclosure,
ft2--~
C81
=
corrected average VOC~concentration of background
emissions at point
i, ppm propane--j
CB
=
average background concentration,
ppm propane--j.
CGJ
=
corrected average VOC~concentration of captured
emissions at point
j,
ppm propane--~j
=
average measured concentration for the drift check
calibration gas, ppm propane--;
C~
=
average system drift check concentration for zero
concentration gas, ppm propane-ri
CH
=
actual concentration of the drift check
calibration gas, ppm propane-.-~
C1
=
uncorrected average background VOC~concentration
measured at point
i, ppm propane-~
C~
=
uncorrected average VOCM concentration measured at
point
j,
ppm propane-~

575
G
=
total
VOC~content of captured emissions,
kg--i
K1
=
1.830 x 10~kg/(m3-ppm)-~~
n
=
number of measurement points-~j
~
=
average
effluent
volumetric
flow
rate
corrected
to
standard conditions at captured emissions point
j,
m3
/
min-ri
T~
=
total
duration
of
captured
emissions
sampling
run,
mm.
7.
CALCULATIONS
7.1
Total VO~ Captured Emissions.
n
G
=
E
(C0~
-
CB
) Q~
T~ K1
Eq.
1
j=l
7.2
VO~jConcentration of the Captured Emissions
at Point
j.
C~
=
(C~
-
CD~)
CH_____
Eq.
2
-
CDH
CDO
7.3
Background
VOG!~jConcentration
at Point
i.
CBI
=
(C1
-
CD~)
CH
Eq.
3
CDO
7.4
Average Background Concentration.
n
E
CB~AI
CB
=
i-i
Eq.
4
nAN
NOTE:
If the concentration at each point
is within 20 percent of
the average concentration of all points,
the terms
~A1t1and “AN”
may be deleted from Equation
4.
-
Procedure G.2
-
Captured VOGM Emissions
(Dilution Technique)
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the volatile organic e-ompoundsmaterials
(VO?I~) content
of
captured gas streams.
It is intended to be used as a segment
in
the development of a gas/gas protocol
in which fugitive emissions

576
are measure.d for determining VOG~capture efficiency
(CE)
for surface coating and printing operations.
A dilution
system is used to reduce the VOGN concentration of the captured
emission to about the same concentration as the fugitive
emissions.
The procedure may not be acceptable in certain
site—specific situations, e.g.,
when:
(1) direct fired heaters or
other circumstances affect the quantity of VO~ at the control
device inlet; and
(2) particulate organic aerosols are formed in
the process and are present in the captured emissions.
1.2
Principle.
The amount of VO~jcaptured
(G)
is calculated as
the sum of the, products of the VOG~jcontent
(CGJ), the flow rate
(QG~)’
and the sampling time
(Ta)
from each captured emissions
point.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each captured or fugitive
emissions point
as follows:
Q0~
=
±S.Spercent and C0~
= ±5
percent.
Based on these numbers, the probable uncert~aintyfor G
is estimated at about ±7.4
percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours,
unless otherwise approved.
1.5
Notes.
Because this procedure is
often
applied
in highly
explosive areas,
caution and care should be exercised
in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations
(percent,
ppm)
are by
volume, unless otherwise noted.
2.
APPARATUS AND REAGENTS
2.1
Gas
VOGN
Concentration.
A
schematic
of the measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1-
Dilution
System.
A Kipp
in-stack dilution probe and
controller or similar device may be used.
The dilution rate may
be
changed
by
substituting
different critical orifices or
adjustments of the aspirator supply pressure.
The dilution
system shall be heated to prevent VO~jcondensation.
Note:
An
out-of-stack dilution device may be used.
-
2.1.2
Calibration Valve Assembly.
Three—way valve assembly at
the
outlet
of-
sample
probe
to
direct
the
zero
and
calibration
gases to the analyzer.
Other methods, such as quick—connect
lines,
to
route
calibration gases to the outlet of the sample
probe are acceptable.

577
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak-free pump,
to pull the sample gas
through
the
system
at
a
flow
rate
sufficient
to
minimize
the
response time of the measurement system.
The components of the
pump that contact the gas stream shall be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample
Flow
Rate
Control.
A
sample
flow
rate
control
valve and rotameter,
or equivalent, to maintain a constant
sampling rate within
10 percent.
The flow control valve and
rotam?ter must be heated to prevent condensation.
A control
valve may also be located on the sample pump bypass 1oop to
assist
in controlling the sample pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion
of
the sample gas stream to the flame ionization analyzer
(FIA),
and
the
remainder
to the bypass discharge vent.
The manifold
components shall
be constructed of stainless steel or Teflon.
If
captured
or
fugitive
emissions
are
to
be
measured
at
multiple
locations,
the measurement system shall be designed to use
separate
sampling
probes,
lines,
and
pumps
for
each
measurement
location and a common sample gas manifold and FIA.
The sample
gas manifold and connecting lines to the FIA must be heated to
prevent condensation.
2.1.7
Organic Concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however,
other
span values may be used
if
it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration Drift.
Less than ±3.0percent of the span
value.
2.1.7.3
Calibration Error.
Less than
±5.0
percent of the
calibration
gas
value.
2.1.7.4
Response Time.
Less than 30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values
is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
-

-
578
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required)
are contained
in
compressed
gas
cylinders.
All
calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer
to
±1 percent
of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available,
alternative methods for preparing calibration gas
mixtures,
such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A 40 percent
112/60 percent He or 40 percent H2/60
percemt
N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from a mean value.
2.1.9.2
Carrier Gas and Dilution Air Supply.
High purity air
with less than
1 ppm of organic material
(as propane or carbon
equivalent)
or
less
than
0.1
percent
of
the
span
value,
whichever
is greater.
-
2.1.9.3
FIA Linearity Calibration Gases.
Low-, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
45-55,
and 70-80 percent of the span
value in air,
respectively.
Other calibration values and other
span values may be used if
it can
be. shown that more accurate
measurements would be achieved.
2.1.9.4
Dilution Check Gas.
Gas mixture standard containing
propane in air, approximately half the span value after dilution.
2.1.10
Particulate Filter.
An in—stack or an out-of—stack glass
fiber filter is recommended
if exhaust gas particulate loading is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless it can be demonstrated that no
condensation occurs.
2.2
Captured Emissions Volumetric Flow Rate.
2.2.1
Method
2 or
2A
Apparatus.
For determining volumetric flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if it can be justified.
2.2.3
Method
4 Apparatus and Reagents.
For determining moisture
content,
if necessary.
-

579
3.
DETERMINATION
OF VOLUMETRIC
FLOW RATE OF CAPTURED EMISSIONS
3.1
Locate all points where emissions are captured from the
affected facility. Using Method
1,
determine the sampling points.
Be sure to check each site for cyclonic or swirling flow.
3.2
Measure the velocity at each sampling site at least once
every hour during each sampling run using Method 2 or 2A.
4.
DETERMINATION-OF VO~jCONTENT OF CAPTURED EMISSIONS
4.1
Analysis ~Duration.
Measure the VOGI~jresponses at each
captured
emissions
point
during
the entire test run or,
if
applicable,
while the process
is operating.
If there are a
multiple captured emissions locations, design a sampling system
to allow a single FIA to be used to determine the VOGM responses
at all sampling locations.
4.2
Gas VO~jConcentration.
4.2.1
Assemble the sample train as shown in Figure
1.
Calibrate
the FIA according to the procedure in Section S.l.
4.2.2
Set the dilution ratio and determine the dilution factor
according to the procedure in Section 5.3.
4.2.3
Conduct
a
system check according to the procedure in
Section S.4.
4.2.4
Install the sample probe
so that the probe
is centrally
located
in the stack,
pipe,
or duct,
and
is sealed tightly at the
stack port connection.
4.2.5
Inject zero gas at the calibration valve assembly.
Measu-re the system response time as the time required for the
system to reach the effluent concentration after the calibration
valve has been returned to the effluent sampling position.
4.2.6
Conduct a system check before and a system drift check
after each sampling run according to the procedures
in Sections
5.2 and
5.4.
If the drIft check following a run indicates
unacceptable performance,
the run is not valid.
The tester may
elect to perform system drift checks during the run not to exceed
one drift check per hour.
4.2.7
Verify that the sample lines,
filter, and pump
temperatures are 120 ±S°C.
4.2.8
Begin sampling at the start
of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as

580
appropriate.
If
multiple
captured
emission
locations
are
sampled
using a single FIA,
sample at each location for the same amount
of time
(e.g.,
2 minutes)
and continue to switch from one
location to another for the entire test run.
Be sure that total
sampling time at each location
is the same at the end of the test
run.
Collect at least
4 separate measurements from each sample
point during each hour of testing.
Disregard the measurements at
each sampling location until two times the response time of the
measurement system has elapsed.
Continue sampling for at least
1
minute and record the concentration measurements.
4.3
Backgrouri,d Concentration.
-
4.3.1
Locate all NDO’s of the TTE.
A sampling point shall be
centrally
located
outside
of the TTE at
4 equivalent diameters
from each NDO,
if possible.
If there are more than
6 NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.2
Assemble the sample train as shown in Figure
2.
Calibrate
the FIA and conduct a system check according to the procedures
in
Sections 5.1 and 5.4.
4.3.3
Position
the
probe
at
the
sampling
location.
4.3.4
Determine the response time,
conduct the system check and
sample -according to the procedures described in Sections 4.2.4 to
4.2.8.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described
in Section 7.2
of Method 18 may be
used to determine the gas VOG~concentration.
The system must be
designed to collect and analyze at least one sample every
10
minutes.
S.
CALIBRATION
AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject
a calibration gas into the
measurement system after the dilution system and adjust the back—
pressure regulator to the value required to achieve the flow
rates
specified
by
the
manufacturer.
Inject
the
zero—
and
the
high—range calibration gases and adjust the analyzer calibration
-
to provide the proper responses.
Inject the low— and mid—range
gases and record
the
responses
of
the
measurement
system.
The
calibration and linearity of the system are acceptable
if the
responses for all four gases are within
5 percent of the
respective gas values.
If the performance of the system is not
acceptable, repair or adjust the system and repeat the linearity
check.
Conduct a calibration and linearity check after

581
assembling the analysis system and after a major change is made
to the system.
5.2
Systems Drift checks.
Select the calibration gas
that
most
closely approximates
.
the concentration of the diluted captured
emissions for conducting the drift checks.
Introduce the zero
and calibration gas at the calibration valve assembly and verify
that the appropriate gas flow rate and pressure are present at
the VIA.
Record the measurement system responses to the zero
and
calibration gases.
The performance of the system is acceptable
if the difference between the drift
check
measurement and the
value obtained in Section 5
1 is less
than
3 percent of the span
value.
condudt
the
system
drift
check
at the end of each run.
5.3
Determination of Dilution Factor.
Inject the dilution check
gas into the measurement system before the dilution system and
record the response.
calculate the dilution factor using
Equation 3.
5.4
System. check.
Inject the high .range calibration gas at the
inlet to the sampling probe while the dilution air is turned off.
Record the response.
The performance of the system is acceptable
if the measurement system response is within 5 percent of the
value obtained in Section 5.1 for the high range calibration gas.
conduct a system check before and after each test run.
5.5
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
6
NOMENCLATURE
A1
a
area
of
NDO
i,
ft2-rL
AN
a
total
area
of
all
NDO’s
in
the enclosure,
ft2-irj
CA
a
actual concentration of the dilution check gas,
ppm
propanerj.
a
corrected
average
voczj
concentration
of
background
emissions
at point
i,
ppm propanewj.
a
average background concentration, ppm propanev-j
a
average measured concentration for the drift check
calibration gas, ppm propan*rj.
a
average system drift check concentration for zero
concentration gas, ppm propane-rj

582
CH
=
actual concentration of the drift check
calibration gas, ppm propane--;
C1
=
uncorrected average background VOCM concentration
measured at point
i, ppm propane--j
=
uncorrected average VOCN concentration measured at
point
j, ppm propane--j
CM
=
measured concentration of the dilution check gas,
ppm propane-~j
DF
=
dilution factor-~
G
=
total VOC~content of captured emissions,
kg--j
K1
=
1.830 x 106 kg/(m3-ppm)-~~
n
=
number of measurement points--~
QG~
=
average effluent volumetric flow rate corrected to
standard conditions at captured emissions point
j,
m3 /min-rj
T~
=
total
duration
of
capture
efficiency
sampling
run,
mm.
7.
CALCULATIONS
7.1
Total VOG~jCaptured Emissions.
n
G
=
E
CGJ
QGJ
T~
K1
Eq.
1
j=l
7.2
V~~Gl~
Concentration of the Captured Emissions at Point
j.
CGJ
= DF
(C~
-
CDO)
CH_____
Eq.
2
CDH
7.3
Dilution Factor.
DF
=
CA
Eq.
3
C~
7.4
Background VO-GN Concentration at Point
i.
CB~
=
(C1
-
CDQ)
CH
Eq.
CDH
CDO
7.5
Average Background Concentration.

583
n
E
C~
A1
CB = i=1
Eq.
5
nAN
NOTE:
If
the concentration at each point is within 20 percent of
the average concentration of all points, the terms
“Ai” and “AN”
may be deleted from Equation
4.
Procedure F.2
-
Fugitive VO~N
Emissions from Building Enclosures
1.
INTRODUCTIDN
1.1
Applicability.
This
procedure
is
applicable for determining
the fugitive volatile organic compoundzmaterials
(VOGM)
emissions
from a building enclosure
(BE).
It is intended to be used as
a
segment in the development of liquid/gas
or gas/gas protocols for
determining VOGN capture efficiency
(CE)
for surface coating and
printing
operations.
1.2
Principle.
The total amount of fugitive
VOGM
emissions
(FB)
from the BE is calculated as the sum of the products of the VOGM
content
(CFJ)
of each fugitive emissions point,
its flow rate
(QF~)’
and time
(TF).
1.3
Measurement Uncertainty.
The measurement uncertainties are
estimated for each fugitive emissions point as
follows:
QF3
=
±5.0percent and
CF3
=
±5.0percent.
Based on these numbers, the
probable uncertainty for
FB
is estimated at about ±11.2percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.
1.5
Notes.
Because
this
procedure
is
often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations
(percent,
ppm)
are by
volume,
unless otherwise noted.
2.
APPARATUS AND REAGENTS
2.1
Gas VOGN
Concentration.
A
schematic
of
the
measurement
system is shown in Figure
1.
The main components are described
below:
2.1.1
Sample Probe.
Stainless steel,
or equivalent.
The probe
shall
be
heated
to
prevent
VOG~condensation.

584
2.1.2
Calibration Valve Assembly.
Three—way valve assembly at
the outlet of sample probe to direct the zero and calibration
gases to the analyzer.
Other methods, such as quick—connect
lines, to route calibration gases to the outlet of the sample
probe are acceptable.
2.1.3
Sample Line.
Stainless steel
or Teflon tubing to
transport the sample gas to the analyzer.
The sample line must
be heated to prevent condensation.
2.1.4
Sample Pump.
A leak-free pump,
to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components
of the
pump that contact the gas stream shall be constructed of
stainless steel
or Teflon.
The sample pump must be heated to
prevent condensation.
-
2.l.S
Sample Flow Rate Control.
A sample flow rate control
valve and rotameter,
or equivalent,
to maintain a constant
-
sampling rate within 10 percent.
The flow rate control valve and
rotameter must be heated to prevent condensation.
A control
valve
may
also
be
located
on
the sample pump bypass loop to
assist
in
controlling
the
sample
pressure and flow rate.
2.1.6
Sample Gas Manifold.
Capable of diverting a portion of
the sample gas stream to the flame ionization analyzer
(FIA),
and
the remainder to the
bypass discharge vent.
The manifold
components shall be constructed of stainless steel or
Teflon.
If
emissions are to be measured at multiple locations, the
measurement
system shall be designed to use separate sampling
probes,
lines, and pumps for each measurement location and a
common sample gas manifold
and
FIA.
The sample gas manifold must
be heated to prevent condensation.
2.1.7
Organic Concentration
Analyzer.
An FIA with a span value
of
1.S
times the
expected concentration
as
propane; however,
other span values may
be used
if
it can
be demonstrated that
they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration
Drift.
Less
than
±3.0percent of the span
value.
2.1.7.3
Calibration Error.
Less than ±5.0percent of the
calibration gas value.
2.1.7.4
Response Time.
Less than 30 seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate

585
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values is
one
measurement
value
every
5 seconds.
The device shall be capable of recording
average
values
at
least
once per minute.
2.1.9
Calibration and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required)
are contained in
compressed gas cylinders.
All calibration gases shall be
traceable
to
NIST
standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should provide a recommended shelf
life for each ‘calibration gas cylinder over which the
concentration does not change more than ±2percent from the
certified value.
For calibration gas values not generally
available, alternative methods for preparing calibration gas
mixtures,
such
as
dilution
systems,
may
be used with prior
approval.
-
2.1.9.1
Fuel.
A 40 percent H2/60 percent He or
40
percent
H2/60
percent
N2 gas mixture is recommended to avoid an oxygen
synergism
effect
that
reportedly
occurs
when
oxygen
concentration
varies significantly from a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than
1 ppm of
organic
material
(propane
or carbon equivalent)
or less than 0.1
percent
of the span value, whichever
is greater.
2.1.9.3
FIA
Linearity
Calibration
Gases.
Low-,
mid-,
and
high—range gas mixture standards with nominal propane
concentrations
of
20-30,
4S—SS,
and 70-80 percent of the span
value in air,
respectively.
Other calibration values and other
span values may be used if it can be shown that more accurate
measurements would be achieved.
2.1.10
Particulate Filter.
An in-stack or an out-of-stack glass
fiber filter is recommended if
exhaust
gas particulate loading is
significant.
An out-of—stack filter must be heated to prevent
any condensation unless
it can be demonstrated that no
condensation occurs.
2.2
Fugitive Emissions Volumetric Flow Rate.
2.2.1
Flow Direction Indicators.
Any means of indicating inward
or outward flow,
such as
light plastic film or paper streamers,
smoke
tubes,
filaments, and sensory perception.
2.2.2
Method
2 or 2A Apparatus.
For determining volumetric flow
rate.
Anemometers or similar devices calibrated according to the
manufacturer’s instructions may be used when low velocities are
present.
Vane anemometers
(Young—maximum response propeller),

586
specialized pitots with electronic manometers
(e.g., Shortridge
Instruments
Inc., Airdata Multimeter 860) are commercially
available
with
measurement
thresholds
of
15
and
8
mpm
(50
and
25 fpm),
respectively.
2.2.3
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used if it can be justified.
2.2.4
Method
4 Apparatus and Reagents.
For determining moisture
content,
if necessary.
3.
DETERMINATION
OF VOLUMETRIC
FLOW RATE OF FUGITIVE EMISSIONS
3.1
Preliminary Determinations.
The purpose of this exercise is
to de~erminewhich exhaust points should be measured for
volumetric flow rates and VOGM concentrations.
3.1.1
Forced Draft Openings.
Identify all forced draft
openings.
Determine
the
volumetric
flow
rate
according
to
Method
2.
3.1.2
NDO’s Exhaust Points.
The NDO’s
in the roof of a
fc~ci1itythebuilding or room in which the emission unit
is
located are considered to be exhaust points.
Determine
volumetric flow rate from these NDO’s.
Divide the
cross—sectional area according to
Method
1 using
12 equal areas.
Use the appropriate velocity measurement;devices,
e.g.,
propeller
anemometers.
3.1.3
Other NDO’s.
3.1.3.1
This step
is optional.
Determine the exhaust flow rate,
including that of the control device,
from the enclosure and the
intake air flow rate.
If the exhaust flow rate divided by the
intake air flow rate
is greater than
1.1,
then all other NDO’s
are not considered to be significant exhaust points.
3.1.3.2
If
the option above is not taken, identify all other
NDO’s and other potential points through which fugitive emissions
may escape the enclosure.
Then use the following criteria to determine whether flow rates
and
VOGN
concentrations need to be measured:
3.1.3.2.1
Using the appropriate flow direction indicator,
determine the flow direction.
An NDO with zero or inward flow is
not an exhaust point.
3.1.3.2.2
Measure the outward volumetric
flow rate from the
remainder
of
the
NDO’s.
If
the
collective
flow rate
is
2
percent,
or less,
of the flow rate from Sections 3.1.1 and 3.1.2,

587
then these NDO’s,
except those within two equivalent diameters
(based
on
NDO
opening) from aVO
sourcc~emittingpoint, may be
-considered to be non-exhaust points.
3.1.3.2.3
If the percentage calculated
in Section 3.1.3.2.2 is
greater than
2 percent, those NDO’s -(except those within two
equivalent diameters from
~VOG~
2ourcc~emittinqpoint) whose
volumetric flow rate total
2 percent of the flow rate from
Sections
3.1.1 and 3.1.2 may be considered as non—exhaust points.
All remaining NDO’s shall be measured for volumetric flow rate
and
VOGN
concentrations during the CE test.
3.1.3.2.4
The’
tester may choose to measure
VOG~
concentrations
at the forced exhaust points and the NDO’s.
If the total VO?M
emissions from the NDO’s are less than
2
percent
of
the
emissions
from the forced draft and roof NDO’s, then these NDO’s may be
eliminated from further consideration.
3.2
Determination of Flow Rates.
3.2.1
Measure the volumetric flow rate at all locations
identified as exhaust points
in Section
3.1.
Divide each exhaust
opening into
9 equal areas for rectangular openings and 8 for
circular openings.
-
3.2.2
Measure the velocity at each site at least once every hour
during each sampling run using Method
2 or 2A,
if applicable,
or
using the low velocity instruments in Section 2.2.2.
4.
DETERMINATION
OF VOG~ CONTENT
OF FUGITIVE EMISSIONS
4.1
Analysis Duration.
Measure the VOG~responses at each
fugitive
emission
point
during the entire test run or,
if
applicable,
while the process
is operating.
If there are
multiple emissions locations, design
a sampling system to allow a
single FIA to be used to determine the VO?l~responses at all
sampling locations.
4.2
Gas VOG~Concentration.
4.2.1
Assemble the sample train as shown in Figure -1.
Calibrate
the FIA and conduct a system check according to the procedures
in
Sections 5.1 and 5.3,
respectively.
4.2.2
Install
the
sample
probe
so
that
the
probe
is centrally
located in the stack, pipe,
or duct,
and is sealed tightly at the
stack port connection.
4.2.3
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach
zero.
Measure the
system response time as the time required for the system to reach

588
the effluent concentration after the calibration valve has been
returned to the effluent sampling position.
4.2.4
Conduct a system check before and a system drift check
after each sampling run according to the procedures
in Sections
5.2
and
5.3.
If
the drift check following a run indicates
unacceptable performanc-e, the run is not valid.
The tester may
elect
to
perform
drift
checks
during
the
run
not
to
exceed
one
drift check per hour.
4.2.5
Verify that the sample lines,
filter, and pump
temperatures
a,re 120
±5°C.
4.2.6
Begin sampling at the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
-
appropriate.
If
multiple emission locations are sampled using
a
single
FIA,
sample at each location for the same amount of time
(e.g.,
2
minutes)
and
continue
to switch from one location to
another for the entire test run.
Be sure that total sampling
time at each location is the same at the end of the test run.
Collectat
least
4 separate measurements from each sample point
during each hour of testing.
Disregard the response measurements
at each sampling location until two times the response time of
the measurement system has elapsed.
Continue sampling for at
least
1 minute and record the concentration measurements.
4.3
Alternative Procedure
The direct interface sampling and
analysis
procedure
described
in Section 7.2 of Method 18 may be
used to determine the gas
VOG~j
concentration.
The system must be
designed to collect and analyze at least one sample every 10
minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero- and the high—range calibration
gases
and
adjust
the
analyzer
calibration
to provide the proper
responses.
Inject the low- and mid-range gases and record the
responses
of the measurement system.
The calibration and
linearity of the system are acceptable
if the responses for all
four gases are within
5 percent of the respective gas values.
If
the performance of the system is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct
a calibration
and linearity check after assembling the analysis system and
after a major change is made to the system.

-
589
-
5.2
Systems Drift Checks.
Select the calibration gas that most
closely approximates the concentration of the captured emissions
for conducting the drift checks.
Introduce the zero and
calibration gas at the calibration valve assembly and verify that
the -appropriate gas flow rate and pressure are present at the
FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained in Section 5.1 is less than
3 percent of the span
value.
Conduct a system drift check at the end of each run.
5.3
System Cl~eck.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
The
performance
of
the
system
is
acceptable
if
the
measurement
system
respox~seis within
5 percent of the value obtained in Section
S.l
for
the
high
range calibration gas.
Conduct
a system check
before each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described
in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within 10
percent.
6.
NOMENCLATURE
=
average measured concentration for the drift check
calibration
gas,
ppm
propane-~
=
average
system
drift
check
concentration
for
zero
concentration gas, ppm propane-~
CFJ
=
corrected average VOG~jconcentration of fugitive
emissions
at
point
j, ppm propane~
=
actual concentration of the drift check
calibration
gas,
ppm
propane-~-;
C3
=
uncorrected average VOGN concentration measured at
-
point
j,
ppm
propane.j~
FB
=
total VOGN content of fugitive emissions from the
building,
kg-ri
K1
=
1.830
x
106
kg/(m3-ppm)-~~
n
=
number of measurement points--;
QF3
=
average effluent volumetric
flow
rate
corrected
to
standard conditions at fugitive emissions point
j,
m3/min--j

590
=
total
duration
of
capture
efficiency
sampling
run,
mm.
7.
CALCULATIONS
7.1
Total
VOGN
Fugitive Emissions From the Building.
n
=
E
CF3
QF3
TF
K1
Eq.
1
j=1
-
7.2
VOGM Concentration of the Fugitive Emissions at Point
j.
CFJ
=
(C3
-
CDQ)
CH_____
-
Eq.
2
CDH~CDQ
Procedure F.1
Fugitive VOGN Emissions from Temporary Enclosures
1.
INTRODUCTION
-
1.1
Applicability.
This
procedure
is
applicable
for
determining
the fugitive volatile organic compound~materials (VOGM)
emissions
from a temporary total enclosure
(TTE).
It is intended to be
used as a segment in the development of liquid/gas or gas/gas
protocols for determining VOG~capture efficiency
(CE)
for
surface coating and printing operations.
1.2
Principle.
The amount of fugitive
VOGN
emissions
(F) from
the TTE
is calculated as the sum of the products of the
VOGM
content
(CFI), the flow rate
(QF3),
and the sampling time
(TF)
from
each fugitive emissions point.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties
are
estimated
for
each fugitive emission point as
follows:
Q~
±S.S
percent
and
CF3
=
±5.0percent.
Based on
these numbers, the probable uncertainty for F
is estimated at
about ±7.4percent.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least
8 hours, unless otherwise approved.
1.5
Notes.
Because
this
procedure
is often applied in highly
explosive areas, caution and care should be exercised in choosing
appropriate
equipment
and
installing
and
using
the
equipment.
Mention of trade names or company products does not constitute
endorsement.
All
gas
concentrations
(percent,
ppm)
are
by
volume,
unless otherwise noted.
2.
APPARATUS AND REAGENTS

591
2.1
Gas
VOGi~
Concentration.
A schematic of the measurement
system is shown
in Figure
1.
The main components are described
below:
2.1.1
Sample Probe.
Stainless steel,
or equivalent.
The probe
shall be heated to prevent
VOG~
condensation.
2.1.2
Calibration Valve Assembly.
Three-way valve assembly at
the outlet of sample probe to direct the zero and calibration
gases to the analyzer.
Other methods,
such as quick—connect
lines,
to
route
calibration
gases
to
the
outlet
of
the
sample
probe are acceptable.
2.1.3
Sample Line.
Stainless steel or Teflon tubing to
transport
the
sample
gas
to
the
analyzer.
The
sample
line
must
be
heated
to
prevent
condensation.
2.1.4
Sample Pump.
A leak-free pump,
to pull the sample gas
through the system at a flow rate sufficient to minimize the
response time of the measurement system.
The components
of the
pump
that
contact
the
gas
stream
shall
be constructed of
stainless steel or Teflon.
The sample pump must be heated to
prevent condensation.
2.1.5
Sample
Flow
Rate
Control.
A
sample
flow
rate
control
valve and rotameter,
or equivalent,
to maintain a constant
sampling
rate
within
10
percent.
The
flow
control
valve
and
rotameter must be heated to prevent condensation.
A control
valve
may
also
be
located
on
the
sample
pump
bypass
loop
to
assist in controlling the sample pressure and flow rate.
2.1.6
Sample
Gas
Manifold.
Capable
of
diverting
a
portion
of
the sample gas stream to the flame ionization analyzer
(FIA), and
the remainder to the bypass discharge vent.
The manifold
components
shall be constructed of stainless steel or Teflon.
If
emissions are to be measured at multiple locations,
the
measurement system shall be designed to use separate sampling
probes1
lines, and pumps for each measurement location and a
common sample gas manifold and FIA.
The sample gas manifold and
connecting
lines to the FIA must be heated to prevent
condensation.
2.1.7
Organic Concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however,
other span values may be used if it can be demonstrated that they
would provide more accurate measurements.
The system shall be
capable of meeting or exceeding the following specifications:
2.1.7.1
Zero Drift.
Less than ±3.0percent of the span value.
2.1.7.2
Calibration Drift.
Less than ±3.0percent of the span
value.

592
2.1.7.3
Calibration Error.
Less than ±5.0
percent
of the
calibration gas value.
2.1.7.4
Response
Time.
Less
than
30
seconds.
2.1.8
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values
is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.1.9
Calibration
and Other Gases.
Gases used for calibration,
fuel,
and combustion air
(if required)
are contained in
compressed gas cylinders.
All calibration gases shall be
traceable to NIST standards and shall be certified by the
manufacturer to ±1percent of the tag value.
Additionally, the
manufacturer of the cylinder should
provide a recommended shelf
life for each
calibration
gas
cylinder
over
which
the
concentration does not change more than ±2
percent from the
certified value.
For calibration gas values not
generally
available,
alternative methods for preparing calibration gas
mixtures,
such as dilution systems, may be used with prior
approval.
2.1.9.1
Fuel.
A
40
percent
H2/60
percent
He
or
40
percent
H2/60
percent
N2 gas mixture is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies significantly from
a mean value.
2.1.9.2
Carrier Gas.
High purity air with less than lppm of
organic material
(as propane or carbon equivalent)
or less than
0.1 percent of the span value, whichever is greater.
2.1.9.3
FIA Linearity Calibration Gases.
Low-, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
45-55,
and 70—80 percent of the span
value
in
air,
respectively.
Other
calibration
values
and
other
span values may be used if
it can be shown that more accurate
measurements would be achieved.
2.1.10
Particulate Filter-.
An in—stack or an out—of-stack glass
fiber filter is recommended if exhaust gas particulate loading is
significant.
An out-of-stack filter must be heated to prevent
any condensation unless it can be demonstrated that no
condensation occurs.
2.2
Fugitive Emissions Volumetric Flow Rate.

593
2.2.1
Method
2
or
2A
Apparatus.
For
determining
volumetric
flow
rate.
2.2.2
Method
3 Apparatus and Reagents.
For determining
molecular weight of the gas stream.
An estimate of the molecular
weight of the gas stream may be used
if it can be justified.
2.2.3
Method
4 Apparatus and Reagents.
For determining moisture
content,
if necessary.
2.3
Temporary Total Enclosure.
The criteria for designing a TTE
are discussed,in Procedure
T.
3.
DETERMINATION OF VOLUMETRIC FLOW RATE OF FUGITIVE EMISSIONS
3.1
Locate all points where emissions are exhausted from the
TTE.
Using Method
1,
determine the sampling points.
Be sure to
check each site for cyclonic or swirling flow.
3.2
Measure the velocity at each sampling site at least once
every hour during each sampling run using Method
2 or 2A.
4.
DETERMINATION OF VOGM CONTENT OF FUGITIVE EMISSIONS
4.1
Analysis Duration.
Measure the VOG~responses at each
fugitive emission point during the entire test run or,
if
applicable, while the process is operating.
If there are
multiple emission locations, design a sampling system to allow a
single FIA to be used to determine the VOC~responses at all
sampling locations.
4.2
Gas VOGM Concentration.
4.2.1
Assemble the sample train as shown in Figure
1.
Calibrate
the FIA and conduct
a system check according to the procedures
in
Sections 5.1 and 5.3, respectively.
4.2.2
Install the sample probe so that the probe
is centrally
located
in
the
stack,
pipe,
or
duct,
and
is
sealed
tightly
at
the
stack port connection.
4.2.3
Inject zero gas at the calibration valve assembly.
Allow
the measurement system response to reach zero.
Measure the
system response time as the time required for the system to reach
the effluent concentration after the calibration valve has been
returned to the effluent sampling position.
4.2.4
Conduct a system check before and a system drift check
after each sampling run according to the procedures
in Sections
5.2 and
5.3.
If the drift check following a run indicates
unacceptable performance,
the run
is not valid.
The tester may

594
elect to perform system drift checks during the run not to exceed
one drift check per hour.
4.2.5
Verify that the sample lines,
filter, and pump
temperatures are 120 ±5°C.
-
4.2.6
Begin sampling at the start of the test period and
continue to sample during the entire run.
Record the starting
and ending times and any required process information as
appropriate.
If multiple emission locations are sampled using
a
single FIA,
sample at each location for the same amount of time
(e.g.,
2 minut~es) and continue to switch from one location to
another for the entire test run.
Be sure that total sampling
time at each location is the same at the end of the test run.
Colleet
at
least
4
separate
measurements
from
each
sample
point
during each hour of testing.
Disregard the response measurements
at each sampling location until two times the response time of
the measurement system has elapsed.
Continue sampling for at
least
1 minute and record the concentration measurements.
4.3
Background Concentration.
4.3.1
Determination of VOG~Background Concentration.
4.3.1.1
Locate all NDO’s of the TTE.
A sampling point shall be
centrally located outside of the TTE at
4
equivalent diameters
from each NDO,
if possible.
If there are more than
6 NDO’s,
choose
6 sampling points evenly spaced among the NDO’s.
4.3.1.2
Assemble the sample train as shown
in Figure
2.
Calibrate the FIA and conduct a system check according to the
procedures
in Sections 5.1 and 5.3.
4.3.1.3
Position the probe at the sampling location.
4.3.1.4
Determine the response time,
conduct the system check
and sample according to the procedures described in Sections
4.2.3 to 4.2.6.
4.4
Alternative Procedure.
The direct interface sampling and
analysis procedure described
in Section 7.2 of Method
18 may be
used to determine the gas
VOGN
concentration.
The system must be
designed
to
collect
and
analyze
at
least
one
sample
every
10
minutes.
5.
CALIBRATION AND QUALITY ASSURANCE
-
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the
FIA
and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the

-
59S
-
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero- and the high—range calibration
gases
and
adjust
the
analyzer
calibration
to
provide
the
proper
responses.
Inject the low— and mid—range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable if the responses for all
four gases are within
5 percent of the respective gas values.
If
the performance of the system is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct a calibration
and linearity check after assembling the analysis system and
after a major change is made to the system.
5.2
Systems Drift Checks.
Select the calibration gas
concentration that most closely approximates that of the fugitive
gas emissions to conduct the
drift checks.
Introduce the zero
and calibration gas at the calibration valve assembly and verify
that the appropriate gas flow rate and pressure are present
at
the FIA.
Record the measurement system responses to the zero and
calibration gases.
The performance of the system is acceptable
if the difference between the drift check measurement and the
value obtained
in Section 5.1 is less than
3 percent of the span
value.
-
Conduct a system drift check at the end of each run.
5.3
System Check.
Inject the high range calibration gas at the
inlet of the sampling probe and record the response.
The
performance
of the system is acceptable
if the-measurement system
response
is within
5 percent of the value obtained in Section 5.1
for the high range calibration gas.
-
Conduct a system check
before each test run.
5.4
Analysis Audit.
Immediately before each test analyze an
audit cylinder as described in Section 5.2.
The analysis audit
must agree with the audit cylinder concentration within
10
percent.
6.
NOMENCLATURE
A1
=
area of NDO
i,
ft2--j
AN
=
total area of all NDO’s
in the enclosure,
ft2-~
C81
=
corrected average
VOGN
concentration of background
emissions at point
i, ppm propane--i
-
CB
=
average background concentration, ppm propane-~
CDH
=
average measured concentration for the drift check
calibration gas, ppm propane-~
C~
=
average system drift check concentration for zero
concentration gas, ppm propane-rj

596
CF3
=
corrected average VOGN concentration of fugitive
emissions
at
point
j, ppm propane--j
=
actual concentration of the drift check
calibration gas, ppm propane--j
C1
=
uncorrected average background
VOG~.
concentration
measured at point
i, ppm propane--:
C3
=
uncorrected average
VOG~
concentration measured at
point
j, ppm propane-a
G
=
total VOGM content
of captured emissions,
kg--j
K1
=
1.830 x 10~kg/(m3-ppm)~
n
=
number of measurement points--j
=
average effluent volumetric flow rate corrected to
standard conditions
at fugitive emissions point
j,
m3/min~-j
TF
=
total duration of fugitive emissions sampling run,
-
mm.
7.
CALCULATIONS
7.1
Total VOGN Fugitive Emissions.
n
F
=
E
(CFJ
C13
)
QFJ
TF
K1
Eq.
1
j=1
7.2
VOGN
Concentration of the Fugitive Emissions at Point
j.
CFJ
=
(C3
-
CD()
CH
Eq.
2
CDQ
7.3
Background VOGI~Concentration at Point
i.
C131
=
(C1
-
CDO)
CH
Eq.
3
CDH
CDQ
7.4
Average Background Concentration.
n
E
C13
A1
CB
= i=l
Eq.
S
nAN

597
NOTE:
If the concentration at each point is within 20 percent of
the average concentration of all points, the terms
“A1” and “AN”
may be deleted from Equation 4.
Procedure L
-
VOGN Input
1.
INTRODUCTION
1.1
Applicability.
This procedure is applicable for determining
the input of volatile organic compound~materials (VOGM).
It is
intended to be used as a segment in the development of liquid/gas
protocols for,determining
VOGN
capture efficiency
(CE)
for
surface coating and printing operations.
1.2
Principle.
The amount of VOGN introduced to the process
(L)
is the sum of the products of the weight
(W)
of each
VOGN
containing liquid
(ink,
paint,
solvent,
etc.)
used and its VOG~
content
(V).
A sample of each VOG~containing liquid is analyzed
with a flame ionization analyzer
(FIA)
to determine V.
1.3
Estimated Measurement Uncertainty.
The measurement
uncertainties are estimated for each
VO?~
containing liquid as
follows:
W
±2.0percent and V
=
±12.0percent.
Based on these
numbers, the probable uncertainty for L
is estimated at about
±12.2percent for each
VOG~
containing liquid.
1.4
Sampling Requirements.
A capture efficiency test shall
consist of at least three sampling runs.
The sampling time for
each run should be at least 8 hours, unless otherwise approved.
1.5
Notes.
Because this procedure
is often applied in highly
explosive areas,
caution and care should be exercised in choosing
appropriate equipment and installing and using the equipment.
Mention of trade names or company products does not constitute
endorsement.
All gas concentrations
(percent,
ppm)
are by
volume,
unless otherwise noted.
2.
APPARATUS AND REAGENTS
2.1
Liquid Weight.
2.1.1
Balances/Digital Scales,
To weigh drums of
VOGN
containing liquids to within 0.2 lb.
2.1.2
Volume Measurement Apparatus
(Alternative).
Volume
meters,
flow meters, density measurement equipment,
etc.,
as
needed to achieve same accuracy as direct weight measurements.
2.2
VO?~ Content
(Flame Ionization Analyzer Technique).
The
liquid sample analysis system is shown
in Figures
1 and
2.
The
following equipment is required:

-
598
2.2.1
Sample Collection Can.
An appropriately sized metal can
to be used to collect
VOGL~
containing materials.
The can must be
constructed
in such
a way that it can be grounded to the coating
container.
2.2.2
Needle Valves.
To control gas flow.
2.2.3
Regulators.
For carrier gas and calibration gas
cylinders.
2.2.4
Tubing.
Teflon or stainless steel tubing with diameters
and lengths determined by connection requirements of equipment.
The tubing be?ween the sample oven outlet and the
FIA
shall be
heated to maintain a temperature of
120 ±5°C.
2.2.5~ Atmospheric Vent.
A tee and 0- to 0.5-liter/mm
rotameter
placed in the sampling line between the carrier gas cylinder and
the
VOGM
sample vessel to release the excess carrier gas.
A
toggle valve placed between the tee and the rotameter facilitates
leak tests of the analysis system.
2.2.6
Thermometer.
Capable of measuring the temperature of the
hot water bath to within 1°C.
2.2.7
-
Sample Oven.
Heated enclosure,
containing calibration gas
coil heaters, critical orifice, aspirator,
and other liquid
sample analysis components,
capable of maintaining a temperature
of 120 ±5°C.
-
2.2.8
Gas Coil Heaters.
Sufficient lengths of stainless steel
or Teflon tubing to allow zero and calibration gases to be heated
to the sample oven temperature before entering the critical
orifice or aspirator.
2.2.9
Water Bath.
Capable of heating and maintaining a sample
vessel temperature of
100 ±5°C.
2.2.10
Analytical Balance.
To measure ±0.001 g.
2.2.11
Disposable
Syringes.
2—cc or S—cc.
2.2.12
Sample Vessel.
Glass,
40—ml septum vial.
A separate
vessel
is needed for each sample.
2.2.13
Rubber Stopper.
Two-hole stopper to accommodate 3.2-mm
(1/8-in.)
Teflon tubing, appropriately sized to fit the opening
of the sample vessel.
The rubber stopper should be wrapped
in
Teflon tape to provide a tighter seal and to prevent any reaction
of the sample with the rubber stopper.
Alternatively,
any
leak—free closure fabricated of non—reactive materials and
accommodating the necessary tubing fittings may be used.

599
2.2.14
Critical Orifices.
Calibrated critical orifices capable
of providing constant flow rates from 50 to 250 mi/mm
at known
pressure drops.
Sapphire orifice assemblies
(available from
O’Keefe Controls Company) and glass capillary tubing have been
found to be adequate for this application.
2.2.15
Vacuum Gauge.
0- to 760-mm
(0- to 30-in.)
Hg U-Tube
manometer or vacuum gauge.
2.2.16
Pressure Gauge.
Bourdon gauge capable of measuring the
maximum air pressure at the aspirator inlet
(e.g.,
100 psig).
2.2.17
Aspirator.
A device capable of generating sufficient
vacuum at the sample vessel to create critical flow through the
calibrated orifice when sufficient air pressure is present at the
aspirator
inlet.
The aspirator must also provide sufficient
sample pressure to operate the
FIA.
The sample is also mixed
with the dilution gas within the aspirator.
2.2.18
Soap Bubble Meter.
Of an appropriate size to calibrate
the critical orifices in the system.
2.2.19
Organic Concentration Analyzer.
An FIA with a span value
of 1.5 times the expected concentration as propane; however other
span values may be used if
it can be demonstrated that they would
provide more accurate measurements.
The system shall be capable
of meeting or exceeding the following specifications:
2.2.19.1
Zero Drift.
Less than ±3.0percent of the span value.
2.2.19.2
Calibration Drift.
Less than ±3.0percent of span
value.
2.2.19.3
Calibration Error.
Less than ±S.0percent of the
calibration gas value.
2.2.20
Integrator/Data Acquisition System.
An analog or digital
device or computerized data acquisition system used to integrate
the FIA response or compute the average response and record
measurement data.
The minimum data sampling frequency for
computing average or integrated values is one measurement value
every
5 seconds.
The device shall be capable of recording
average values at least once per minute.
2.2.21
Chart Recorder
(Optional).
A chart recorder or similar
device
is recommended to provide a continuous analog display of
the measurement results during the liquid sample analysis.
2.2.22
Calibration and Other Gases.
For calibration,
fuel,
and
combustion air
(if required)
contained in compressed gas
cylinders.
All calibration gases shall be traceable to NIST
standards and shall be certified by the manufacturer to ±1

600
percent of the tag value.
Additionally, the manufacturer of the
cylinder should provide a recommended shelf-life for each
calibration gas cylinder over which the concentration does nor
change more than ±2
percent from the certified value.
For
calibration gas values not generally available,
alternative
methods for preparing calibration gas mixtures, such as dilution
systems, may be used with prior approval.
2.2.22.1
Fuel.
A 40 percent H2/60 percent He
or 40 percent H2/60
percent
N2 gas mixture
is recommended to avoid an oxygen
synergism effect that reportedly occurs when oxygen concentration
varies signifjcantly from a mean value.
2.2.22.2
Carrier Gas.
High purity air with less than
1 ppm of
organic material
(as propane)
or less than 0.1
percent of the
span value, whichever
is greater.
2.2.22.3
FIA Linearity Calibration Gases.
Low-, mid-,
and
high—range gas mixture standards with nominal propane
concentrations of 20-30,
4S-SS,
and 70—80 percent of the span
value in air, respectively.
Other calibration values and other
span values may be used
if
it can be shown that more accurate
measurements would be achieved.
2.2.22.4
System Calibration Gas.
Gas mixture standard
containing propane in
air, approximating the undiluted VOGM
concentration expected for the liquid samples.
3.
DETERMINATION OF LIQUID INPUT WEIGHT
3.1
Weight Difference.
Determine the amount of material
introduced to the process as the weight difference of the feed
material before and after each sampling run.
In determining the
total
VOG~
containing liquid usage, account for:
(a) the initial
(beginning)
VOG~
containing liquid mixture;
(b)
any solvent added
during the test run;
(c)
any coating added during the test run;
and
(d) any residual VOG~containing liquid mixture remaining
at
the end of the sample run.
3.1.1
Identify all points where
VO?M
containing liquids are
introduced to the process.
To obtain an accurate measurement of
VOGM
containing liquids,
start with an empty fountain
(if
applicable).
After completing the run,. drain the liquid in the
fountain back into the liquid drum
(if possible),
and weigh the
drum again.
Weigh the VOG~containing liquids to ±0.5percent of
the total weight
(full)
or ±0.1percent of the total weight of
VOGM containing liquid used during the sample run, whichever is
less.
If the residual liquid cannot
be returned to the drum,
drain the fountain into a preweighed empty drum to determine the
final weight of the liquid.

601
-
3.1.2
If it is not possible to measure a single representative
mixture, then weigh the various components separately
(e.g.,
if
solvent is added during the sampling run, weigh the solvent
before it
is added to the mixture).
If
a fresh drum of
VOGM
containing liquid is needed during the run,
then weigh both the
empty drum and fresh drum.
3.2
Volume Measurement
(Alternative).
If direct weight
measurements are not feasible,
the tester may use volume meters
and flow rate meters
(and density measurements)
to determine the
weight of liquids used if it can be demonstrated that the
technique produces results equivalent to the direct weight
measurements.
If a single representative mixture cannot be
measured, measure-the components separately.
4.
DETERMINATION OF VOGM CONTENT
IN INPUT LIQUIDS
4.1
Collection of Liquid Samples.
4.1.1
Collect a lOO-ml or larger sample of the VOGM containing
liquid mixture at each application location at the beginning and
end of
-each test run.
A separate sample should be taken of each
VOG~
containing liquid added to the application mixture-during
the test run.
If a fresh drum is needed during the sampling run,
then obtain a sample from the fresh drum.
4.1.2
When collecting the sample,
ground the sample container to
the coating drum.
Fill the sample container as close to the rim
as possible to minimize the amount of headspace.
4.1.3
After the sample is collected,
seal the container so the
sample cannot leak out or evaporate.
4.1.4
Label the container to identify clearly the contents.
4.2
Liquid Sample VOG~Content.
4.2.1
Assemble the liquid VOGM
content analysis system as shown
in Figure
1.
4.2.2
Permanently identify all of the critical orifices that may
be used.
Calibrate each critical orifice under the expected
operating conditions
(i.e.,
sample vacuum and temperature)
against a volume meter as described in Section 5.3.
4.2.3
Label and tare the sample vessels
(including the stoppers
and caps) and the syringes.
4.2.4
Install an empty sample vessel and perform a leak test of
the system.
Close the carrier gas valve and atmospheric vent and
evacuate the sample vessel to 250 mm
(10 in.) Hg absolute or less
using the aspirator.
Close the toggle valve at the inlet to the

-
602
-
aspirator and observe the vacuum for at least one minute.
If
there
is any change in the sample pressure, release the vacuum,
adjust or repair the apparatus as necessary and repeat the leak
test.
4.2.5
Perform the analyzer calibration and linearity checks
according to the procedure in Section 5.1.
Record the responses
to each of the calibration gases and the back—pressure setting of
the FIA.
4.2.6
Establish the appropriate dilution ratio by adjusting the
aspirator air supply or substituting critical orifices.
Operate
the aspirator’at a vacuum of at least 25 mm
(1
in.) Hg greater
than the vacuum necessary to achieve critical flow.
Select the
dilution ratio so that the maximum response of the FIA to the
sample does not exceed the high—range calibration gas.
-
4.2.7
Perform system calibration checks at two levels by
introducing compressed gases at the inlet to the sample vessel
while the aspirator and dilution devices are operating.
Perform
these checks using the carrier gas
(zero concentration)
and the
system calibration gas.
If the response to the carrier gas
exceeds ±0.5percent of span,
clean or repair the apparatus and
repeat the check.
Adjust the dilution ratio as necessary to
achieve the correct response to the upscale check,
but do not
adjust the analyzer calibration.
Record the identification of
the orifice, aspirator air supply pressure, FIA back—pressure,
and the responses of the FIA to the carrier and system
calibration gases.
4.2.8
After completing the above checks,
inject the system
calibration gas for approximately 10 minutes.
Time the exact
-
duration of the gas injection using a stopwatch.
Determine the
area under the FIA response curve and calculate the system
response factor based on the sample gas flow rate,
gas
concentration,
and the duration of the injection as compared to
the integrated response using Equations
2 and
3.
4.2.9
Verify that the sample oven and sample line temperatures
are 120 ±5°Cand that the water bath temperature
is 100 ±S°C.
4.2.10
Fill a tared syringe with approximately
1 g of the
VO?M
containing liquid and weigh it.
Transfer the liquid to a tared
sample vessel.
Plug the sample vessel to minimize sample loss.
Weigh the sample vessel containing the liquid to determine the
amount of sample actually received.
Also,
as a quality control
check, weigh the empty syringe to determine the amount of
material delivered.
The two coating sample weights should agree
within ±0.02 g.
If not, repeat the procedure until an acceptable
sample is obtained.

-
603
4.2.11
Connect the vessel to the analysis system.
Adjust the
aspirator supply pressure to the correct value.
Open the valve
on the carrier gas supply to the sample vessel and adjust it to
provide a slight excess flow to the atmospheric vent.
As soon
as
the initial response of the FIA begins to
decrease,
immerse the
sample vessel in the water bath.
(Applying heat to the sample
vessel too soon may cause the FID response to exceed the
calibrated range of the instrument,
and thus invalidate the
analysis.)
4.2.12
Continuously measure and record the response of the FIA
until all of the volatile material has been evaporated from the
sample and the instrument response has returned to the baseline
(i.e., response less than 0.5 percent of the span value).
Obserye the aspirator supply pressure,
FIA back—pressure,
atmospheric vent,
and other system operating parameters during
the run; repeat the analysis procedure if any of these parameters
deviate from the values established during the system calibration
checks in Section 4.2.7.
After
each sample perform the drift
check described in Section 5.2.
If the drift check results are
acceptable,
calculate the VOGN content of the sample using the
equations in Section
7.
Integrate the area under the FIA
response curve, or determine the average concentration response
and the duration of sample analysis.
5.
CALIBRATION AND QUALITY ASSURANCE
5.1
FIA Calibration and Linearity Check.
Make necessary
adjustments to the air and fuel supplies for the FIA and ignite
the burner.
Allow the FIA to warm up for the period recommended
by the manufacturer.
Inject a calibration gas into the
measurement system and adjust the back—pressure regulator to the
value required to achieve the flow rates specified by the
manufacturer.
Inject the zero- and the high-range calibration
gases and adjust the
analyzer calibration to provide
the
proper
responses.
Inject the low— and mid—range gases and record the
responses of the measurement system.
The calibration and
linearity of the system are acceptable
if the responses for all
four gases are within
5 percent of the respective gas values.
If
the performance of the system is not acceptable, repair or adjust
the system and repeat the linearity check.
Conduct
a calibration
and linearity check after assembling the analysis system and
after a major change
is made to the system.
5.2
Systems Drift Checks.
After each sample, repeat the system
calibration checks in Section 4.2.7 before any adjustments to the
FIA or measurement system are made.
If the zero or calibration
drift exceeds ±3percent of the span value,
discard the result
and repeat the analysis.
5.3
Critical Orifice Calibration.

604
5.3.1
Each critical orifice must be calibrated at the specific
operating conditions that it will be used.
Therefore,
assemble
all components of the liquid sample analysis system as shown in
Figure
3.
A stopwatch is also required.
5.3.2
Turn on the sample oven,
sample
line,
and water bath
heaters and allow the system to reach the proper operating
temperature.
Adjust the aspirator to
a vacuum of 380 mm
(15
in.)
Hg vacuum.
Measure the time required for one soap bubble to move
a known distance and record barometric pressure.
5.3.3
Repeat the calibration procedure at
a vacuum of 406 mm
(16
in.) Hg and a?
25-mm
(i-in.)
Hg intervals until three consecutive
determinations provide the same flow rate.
Calculate the
critical flow rate for the orifice in ml/min at standard
conditions.
Record the vacuum necessary to achieve critical
flow.
6.
NOMENCLATURE
AL
=
area under the response curve of the liquid
sample,
area count-~j
A13
=
area under the response curve of the calibration
gas, area count-;.
-
C13
=
-
actual concentration of system calibration gas,
ppm propane--j
-
K
=
1.830 x i0~g/(ml—ppm)~-j
L
=
total VOGN content of liquid input,
kg--i
ML
=
mass of liquid sample delivered to the sample
vessel, g--~
q
=
flow rate through critical
orifice, ml/min-~
RF
=
liquid analysis system response factor,
g/area
count,-;
T13
=
total
gas- injection time for system calibration
gas
during integrator calibration, min-~
VF~
=
final VOG~fraction of
VOGN
containing liquid
j--~
V1~
=
initial VOG~fraction of VOG~containing liquid
j-;-~~
VAJ
=
VOGM fraction of VOGM containing
liquid
j
added
during the run--j
-

605
V
=
VOG~
fraction of liquid sample~
WF3
=
weight of
VOG~
containing liquid
j
remaining at
end of the run,
kg--i
=
weight of
VOG~i
containing liquid
j
at beginning of
the run, kg~-~
=
weight of
VOGN
containing liquid
j
added during
the run,
kg.
7.
CALCULATIONS
7.1
Total
VOG~
Content of the Input
VOG~
Containing Liquid.
n
n
n
L
=
E
V1~W1~
=
VF3
WF3
+
E
VA3
WAJ
R
Eq.
1
j=l
j=l
j=1
7.2
Liquid Sample Analysis System Response Factor for Systems
Using Integrators, Grams/Area Counts.
RF
=
~gj
Eq.
2
A13
-
7.3
VOG~Content
of the Liquid Sample.
=
A1~
Eq.
3
ML
Procedure T
Criteria for and Verification of a Permanent or
Temporary Total Enclosure
1.
INTRODUCTION
-
1.1
Applicability.
This procedure is used to determine whether
a permanent or temporary enclosure meets the criteria of a total
enclosure.
1.2
Principle.
An enclosure
is evaluated against a set of
criteria.
If the criteria are met and if all the exhaust gases
are ducted to a control device, then the volatile organic
compound5materials
(VOGN)
capture efficiency
(CE)
is assumed to
be 100 percent and CE need not be measured.
However,
if part of
the exhaust gas stream is not ducted to a control device, CE must
be determined.
2.
DEFINITIONS
2.1
Natural Draft Opening
(NDO)
--
Any permanent opening in the
enclosure that remains open during operation of the facility

606
emission unit and is not connected to a duct in which a fan is
installed.
2.2
Permanent Total Enclosure
(PTE)
—-
A permanently installed
enclosure that completely surrounds a~3ourcc of emissionsunit
such that all VOGi~emissions are captured and contained for
discharge through a control device.
2.3
Temporary Total Enclosure
(TTE)
--
A temporarily installed
enclosure that completely surrounds a~~ourcc
of emissionsunit
such that all VOGN emissions are captured and contained for
discharge through ducts that allow for the accurate measurement
of VOGM rates.
3.
cRITERIA OF A TEMPORARY TOTAL ENCLOSURE
3.1
Any NDO shall be at least
4 equivalent opening
diameters
from each VOGN emitting point.
3.2
Any exhaust point from the enclosure shall be at least
4
equivalent duct
or hood diameters from each NDO.
3.3
The total area of all NDO’s shall not exceed
5 percent
of
the surface area of the enclosure’s four walls, floor,
and
ceiling.
3.4
The average facial velocity
(FV)
of air through all NDO’s
shall be at least 3,600 m/hr
(200
fpm).
The direction of air
through all NDO’s shall be into the enclosure.
3.5
All access doors and windows whose areas are not included in
Section
3.3
and
are not included
in the calculation in Section
3.4
shall.be
closed
during routine operation of the
procczoemisSiOn
unit.
4.
CRITERIA OF A PERMANENT TOTAL ENCLOSURE
4.1
Same as Sections 3.1 and 3.3
3.5.
4.2
All VOGI~emissions must be captured and contained for
discharge through
a control device.
5.
PROCEDURE
5.1
Determine the equivalent diameters of the NDO’s and
determine the distances from each
VOG~emitting point to all
NDO’s.
Determine the equivalent diameter of each exhaust duct or
hood and its distance to all NDO’s.
Calculate the distances
in
terms of equivalent diameters.
The number of equivalent
diameters shall be at least 4.

607
-
5.2
Measure the total area
(A1)
of the enclosure and the total
area
(AN)
of all NDO’s of the enclosure.
Calculate the NDO to
enclosure area ratio
(NEAR)
as follows:
NEAR
= AN/Al
The NEAR must be
0.05.
5.3
Measure the volumetric flow rate,
corrected to standard
conditions,
of each gas stream exiting the enclosure through an
exhaust duct or hood using EPA Method
2.
In some cases
(e.g.,
when the building
is the enclosure),
it may be necessary to
measure the volumetric flow rate, corrected to standard
conditions,
of each gas stream entering the enclosure through a
forced makeup air duct using Method
2.
Calculate FV using the
following equation:
FV
=
Q0
Ql)/AN
where:
Q0
=
the sum of the volumetric flow from all gas
streams exiting the enclosure through an exhaust
duct or hood.
=
the sum of the volumetric flow from all gas
streams into the enclosure through
a forced makeup
air duct;
zero,
if there
is no forced makeup air
into the enclosure.
AN
=
total area of all NDO’s
in enclosure.
The FV sh~1lbe at least 3,600 m/hr
(200 fpm).
5.4
Verify that the direction of air flow through all NDO’s
is
inward.
Use streamers,
smoke tubes, tracer gases,
etc.
Strips
of plastic wrapping film have been found to be effective.
Monitor the direction of air flow at intervals of at least 10
minutes for at least
1 hour.
6.
QUALITY ASSURANCE
6.1
The success of this protocol lies in designing the TTE to
simulate the conditions that exist without the TTE,
i.e.,
the
effect of the TTE on the normal flcw patterns around the affected
facilityemission unit or the amount of fugitive
VOG~
emissions
should be minimal.
The TTE must enclose the application
stations,
coating reservoirs,
and all areas from the application
station to the oven.
The oven does not have to be enclosed if
it
is under negative pressure.
The NDO’s of the temporary enclosure
and a fugitive exhaust fan must be properly sized and placed.

-
608
-
6.2.
Estimate the ventilation rate of the TTE that best
simulates the conditions that exist without the TTE,
i.e., the
effect of the TTE on the normal flow patterns around the affected
~-aci1ityemission
unit or the amount of fugitive
VOG~
emissions
should be minimal.
Figure
1 may be used as an aid.
Measure the
concentration
(C6)
and flow rate
(QG)
of the captured gas stream,
specify a safe concentration
(CF)
for the fugitive gas stream,
estimate the CE, and then use the plot in Figure
1 to determine
the volumetric flowrate of the fugitive gas stream (QF)~ A
fugitive
VOGN
emission exhaust fan that has a variable flow
control is desirable.
6.2.1
Monitor the concentration of
VOG~
into the capture device
without the TTE.
To minimize the effect of temporal variation on
the captured emissions,
the baseline measurement should be made
over as
long a time period as practical.
However, the process
conditions must be the same for the measurement
in Section 6.2.3
as they are for this baseline measurement.
This may require
short measuring times for this quality control check before and
after the construction of the TTE.
6.2.2
After the TTE
is constructed, monitor the
VOq~
concentration inside the TTE.
This concentration shall not
continue to increase and must not exceed the safe level according
to OSHA requirements for permissible exposure limits.
An
increase in VOG~concentration indicates poor TTE design or poor
capture efficiency.
-
6.2.3
Monitor the concentration of
VOG~
into the capture device
with the TTE.
To limit the effect of the TTE on the process, the
VOGM
concentration with and without the TTE must be
within ±10
percent.
.If the measurements do not agree,
adjust the
ventilation rate from the TTE until they agree within 10 percent.
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

609
Section 219.Appendix C
Reference Test Methods and Proccdurc3For Air Oxidation Processes
Introduction
This Appendix presents the reference methods and procedures
required for implementing Reasonably Available Control Technology
(RACT).
Methods
and
procedures
are
identified
for
two
types
of
RACT
implementation:
a)
Determination
of VOG~destruction efficiency for evaluating
compliance with the 98 weight percent
VOG~
reduction or 20
ppmv emission limit specified in Sections 215.520 through
21S.527; and
b)
betermination of offgas flowrate, hourly emissions and
stream net heating value for calculating
ThE.
All reference methods identified
in this Appendix refer to the
reference methods specified at 40 CFR 60, Appendix A,
-
incorporated by reference in Section 215.lOS.
VOGM
DESTRUCTION EFFICIENCY DETERMINATION
The following reference methods and procedures are required for
determining compliance with the percent destruction efficiency
specified in Sections 215.520 through 215.527.
a)
Reference Method
1 or lA for selection of the sampling site.
The control device inlet sampling site for determination of
vent stream molar composition or total organic compound
destruction efficiency shall be prior to the inlet of any
control device and after all recovery devices.
b)
Reference
Methods
2,
2A,
2C
or
2D
for
determination
of
the
volumetric
flowrate.
c)
Reference Method
3 to measure oxygen concentration of the
air dilution correction.
The emission sample shall be
corrected to
3 percent oxygen.
d)
Reference Method 18 to determine the concentration of total
organic compounds
(minus methane and ethane)
in the control
device outlet and total organic compound reduction
efficiency of the control device.
TRE
DETERMINATION
-
The following reference methods and procedures are required for
determining the offgas flowrate, hourly emissions,
and the net
heating
value
of
the
gas
combusted
to
calculate
the vent stream
TRE.

610
a)
Reference Method
1 or 1A for selection of the sampling site.
The sampling site for the vent stream flowrate and molar
composition determination prescribed in
(b)
and
(c)
shall be
prior to the inlet of any combustion device, prior to any
post-reactor dilution of the stream with air and prior to
any post—reactor introduction of halogenated compounds into
the vent stream.
Subject to the preceding restrictions on
the sampling site,
it shall be after the final recovery
device.
If any gas stream other than the air oxidation vent
stream is normally conducted through the recovery system of
the affected facility,
such stream shall be rerouted or
turned o~fwhile the vent stream is sampled, but shall be
routed normally prior to the measuring of the initial value
of the monitored parameters for determining compliance with
.the recommended RACT.
If the air oxidation vent stream is
normally routed through any equipment which is not a part of
the air oxidation process as defined in
35
Ill. Adm.
Code
211.122,
such equipment shall be bypassed by the vent stream
while the vent stream is sampled,
but shall not be bypassed
during the measurement of the initial value of the monitored
parameters for determining compliance with Subpart V.
b)
The molar composition of the vent stream shall be determined
using the following methods:
1)
Reference Method
18 to measure the concentration of all
organics,
including those containing halogens, unless
a
-
significant portion of the compounds of interest are
polymeric
(high molecular weight), can polymerize
before analysis or have low vapor pressures,
in which
case Reference Method 25(a)
shall be used.
2)
~ASTM Dl946-67
(reapproved 1977),
incorporated by
reference in Section 215.105, to measure the
concentration of carbon monoxide and hydrogen.
3)
Reference
Method
4
to
measure
the
content
of
water
vapor,
if necessary.
c)
The volumetric flowrate shall be determined using Reference
Method
2,
2A,
2C or 2D,
as appropriate.
d)
The net heating value of the vent stream shall be calculated
using the following equation:
n
H=K
E
CiHi
i=l
Where:

611
H
=
Net heating value of the sample, MJ/scm, where the
net enthalpy per mole of offgas
is based on
combustion at 25°Cand 760 mm Hg, but the standard
temperature for determining the volume
corresponding to one mole is 20°C,as in the
definition of F
(vent stream flowrate)
below.
K
=
Constant, 1.740 x l0~(1/ppm)
(mole/scm)
(MJ/kcal)
where standard temperature for mole/scm is 20°C.
Ci
=
Concentration of sample component
i, reported on a
wet basis,
in ppm,
as measured by Reference Method
18 or ASTM Dl946-67
(reapproved 1977),
incorporated by reference in Section 215.105.
Hi
=
Net heat of combustion of sample component
i,
kcal/mole based on combustion at 25°Cand 760 mm
Hg.
If published values are not available or
cannot be calculated, the heats of combustion of
vent stream components are required to be
determined using ASTM D2382-76, incorporated
by
reference in Section 215.105.
e)
The emission rate of total organic compounds
in
the- process
vent stream shall be calculated using the following
equation:
n
E=K
F
E
CiMi
i=1
Where:
-
E
=
Emission rate of total organic compounds
(minus
methane and ethane)
in the sample in kg/hr--;
K
=
Constant
2.494
x
l0~(1/ppm)
(mole/scm)
(kg/g)
(min/hr),
where standard temperature for
(mole/scm)
is 20°C,-;
Mi
=
Molecular weight
of
sample
component
i
(g/mole)~-;
F
=
Vent stream flowrate (scm/mm),
at a
standard
temperature of 20°C.
f)
The total vent stream concentration
(by volume)
of compounds
containing halogens
(ppmv, by compound)
shall be summed from
the individual concentrations of compounds containing
halogens which were measured by Reference Method l8~
(Source:
Amended at
Ill.
Reg.
______,
effective
____________

612
Section 2l9.Appendix D
Coefficients for the Total Resource Effectiveness Index
(TRE)
Equation
This Appendix contains values for the total resource
effectiveness index
(TRE)
equation in Subpart V.
If a flow rate falls exactly on the boundary between the
indicated ranges,
the operator shall use the row in which the
flow rate is maximum.
COEFFICI.ENTS FOR TRE EQUATION FOR CHLORINATED
PROCESS
VENT STREAMS WITH
NET HEATING VALUE LESS THAN OR EQUAL TO 3.5 NJ/scm
FLOW RATE
-
(scm/mm)
Mm.
Max.
a
b
c
d
e
f
0.0
13.S
48.73
0.
0.404
—0.1632
0.
0.
13.5
700.
42.35
0.624
0.404
—0.1632
0.
0.0245
700.
1400.
84.38
0.678
0.404
—0.1632
0.
0.0346
1400.
2100.
126.41
0.712
0.404
—0.1632
0.
0.0424
2100.
2800.
168.44
0.747
0.404
—0.1632
0.
0.0490
2800.
3500.
210.47
0.758
0.404
—0.1632
0.
0.0548
COEFFICIENTS FOR TRE EQUATION FOR CHLORINATED PROCESS
VENT STREAMS WITH
NET HEATING VALUE GREATER THAN 3.5 NJ/scm
-
FLOW RATE
(scm/min)
Mm.
Max.
a
b
c
d
e
f
0.
13.5
47.76
0.
—0.292
0.
0.
0.
13.5
700.
41.58
0.605 —0.292
0.
0.
0.0245
700.
1400.
82.84
0.658 —0.292
0.
0.
0.0346
1400.
2100.
123.10
0.691 —0.292
0.
0.
0.0424
2100.
2800.
165.36
0.71S —0.292
0.
0.
0.0490
2800.
3500.
206.62
0.734 —0.292
0.
0.
0.0548
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS
VENT STREAMS WITH
NET HEATING VALUE LESS THAN OR EQUAL TO 0.48 NJ/scm
FLOW RATE
(scm/mm)
Mm.
Max.
a
b
c
d
e
f
0.
13.5
19.05
0.
0.113
—0.214
0.
0.
13.5 13S0.
16.61
0.239
0.113
—0.214
0.
0.0245
1350.
2700.
32.91
0.260
0.113
—0.214
0.
0.0346
2700.
4050.
49.21
0.273
0.113
—0.214
0.
0.0424

613
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS
VENT STREAMS
WITH NET HEATING VALUE GREATER THAN 0.48 AND LESS THAN OR
EQUAL TO 1.9 NJ/scm
FLOW RATE
(scm/min)
Mm.
Max.
a
b
c
d
e
f
0.
13.5
19.74
0.
0.400
—0.202
0.
0.
13.5 1350.
18.30
0.138
0.400
—0.202
0.
0.0245
1350.
2700.
36.28
0.150
0.400
—0.202
0.
0.0346
2700.
4050.
*
54.26
0.158
0.400
—0.202
0.
0.0424
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS
VENT STREAMS
WITH NET HEATING VALUE GREATER THAN 1.9 AND LESS THAN OR
EQUAL TO 3.6 MJ/scm
FLOW RATE
(scm/min)
Mm. Max.
a
b
c
d
e
f
.0
-
13.5
15.24
0.
0.033
0.
0.
0.
13.5 1190.
13.63
0.157
0.033
0.
0.
0.0245
1190.
2380.
26.95
0.171
0.033
0.
0.
0.0346
2380.
3570.
40.27
0.179
0.033
0.
0.
0.0424
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS
VENT STREAMS- WITH
NET
HEATING
VALUE
GREATER
THAN 3.6 MG/scm
FLOW RATE
(scm/mm)
Mm.
Max.
a
b
c
d
e
f
0.
13.5
15.24
0.
0.
0.0090
0.
0.
13.5 1190.
13.63
0.
0.
0.0090
0.0503
0.0245
1190.
2380.
26.95
0.
0.
0.0090
0.0546
0.0346
2380.
3570.
40.27
0.
0.
0.0090
0.0S73
0.0424
(Source:
Amended at
Ill.
Reg.
______,
effective
)

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