ILLINOIS POLLUTION CONTROL BOARD
September
8,
1988
IN THE MATTER OF:
PROPOSED AMENDMENTS TO PART
)
R88-23
211 AND 215, LEAKS FROM
)
SYNTHETIC ORGANIC CHEMICAL
AND POLYMER MANUFACTURING
EQUIPMENT
PROPOSED RULE.
FIRST NOTICE.
ORDER OF THE BOARD
(by J.
D.
Dumelle):
This matter comes before the Board upon
an August 24,
1988,
Joint Proposal filed simultaneously with
a Joint Motion by the
Illinois Environmental Protection Agency (Agency), Amoco Chemical
Company (Amoco), the Dow Chemical Company (Dow), Mobil Chemical
Company,
Inc.
(Mobil), and Stepan Company (Stepan), all of whom
will
be generally referred
to as “Joint Proponents”
or
“Joint
Movants”.
The joint motion requests the Board
to conduct an
expedited rulemaking on the joint proposal.
The Board
is amenable to expediting the rulemaking process
as much as possible consistent with the Administrative Procedure
Act; however, the Board notes that
a
rulemaking proceeding can be
expedited only inasmuch as the proponents and participants
demonstrate
a willingness
to cooperate.
For
its part, the Board
today sends the proposal
to First Notice.
However, due
to the
expedited nature of this proceeding,
the Board takes no position
at this time on the substance of the proposed text.
The Hearing Officer
is directed
to schedule hearings as soon
as practicable.
ORDER
The Board hereby proposes the following amendments to 35
Ill. Adm. Code 211 and 215 for
First Notice publication.
The
Clerk
is directed
to submit these proposed amendments to the
Secretary of State’s Office for publication
in the Illinois
Register.
92—441
—2—
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 B:
DEFINITIONS
Section 211.122
Definitions
“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.
“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
p4pesvalves.
This definition excludes valves which are not
externally regulated,
flanges, and equipment
in heavy liquid
service.
For purposes of Subpart
Q
(35 111.
Adm. Code 215),
this
definition also excludes bleed ports of gear pumps
in polymer
service.
“Control Device”:
For purposes of Subpart
Q,
an enclosed
combustion device, vapor
recovery system, flare,
or closed
container.
0In~~situSampling Systems”:
nonextractive samplers or in—line
samplers.
“Light Liquid”:
Volatile organic material
in the liquid state
which
is not defined
as
a heavy liquid.
“Liquids Dripping”:
Any visible leaking from
a seal including
spraying, misting, clouding and ice formation.
“Pressure Release”:
The emission of materials resulting from
~ystem pressure being greater than set pressure of the pressure
92—442
—3—
relief device.
“Process Unit”:
Components assembled
to produce,
as intermediate
or final products, one or more of the chemicals listed
in
Appendix 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 spare components and technically feasible
bypassing
of components without stopping production are not
process unit shutdowns.
“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
a
uncontaminated sample may then be taken
for testing or analysis.
“Sensor”:
A device
that measures
a physical quantity or the
change
in a physical quantity such as temperature, pressure, flow
rate, pH,
or liquid level.
“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 Appendix
D.
“Zero Volatile Organic Material Emissions”:
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 Section 60.485(c).
(Source:
Amended
at
______
Ill.
Reg.
_______
effective
____________)
92—443
—4—
TITLE
35:
ENVIRONMENTAL PROTECTION
SUBTITLE B:
AIR POLLUTION
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER C:
EMISSIONS STANDARDS AND LIMITATIONS FOR
STATIONARY SOURCES
PART 215
ORGANIC MATERIAL EMISSION STANDARDS AND LIMITATIONS
SUBPART
A:
GENERAL PROVISIONS
Section 215.104
Definitions
The definitions of 35
Iii. Adm.
Code 201
arid 211 apply to this
Part, as well as the definition contained in this Section.
Where
the definition contained
in this Section
is more specific than
that found
in Parts
201 or 211,
it shall take precedence
in
application of this Part.
~
t,4~-~Ve~~e e~g~~emer4~
4r~~J’~e44~t~4d
~t~e
w~e1~
4~
t’~e~
~ef4rie~
~
(Source:
Amended at
_____
Ill. Reg.
___________
effective
_____________).
Section 215.105
Incorporation by Reference
The following materials are incorporated by reference:
a)
American Society for Testing and Materials,
1916 Race
Street, Philadelphia,
PA 19103:
1)
ASTM D 1644—59 Method A
2)
ASTM D 1475—60
3)
ASTM D 2369—73
4)
ASTM D 2879—83
(Approved 1983)
5)
ASTM D 323—82
(Approved 1982)
6)
ASTM D 86—82
(Approved 1982)
7)
ASTM
E 260—73
(Approved 1973),
E 168—67
(Reapproved 1977),
E 169—63
(Reapproved 1981),
E
20
(Approved 1985)
8)
ASTM
D 97—66
9)
ASTM D 1946—67
9 2—444
—5—
10)
ASTM D 2382—76
11)
ASTM 0 2504—83
12)
ASTM D 2382—83
b)
Federal Standard l4la, Method 4082.1
C)
National Fire Codes, National Fire Prevention
Association, Battery March Park,
Quincy, Massachusetts
02269
(1979)
d)
United States Environmental Protection Agency,
Washington,
D.C., EPA—450/2—77—026, Appendix A
(October
1977)
e)
United States Environmental Protection Agency,
Washington,
D.C.,
EPA—450/2—78—051 Appendix A and
Appendix B (December 1978).
f)
Standard Industrial Classification Manual, published by
Executive Office of the President, Office of Management
and Budget, Washington,
D.C.,
1972
g)
40 CFR 60, Appendix
A,
1986
h)
United States Environmental Protection Agency,
Washington D.C.,
EPA—450/2—78—04l.
(Board Note:
The incorporations by reference listed above
contain
no later amendments or editions.)
(Source:
Amended at
_____
Ill.
Reg.
________
effective
______________).
SUBPART
Q:
LEAKS FROM SYNTHETIC ORGANIC CHEMICAL AND POLYMER
MANUFACTURING EQUIPMENT
Section 215.420
Applicability
The provisions of Sections 215.421 through 215.429
of this
subpart shall apply to all plants
in the State of Illinois which
manufacture synthetic organic chemicals and polymers,
except
those located
in any of the following counties:
Will,
McHenry,
Cook, DuPage, Lake, Kane,
Madison, St.
Clair, Macoupin, and
Monroe.
The provisions of Section 215.430 through ~5-438
215.329 shall apply to the counties specifically enumerated
above.
In addition,
if any county
is redesignated as non—attainment by
the USEPA subsequent
to December 31,
1987,
the owner or operator
92—445
—6—
of a plant
located
in
that county shall comply with the
requirements of Sections 215.430
through 2~5748 215.439 upon the
effective date of the redesignation.
(Source:
Amended
at
_____
Ill.
Reg.
_______
effective
_______________
Section 215.430
General Requirements
The owner
or operator of a plant which processes more than 3660
Mg/yr
(4033
tons/year)
gaseous e~and
light liquid volatile
organic material, and whose components are used
to manufacture
the synthetic organic chemicals or polymers listed
in Appendix
0,
shall eo~th~e~
~e&~
ee~4et~a~
~
~
fOf
~
4t~t
~eeef~1~ee
w4~1~
~th4~
S~r~ comply with Sections
215.430
to 215.439.
E~e&~
ee~4ei~
~nd
fep~4f
~
~+i~H ~e
eet~e~e~
fef ~th~ter~e~
The provisions of Sections 215.430
to 215.439 are applicable
to components containing
10 percent or
more by weight volatile organic material as determined by ASTM
method E—l68, E—169
and E—260,
incorporated by reference
in
Section 215.105.
Those components
that are not process unit
components are exempt from Sections 215.430
to 215.439.
A
component shall
be considered
to be leaking
if the volatile
organic material
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 215.105, 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
____________
Section 215.432
Inspection Program for Leaks
The owner
or operator of
a synthetic organic chemical or polymer
manufacturing plant subject
to Section 215.430 through ~5~-438,
215.439,
shall
for the purposes of detecting leaks, conduct
a
component
inspection program utilizing
the test methods specified
in Reference Method 21,
40 CFR 60, Appendix
A (1986),
incorporated
by reference
in Section 215.105, 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 located more
than two meters above permanent worker
access structures
or surfaces;
92—44 6
—7—
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)
are found not to leak for
5
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
3 quarters.
If more
than
2 percent are leaking, then tests are required for
the next
5 quarters.
d)
Observe visually all pump seals weekly.
e)
Test immediately any pump seal
in light liquid service
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 e~e~
components
in heavy liquid service,
is not required.
However,
any
valve which is not externally regulated,
flange, or
p4eee cf e~prt~en~
component
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.
i)
Within
1 hour of its detection,
a weátherp~oof,rëadily
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)
Any component that
is
in vacuum service7
or any pressure
relief devices connected
to an operating flare header or
to
a vapor recovery devices ~e
is exempt from the
monitoring requirements
in this Section.
(Source:
Amended at
_____
Ill.
Reg.
_______
effective
)
92—44
7
—8—
Section 215.435
Report for Leaks
The owner or operator of
a synthetic organic chemical
or polymer
manufacturing plant subject
to Section 215.430 through ~S7438
215.439 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 215.432 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 and
in gas service inspected and the number and
percentage of valves
found leaking.
b)
Submit
a signed statement with the report attesting that
all monitoring and repairs were preformed as required
under Section 215.430 through 215.436.
(Source:
Amended at
_____
Ill.
Reg.
_______
effective
____________).
Section 215.437
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 e2pen—ended valves and which serve
as a sampling connection shall be e4p~e~w4~he e4e~ed
~~ge
~
Of
e~cse~
vera ~ys~em controlled
such that:
1)
A closed purge system or closed vent system
shall
return Pt~fge~
purged process fluid ~
fe~f~tedto the process line with zero ~eM volatile
organic material emissions
to the atmosphere,
or
2)
A closed purge system or closed vent system shall
collect and
recycle P~f~e~
purged process fluid
eeeete~
oi~
reeyeled to the process line
with zero volatile organic material emissions to
the
atmosphere,
or
92—448
—9—
3)
Purged process
fluid
shall
be transported
to
a
control device that complies with the requirements
of Section 215.438.
d)
In—situ sampling systems are exempt from subsection
(c).
(Source:
Amended
at
Ill. Reg.
__________
effective
______________
215.438
Standards
for Control Devices
Control devices used to comply with Section 215.437(c)
shall
comply with 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 cevice
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,
incorporated
by
reference
in Section 215.105, 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 MJ/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 MJ/scm or greater
if the
flare
is nonassisted.
The net heating value of the
gas being combusted shall
be calculated
using
the
following equation:
92—449
—10—
n
Hr
KZC1H~
i=l
Where:
H
—
Net heating value
of the sample, MJ/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 value
corresponding
to one mole is 20
C.
K
Consta9t,
1
g mole
MJ
1.740
x
10
ppm
scm
kcal
where
standard temperature
for
g mole
is
20
C.
scm
C1
=
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 215.105.
H1
=
Net heat of combustion
of
sample
component
i,
kcal/g mole.
The heats of
combustion may be
determined
using ASTM D
2382—83,
incorporated by reference
in
Section 215.105,
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 215.105,
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, ~
as determined
by the
following equation:
Vmax
=
8.706
+
O.7O84(Hr)
Vm~y=Maximum permitted velocity, rn/sec.
92—450
—11—
8.706
=
Constant.
0.7084
=
Constant.
Hr
=
The net heating value
as determined
in
subsection
(c)(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 zero volatile organic material
emissions as determined
by USEPA Reference Method 21 as
specified at 40 CFR 60, Appendix
A (1986),
incorporated
by reference
in Section 215.105.
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.
e)
The owner
or operator
of
a control device shall monitor
the
control device to ensure that it
is operated and
maintained
in conformance with its design.
f)
The control device shall be operated
at all times when
emissions may be vented
to
it.
(Source:
Section 215.438
renumbered
to Section 215.439, new
Section 215.438 adopted at
_____
Ill. Reg.
_______
effective
____________).
Section 2~5~4~82l5.439Compliance Date
The owner
or operator of
a synthetic organic chemical or polymer
manufacturing plant subject to Sections 215.430~through
~4B
215.439
shall comply with the standards and
limitations of those
Sections no later than December
31,
1987.
(Source:
Section 215.439 renumbered
from Section 215.438
and
amended
at
_____
Ill.
Reg.
_______,
effective
_________________
92—451
—12—
APPENDIX
D
LIST OF CHEMICALS DEFINING SYNTHETIC
ORGANIC
CHEMICAL
AND
POLYMER MANUFACTURING
O~?BB
Ne~
CAS No.
a
Chemical
29
105—57—7
Acetal
39
75—07—0
Acetaldehyde
49
107—89—1
Acetaldol
60—35—5
Acetamide
65
103—84—4
Acetanilide
64—19—T
Acetic
acid
88
108—24—7
Acetic
anhydride
99
67—64—1
Acetone
499
75—86—5
Acetone
cyanohydrin
4~9
75—05—8
Acetonitrile
429
98-86—2
Acetophenone
425
75-36—5
Acetyl chloride
438
74—86—2
Acetylene
449
107—02—8
Acrolein
459
79—06—1
Acrylamide
468
79—10~i
Acrylic acid ~
107—13—1
Acrylonitrile
488
124—04—9
Adipic acid
485
111—69—3
Adiponitrile
499
(b)
Alkyl
naphthalenes
298
107—18—6
Allyl
alcohol
249
107—05—1
Allyl
chloride
229
1321—11—5
Aminobenzoic
acid
239
111—41—1
Aminoethylethanolarnine
235
123—30—8
p—aminophenol
249
628—63—7,
Amyl
acetates
12 3—92—2
258
7l-4l—Oc
Amyl
alcohols
268
110—58—7
Amyl
amine
2~8
543—59—9
Amyl
chloride
288
l10—68—7c
Amyl
mercaptans
299
1322-06—1
Amyl phenol
399
62—53—3
Aniline
349
142—04—1
Aniline
hydrochloride
328
29191—52—4
Anisidine
338
100—66—3
Anisole
348
118—92—3
Anthranilic
acid
358
84—65—1
Anthraquinone
369
100—52—7
Benzaldehyde
3~9
55—21—0
Benzamide
388
71—43—2
Benzene
398
98—48—6
Benzenedisulfonic
acid
489
98-11—3
Bee—s~4fon~e
Benzenesulfonic
acid
449
134—81—6
Benzil
92—452
1.11
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2 5586—43—0
88—73—3
100—00—5
25167—80—0
126—99—8
7790—94—5
108—41—8
9 5—4 9—8
106—43—4
75—72—9
10 8—3 9—4
95—48—7
106—44—5
1319—77—3
1319—77
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3724—65—0
98—82—8
80—15—9
3 7 2—0 9—8
506—77—4
108—80—5
108—77—0
110—82—7
108—93—0
108—94--i
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,
57 311—9 2—9
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541—73—1
95—SO—i
106—46—7
75—71—8
114—44—4
107—06—2
96—23—1
26952—23—8
101—83—7
109—89—7
111—46—6
Chloroform
Chi oronaphthalene
o—chi or oni t robe n zen e
p— chi or o rii t robe n zen e
Chi orophenols
Chioroprene
Chiorosulfonic
acid
rn—c hi or o to 1 ue n e
o—chlorotol
uene
p—chlorotol
uene
Chlorotr
ifluoromethane
m— cr eso 1
0—
Cr eso 1
p—cresol
Mixed
cresols
Cresylic
acid
Crotonaldehyde
Crontonic acid
Cumene
Cumene hydroperoxide
Cyanoacetic acid
Cyanogen chloride
Cyanuric
acid
Cyanuric chloride
Cyclohexane
Cyclohexanol
Cyclohexanone
Cyclohexene
Cyci oh e x yl amine
Cyclooc tad lene
Decanol
Diacetone
alcohol
Diaminobenzoic
acid
Dichioroanil
me
m—d ichlorobenzerie
o—d ichlorobenzene
p— d Ic hi or o benz
erie
Dichiorodi
fluoromethane
Dichioroethyl
ether
1,2—dichioroethane
~~pC)
Dichlorohydr
in
Dichioropropene
Dicyclohexylamine
Diethylamine
Diethylerie glycol
92—4 54
—15—
Diethylene glycol diethyl
ether
Diethylene glycol dimethyl ether
Diethylene
yee~mer~eb~y~
glycol
monobutyl ether
Diethylene
yee’~mcrte~ti~y~
glycol
morionbutyl ether acetate
Diethylerie
yeMe~eethy~glycol
monoethyl
ether
Diethylene
yee4menee~thyIglycol
moriomethyl
ether
acetate
Diethylene
yee~mencme~thy~
glycol
monomethyl
ether
Diethyl sulfate
Di fluoroethane
Diisobutylene
Diisodecyl phthalate
Diisooctyl phthalate
Diketene
Dimethylamine
N,N—dimethylaniline
N,N—d~Mey~e~i~ter
dimethyl ether
N,N—dimethylformamide
Dimethyihydrazine
Dirnethyl
sulfate
Dimethyl sulfide
B~Meyufe~~e Dimethyl sulfoxide
~
Dimethyl
terephthalate
3,5—dinitrobenzoic acid
Dinitrophenol
Diriitrotoluene
Dioxane
Dioxolane
Diphenylamirie
Diphenyl oxide
Diphenyl
thiourea
Dipropylene glycol
Dodecene
Dodecylanilme
Dodecyiphenol
Epichlorohydr
in
Ethanol
Ethanolamines
Ethyl acetate
Ethyl acetocetate
Ethyl acrylate
Ethylamine
Ethylbenzerie
Ethyl bromide
Ethylcellulose
Ethyl chloride
i304
~3OS
~49
112—36—7
111—96—6
~k~.~?~—34—5
124—17—7
~339
111—90—0
4340
112—15—2
~69
111—77—3
~4~G
~4~9
~44G
~44~
~444
i459
3:469
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44&9
~49O
1495
~
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4S20
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64—67—5
75—37—6
25167—70—8
26761—40—0
27554—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
.i540
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4560
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458G
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46
1628
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1640
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46&9
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1~3O
4~4G
99—34—3
51—28—5
25321—14—6
123—91—1
646—06—0
122—39—4
101—84—4
1O2—O~~
25265—71—8
25378—22—7
28675—17—4
27193—86—8
106—89—8
64—17—5
141—43—5c
141—78—6
141—97—9
140—88—5
75—04—7
100—41—4
74—96—4
9004—57—3
75—00—3
92—455
—16—
so
4~6G
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2000
2929
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2849
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2969
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2~6S
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2268
226k
105—39—5
105—56—6
74—85—1
96—49—1
107—07—3
107—15—3
106—93—4
107—21—1
111—55—7
110—71—4
111—76—2
112—07—2
110—80—5
111—15—9
109—86—4
110—49—6
122—99—6
2807—30—9
75—21—B
60—29—7
104—76—7
122—51—0
95—92—1
41892—71—1
50—00—0
75—12—7
64—18—6
110—17—8
98—01—1
56—81—5
26545—73—7
25791—96—2
56—40—6
107—22—2
118—74—1
67—72—1
36653—82—4
124—09—4
629—11—8
100—97—0
74—90—8
123—31—9
99—96—7
26760—64—5
78—83—1
110—19—0
115—11—7
glycolmonoethyl
ether
glycolmonomethyl ether
glycol monophenyl
glycolmonopropyl ether
oxide
Ethyl chioroacetate
Ethylcyanoacetate
Ethylene
Ethylene carbonate
Ethylene Chiorohydrin
Ethylenediarnine
Ethylene dibromide
Ethylene glycol
Ethylene glycol diacetate
Ethylene glycol dimethyl ether
Ethylene glycol monobutyl ether
Ethylene
glycol
monobutyl
ether
acetate
Ethylene glycol morioethyl ether
Ethylene glycolmonoethyl ether
acetate
Ethylene
Ethylene
acetate
Ethylene
ether
Ethylene
Ethylene
Ethyl ether
2—ethyihexanol
Ethyl orthoformate
Ethyl oxalate
Ethyl sodium oxaloacetate
Formaldehyde
Formamide
Formic
acid
Fumaric acid
Furfural
Glycerol
(Synthetic)
Glycerol
dichiorohydrin
Glycerol
triether
Glycme
Giyoxal
Hexachlorobenzene
Hexachioroethane
Hexadecyl alcohol
Hexamethylenediamine
Hexamethylene glycol
Uexamethylenete trarnine
hydrogen cyanide
Hydroquinone
p——be~e~e
p—hydroxybenzoic
acid
Isoamylene
Isobutanol
Isobutyl acetate
Isobutylene
92—456
—17—
Isobutyraldehyde
Isobutyric
acid
Isodecanol
Isooctyl alcohol
Isoperitane
Isophorone
Isophthalic
acid
Isoprene
Isopropanol
~O~f
e~y~
Isopropyl acetate
Isopropylamine
Isopropyl chloride
Isopropyiphenol
Ketene
Linear ey~e~~e
alkyl
sulfonate
Linear alkylbenzene
(Linear dodecylberizene)
Maleic acid
Maleic anhydride
Malic
acid
Mesityl oxide
Metanilic acid
Methacrylic
acid
Methallyl chloride
Methanol
Methyl acetate
Methyl acetoacetate
Methylamine
n—methylanil me
Methyl
bromide
Methyl butynol
Methyl chloride
Methyl cyclohexane
Methyl cyclohexartone
Methylerie chiôridè
Methylene dianiline
Methylene diphenyl diisocyanate
Methyl ethyl ketone
Methyl formate
Methyl
isobutyl carbiriol
Methyl
isobutyl ketone
Methyl methacrylate
Me~hy~~en~ync~1 Methylpentynol
a—methyistyrene
Morphol the
a—naphthalene sulfonic acid
B—naphthalene sulfonic acid
a—naphtho1
B—naphthol
Neopentanoic
acid
22~8
78—84—2
~288
79-31—2
~38G
25339—17—7
2320
26952—21—6
232~
78—78—4
~33G
78—59—1
2340
121—91—5
~SG
78—79—5
~6G
67—63—0
~3~G
2~&~
108—21—4
75—31—0
2~98
75—29—6
~49G
25168—06—3
~4~G
463—51—4
~4~4
(b)
24~
123—01—3
~4~O
110—16—7
~43O
108—31—6
244G
6915—15—7
245G
141—79—7
246O~
121—47—1
~249
79—41—4
~49G
563—47—3
~5GO
67—56—1
~S~9
79—20—9
~S~9
105—45—3
~539
74—89--S
~549
100—61—8
2545
74—83—9
~55O
37365—71—2
2560
74—87—3
2S~O
108—87—2
~S9G
1331—22—2
~62O
75—09—2
2639
101—77—9
2635
101—68—8
2648
78—93—3
2644
107—31—3
26&~
108—11—2
266G
108—10—1
26&S
80—62—6
26~G
77-75-8
~698
98—83—9
Q~99
110—91—8
85—47—2
120—18—3
23~
90—15—3
2q49
135—19—3
2~SO
75—98—9
92—457
—18—
94—70—2
156—43—4
108—95—2
98—67--9,
585—38--6,
609—46--i,
133—39-~7c
91—40—7
(b)
75—44—5
85—44—9
85—41—6
108—99—6
110—85—0
9003—29—6,
25036—29—7c
253 22—68—3
25322—69—4
123—38—6
79—09—4
71—23—8
107—10—8
540—54—5
115—07—1
127—00—4
78—87—5
57—55—6
75—56—9
110—86--i
106—51—4
o—nitroanil irie
p—nitroanilthe
o—nitroanisole
p—nitroanisole
Nitrobenzene
Nitrobenzoic
acid
(0,
m
&
p)
Nitroetharie
Ni trometharie
2—Nitrophenol
Nitropropane
Nitrotoluerie
Nonene
Nei~’~phene~INonyiphenol
Oety~ ~iene~
Octyiphenol
Paraldehyde
Pentaerythritol
n—pentane
1—pentene
Perchloroethylene
Per~
Perchiorornethyl mercaptan
o—phenetid me
p—phenetidme
Phenol
Phenolsulfonic
acids
Phenyl
arithranilic
acid
Pheriylenediamine
Phosgene
Phthalic anhydride
Phthal imide
~b—p1co1 ine
Piperazine
Polybutenes
Polyethylene glyco.
Polypropylene glyco.
P~4e~e~tyde
Propional
dehyde
Propionic
acid
n—propyl
alcohol
Propylamine
Propyl chloride
Propylene
Propylene chlorohyc3rin
Propylene
dichioride
Propylene glycol
Propylene oxide
Pyridirie
Quirione
88—74—4
100—01—6
91—23—6
100—17—4
98—95—3
2717 8—8 3—2 c
79—24—3
75—52—5
88—75—5
25322—01—4
1321—12—6
27215—95—8
25154—52—3
27193—28—8
123—63—7
115—77—5
109—66—0
109—67—1
127—18—4
594—42—3
2Th6
~
2999
28~8
2828
2830
2849
~8~9
2855
28~8
~89~9
29~9
2939
~94G
29?9
29~6
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a e
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3925
30&3
3066
3680
3999
a~8o
a~o
~3i49
92—458
—19—
87—61—6,
108—70—3,
120—82—ic
71—55—6
79—00—5
79—01—6
75—69—4
96—18 —4
76—13—1
Resorcinol
Resorcylic
acid
Salicylic
acid
Sodium acetate
Sodium benzoate
Sodium ~
carboxymethyl
cellulose
Sodium chioroacetate
Sodium formate
Sodium pheriate
Sorbic acid
Styrene
Succinic acid
Succinitr ile
Sulfanilic acid
Sulfolane
Tannic acid
Terephthalic acid
Tetr achioroethanes
Tetrachlorophthalic
anhydride
Pe~f~e~hyHe~d
Tetraethyi
1ea5
Tetr ahydronaphthalene
Tetrahydrophthalic anhydride
Te~y~e~
Tetramethyl lead
Tetramethylenediamine
Tetramethylethyleried iarnine
Toluene
Tol uene—2
,
4—diamirie
Toluene—2 ,4—diisocyanate
Toluene diisocyanates
(mixture)
Toluene sulfonamide
Pe~efle
~?er~4e Toluenesulfonic
acids
Toluene
eiiy~e’er4~e
sulfonyichioride
Toluidines
Tr ichioroberizenes
1,1, 1—trichioroethane
1,1, 2—tr ichioroethane
Tr ichioroethylene
Tr ichlorofluoromethane
1,2, 3—trichioroproparie
1,1,2—trich1oro~7—
1,2, 2—tn fluoroethane
Tr iethylamine
Triethylene glycol
Triethylene
yeo~t~ethy~glycol
dimethyl ether
Tr i isobutylerie
3~5
0
3~6~
3228
~239
3249
3259
a~s~
3260
32~9
329G
39G
~320
3330
3335
334G
34~
~349
3354
335S
10 8—4 6—3
27138—57—4
69—72—7
127—09—3
53 2—3 2—1
9004
—3 2—4
39 26—6 2—3
141—53—7
139—02—6
110—44—1
100—42—5
110—15—6
110—61—2
121—57—3
126—33—0
1401—55—4
100—21—0
79—34—5c
117—08—8
78—00—2
119—64—2
85—43—8
75—74—1
110—60--i
11O-18—9
10 8—8 8—3
95—80—7
584—84—9
264
7 1—6 2—5
133 3—0
7—9
104—15—4c
~&~
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98—59—9
26915—12--8
338~7 3399
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3400
34~
3429
3439
345G
a4&e
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121—44—8
112—27—6
112—49—2
775 6—94—7
92—459
—20—
___
~
methyl
tert
—butyl ether
__________
Polyethylene
____
Polypropylene
__________
Polystyrene
Phe O~PBB
rttii~èers
~e
referet’~e~4i~4ee~
~4gned
~e the
v4~et~she~e~r~
4r~~he ergart4e ehem4e~4Predttee~Ba~
Be~edeveloped by ~A~teUS~FA~-
a)
CAS numbers
refer
to the Chemical Abstracts
Regist.ery
numbers assigned
to specific chemicals,
isonomers 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
____________
IT
IS SO ORDERED.
I, Dorothy
M. Guna, Clerk of
the Illinois Pollution Control
Board
hereby certif~th~tthe above Order was adopted on
the
_____
day of
~
,
1988,
by a vote of
7_C
Y2~
/~~/
Dorothy M./Gunri, Clerk
Illinois Pollution Control Board
3499
~5~:9
35~8
~530
354°
S
3589
3S99
75—50—3
57—13—6
108—05—4
75—01—4
75—35—4
2 50 13—15—4
133 0—20—7
9 5—4 7—6
106—42—3
1300—71—6
1300—73—8
(b)
9002—88—4
(b)
9009—53—6
Trimethylamine
Urea
Vinyl
acetate
Vinyl chloride
Vinylidene chloride
Vinyl
toluerie
Xylenes
(mixed)
o—xylene
p-
xylene
Xylenol
Xylidine
92—460