.
JCAR350225-08
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TITLE
35: ENVIRONMENTAL
PROTECTION
2
SUBTITLE
B: AIR
POLLUTION
3
CHAPTER
I:
POLLUTION
CONTROL
BOARD
4
SUBCHAPTER
c: EMISSION
STANDARDS
AND LIMITATIONS
5
FOR STATIONARY
SOURCES
6
P
011
Op,,
8
CONTROL
OF EMISSIONS
FROM LARGE
COMBUSTION
SOURCES
1Con’$JNOIs
9
10
SUBPART
A: GENERAL
PROVISIONS
11
12
Section
13
225.100
Severability
14
225.120
Abbreviations
and Acronyms
15
225.130
Definitions
16
225.140
Incorporations
by Reference
17
225.150
Commence
Commercial
Operation
18
19
SUBPART
B:
CONTROL OF MERCURY
EMISSIONS
20
FROM COAL-FIRED
ELECTRIC
GENERATING UNITS
21
22
Section
23
225.200
Purpose
24
225 .202
Measurement Methods
25
225.205
Applicability
26
225.210
Compliance
Requirements
27
225 .220
Clean Air Act
Permit Program
(CAAPP) Permit
Requirements
28
225.230
Emission
Standards for EGUs
at Existing Sources
29
225 .232
Averaging
Demonstrations for
Existing Sources
30
225.233
Multi-Pollutant
Standard
(MPS)
31
225.234
Temporary
Technology-Based
Standard for EGUs
at Existing Sources
32
225.23
5
Units
Scheduled
for Permanent
Shut Down
33
225 .237
Emission Standards
for New
Sources with EGUs
34
225.23
8
Temporary Technology-Based
Standard for New Sources
with EGUs
35
225.239
Periodic Emissions
Testing Alternative
Requirements
36
225.240
General
Monitoring
and
Reporting
Requirements
37
225.250
Initial Certification
and Recertification
Procedures
for Emissions
Monitoring
38
225 .260
Out of
Control Periods and Data
Availability
for Emission Monitors
39
225 .261
Additional
Requirements
to Provide
Heat
Input Data
40
225.263
Monitoring
of Gross Electrical
Output
41
225 .265
Coal
Analysis for Input
Mercury Levels
42
225.270
Notifications
43
225.290
Recordkeeping
and Reporting
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225.291
Combined
Pollutant Standard: Purpose
45
225.292
Applicability of the Combined Pollutant Standard
46
225.293
Combined Pollutant
Standard:
Notice of Intent
47
225.294
Combined
Pollutant Standard: Control Technology Requirements and Emissions
48
Standards for Mercury
49 225.295
Combined-Pollutant Standard: Emissions Standards for
NO
and SO
2
Treatment
50
of Mercury
Allowances
51
225.296
Combined
Pollutant
Standard: Control Technology Requirements for
NON,
SO
52
and
PM
Emissions
53
225.297
Combined Pollutant
Standard: Permanent Shut-Downs
54
225.298
Combined Pollutant Standard: Requirements for
NO
and
SO
2
Allowances
55
225.299
Combined Pollutant
Standard:
Clean
Air
Act
Requirements
56
57
SUBPART C: CLEAN AIR ACT INTERSTATE
58
RULE (CAR) SO
2 TRADING PROGRAM
59
60
Section
61
225.300
Purpose
62
225.305
Applicability
63
225.3 10
Compliance Requirements
64
225.315
Appeal
Procedures
65
225.320
Permit
Requirements
66
225.325
Trading Program
67
68
SUBPART D: CAR
NO
ANNUAL
TRADING
PROGRAM
69
70
Section
71
225 .400
Purpose
72
225.405
Applicability
73
225 .410
Compliance
Requirements
74
225.415
Appeal Procedures
75
225 .420
Permit Requirements
76
225
.425
Annual Trading Budget
77
225.43 0
Timing for Annual Allocations
78
225.435
Methodology for Calculating
Annual
Allocations
79
225 .440
Annual Allocations
80
225 .445
New Unit Set-Aside (NUSA)
81
225 .450
Monitoring, Recordkeeping and Reporting Requirements for Gross
Electrical
82
Output and Useful
Thermal
Energy
83
225.455
Clean Air Set-Aside (CASA)
84
225 .460
Energy Efficiency and Conservation, Renewable Energy, and Clean Technology
85
Projects
86
225.465
Clean Air
Set-Aside (CASA) Allowances
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225 .470
Clean Air Set-Aside (CASA) Applications
88
225.475
Agency Action on Clean Air Set-Aside (CASA) Applications
89
225.480
Compliance Supplement
Pool
90
91
SUBPART E: CAR
NO
OZONE SEASON TRADING PROGRAM
92
93
Section
94
225.500
Purpose
95
225.505
Applicability
96
225.5 10
Compliance Requirements
97
225.515
Appeal Procedures
98
225.520
Permit Requirements
99
225.525
Ozone
Season Trading
Budget
100
225.530
Timing for Ozone Season Allocations
101
225.535
Methodology for Calculating
Ozone Season Allocations
102
225.540
Ozone Season Allocations
103
225.545
New
Unit Set-Aside
(NUSA)
104
225.550
Monitoring, Recordkeeping and Reporting Requirements
for Gross Electrical
105
Output
and Useful Thermal
Energy
106
225.555
Clean Air Set-Aside (CASA)
107
225.560
Energy Efficiency and Conservation, Renewable Energy,
and Clean Technology
108
Projects
109
225.565
Clean Air
Set-Aside
(CASA) Allowances
110
225.570
Clean
Air Set-Aside (CASA)
Applications
111
225.5 75
Agency Action on Clean Air Set-Aside (CASA)
Applications
112
113
SUBPART F: COMBINED
POLLUTANT STANDARDS
114
115
225.600
Purpose (Repealed)
116
225.605
Applicability
(Repealed)
117
225.6 10
Notice of Intent (Repealed)
118
225.615
Control
Technology
Requirements and Emissions Standards for
Mercury
119
(Repealed)
120
225.620
Emissions Standards
for
NO
and
SO
2
(Repealed)
121
225.625
Control Technology Requirements for
NOR,
SO
2,and PM Emissions (Repealed)
122
225.630
Permanent Shut-Downs (Repealed)
123
225.63 5
Requirements for CAR
,2
SO CAR
NOR,
and CAIR
NO
Ozone Season
124
Allowances (Repealed)
125
225.640
Clean Air Act Requirements
(Repealed)
126
127
225.APPENDIX A
Specified EGUs
for
Purposes of the CPS Subpart F (Midwest Generation’s
128
Coal-Fired Boilers as
of July 1,
2006)
129
225.APPENDIX B
Continuous Emission Monitoring Systems
for Mercury
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131
AUTHORITY: Implementing and authorized
by Section
27
of the
Environmental
Protection
Act
132
[415 ILCS 5/27].
133
134
SOURCE: Adopted in R06-25 at 31111.
Reg.
129,
effective December 21, 2006; amended
in
135
R06-26 at 31111. Reg.
12864,
effective August 31, 2007; amended
inRO9-10 at 33111. Reg.
136
, effective
137
138
SUBPART A: GENERAL
PROVISIONS
139
140
Section 225.120 Abbreviations and Acronyms
141
142
Unless otherwise specified within this Part, the abbreviations
used in
this Part
must be the
same
143
as those found
in
35 Ill. Adm. Code 211. The following
abbreviations and acronyms
are used in
144
this
Part:
145
Act
Environmental
Protection Act [415 ILCS 5]
ACT
activated carbon injection
AETB
Air Emission Testing Body
Agency
Illinois Environmental
Protection Agency
Btu
British thermal unit
CAA
Clean Air Act (42
USC
7401
et seq.)
CAAPP
Clean Air Act Permit Program
CA1R
Clean Air Interstate Rule
CASA
Clean Air Set-Aside
CEMS
continuous emission monitoring
system
CO
2
carbon dioxide
CPS
Combined Pollutant Standard
CGO
converted
gross electrical output
CRM
certified
reference materials
CUTE
converted
useful thermal energy
DAHS
data acquisition and handling system
dscm
dry standard cubic meters
EGU
electric generating unit
ESP
electrostatic precipitator
FGD
flue gas desulfurization
feet per minute
GO
gross
electrical
output
GWh
gigawatt hour
HI
heat input
mercury
hr
hour
ISO
International
Organization
for Standardization
JCAR350225-08
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kg
kilogram
lb
pound
MPS
Multi-Pollutant Standard
MSDS
Material Safety Data Sheet
MW
megawatt
MWe
megawatt electrical
MWh
megawatt hour
NAAQS
National
Ambient Air Quality
Standards
NIST
National Institute
of
Standards
and
Technology
NO
nitrogen oxides
NTRM
NIST Traceable Reference Material
NUSA
New
Unit Set-Aside
ORIS
Office of Regulatory Information Systems
02
oxygen
PM
2.5
particles less than 2.5 micrometers in diameter
quality assurance
quality certification
RATA
relative accuracy
test audit
RGFM
reference gas flow meter
SO
2
sulfur dioxide
SNCR
selective noncatalytic reduction
TTBS
Temporary Technology
Based Standard
TCGO
total converted useful thermal energy
UTE
useful thermal energy
USEPA
United States Environmental Protection Agency
yr
year
146
147
(Source:
Amended
at 33
Ill.
Reg.
effective
148
149
Section 225.130
Definitions
150
151
The
following definitions apply for the purposes of this
Part.
Unless
otherwise defined
in this
152
Section or a different meaning
for
a term is clear from its context, the terms used in this Part
153
have the
meanings specified in 35 Ill. Adm. Code 211.
154
155
“Agency” means the Illinois Environmental
Protection Agency. [415 ILCS
156
5/3.105]
157
158
“Averaging demonstration”
means, with regard to Subpart B of this Part, a
159
demonstration of compliance that is based
on the combined performance of
EGUs
160
at two or more sources.
161
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“Base Emission
Rate?!
means, for a group of EGUs subject to emission
standards
163
for
NO
and
SO
2
pursuant
to Section 225.233, the average emission rate of
NO
or
164
SO
2
from the EGUs, in pounds per million Btu heat input,
for calendar years 2003
165
through
2005
(or, for seasonal
NOR,
the 2003 through 2005 ozone seasons),
as
166
determined
from
the
data collected and quality assured by the USEPA, pursuant
167
to the 40 CFR 72 and
96
federal
Acid Rain
and
NO
Budget Trading Programs,
168
for the emissions and heat input of that group of
EGUs.
169
170
“Board” means the Illinois Pollution Control
Board. [415 ILCS 5/3.130]
171
172
“Boiler” means an enclosed
fossil or other fuel-fired combustion device used
to
173
produce heat and to transfer heat to recirculating water, steam, or other
medium.
174
175
“Bottoming-cycle cogeneration unit” means a cogeneration unit in which the
176
energy input to the unit is first used to produce useful thermal
energy and at least
177
some
of
the reject heat
from
the useful thermal energy application or process
is
178
then used for electricity production.
179
180
“CAJR authorized account representative”
means,
for the purpose of general
181
accounts, a responsible natural person who is authorized, in accordance
with 40
182
CFR 96, subparts BB, FF, BBB, FFF, BBBB, and FFFF to transfer and
otherwise
183
dispose of CAR
NON,
,2
SO and
NO
Ozone Season allowances, as applicable,
184
held
in the CAR
NOR,
SO2,
and
NO
Ozone Season general account, and for
the
185
purpose of a CAR
NO
compliance account, a CAR
SO
2compliance account,
or
186
a CAR
NO
Ozone Season compliance account, the CAR designated
187
representative of the source.
188
189
“CAR
designated representative”
means, for a CAR
NO
source, a CAR
SO
2
190
source, and a CAR
NO
Ozone Season source and each
CAIR
NO
unit, CAR
191
SO
2
unit
and
CAR
NO
Ozone Season unit at the source, the natural person
who
192
is authorized by the owners and operators of the source and
all such units at the
193
source, in accordance with 40
CFR 96, subparts BB, FF, BBB, FFF, BBBB,
and
194
FFFF as applicable, to represent and legally bind each owner and
operator in
195
matters pertaining to the CAR
NO
Annual Trading Program, CAR
SO
2
Trading
196
Program, and CAR
NO
Ozone Season Trading Program,
as applicable. For any
197
unit
that
is
subject to one or
more
of the following programs: CAR
NO
Annual
198
Trading Program, CAR
SO
2
Trading Program, CAR
NO
Ozone Season Trading
199
Program, or the
federal
Acid Rain Program, the designated
representative for the
200
unit
must be the
same natural
person for all programs applicable to the unit.
201
202
“Coal” means any solid fuel classified
as anthracite, bituminous, subbituminous,
203
or lignite by the
American
Society for Testing and
Materials (ASTM) Standard
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Specification for Classification
of Coals by Rank D388-77, 90,
91,
95, 98a,
or
99
205
(Reapproved 2004).
206
207
“Coal-derived fuel” means any
fuel (whether in a solid, liquid or gaseous
state)
208
produced by the mechanical, thermal,
or chemical processing of coal.
209
210
“Coal-fired” means:
211
212
For purposes of SubpartSubparts
B
and F, or
for
purposes
of allocating
213
allowances
under Sections 225.435, 225.445, 225.535, and 225.545,
214
combusting any amount of coal
or
coal-derived fuel,
alone or in
215
combination with
any amount of any other fuel, during a specified
year;
216
217
Except as provided above,
combusting any amount of coal or coal-derived
218
fuel, alone or in combination with any amount of any other fuel.
219
220
“Cogeneration
unit”
means, for the purposes of Subparts
C,
D, and E,
a stationary,
221
fossil fuel-fired boiler or a stationary,
fossil
fuel-fired combustion turbine of
222
which both of the following conditions are true:
223
224
It uses equipment to
produce electricity and useful thermal energy for
225
industrial, commercial, heating,
or
cooling
purposes through the sequential
226
use
of energy; and
227
228
It
produces either
of the following during the 12-month period
beginning
229
on the date the unit first produces electricity
and during any subsequent
230
calendar year after that in which the unit first produces electricity:
231
232
For a topping-cycle cogeneration unit, both of the following:
233
234
Useful thermal energy not less than five percent
of total
235
energy output; and
236
237
Useful power that, when added
to one-half of useful
238
thermal energy produced, is not less than 42.5 percent
of
239
total energy input, if useful
thermal
energy produced
is 15
240
percent or more of total energy output,
or not less than 45
241
percent of total energy input if useful thermal energy
242
produced is
less
than
15 percent of total energy output;
or
243
244
For a bottoming-cycle cogeneration unit,
useful
power not less
245
than 45 percent of total energy input.
246
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“Combined
cycle
system” means a system comprised
of
one or
more combustion
248
turbines, heat recovery steam generators,
and steam turbines configured to
249
improve
overall efficiency of electricity generation
or
steam
production.
250
251
“Combustion turbine” means:
252
253
An enclosed device comprising a compressor, a combustor,
and a turbine
254
and in which
the flue gas resulting from the combustion of fuel in the
255
combustor passes through
the
turbine,
rotating the turbine; and
256
257
If the enclosed device described
in the above paragraph of this definition
258
is
combined
cycle, any associated duct burner, heat recovery steam
259
generator and steam turbine.
260
261
“Commence commercial operation” means, for the purposes
of SubpartSubparts
B
262
and F of this Part, with regard
to an EGU that serves a generator, to have begun
to
263
produce steam, gas, or other heated medium used to generate electricity
for sale
or
264
use, including test generation.
Such
date must remain the unit’s date of
265
commencement of operation even if the EGU
is subsequently modified,
266
reconstructed or repowered. For the purposes of Subparts
C,
D and E,
267
“commence commercial
operation” is as defined in Section 225.150.
268
269
“Commence construction” means, for
the purposes of Section 225.460(f),
270
225.470,
225.560(f), and 225.570, that the owner
or
owner’s
designee has
271
obtained all
necessary
preconstruction approvals (e.g., zoning) or permits
and
272
either has:
273
274
Begun,
or
caused to
begin, a continuous program of actual on-site
275
construction of the source, to be completed within a
reasonable time; or
276
277
Entered into binding agreements or contractual obligations,
which cannot
278
be cancelled or modified without
substantial loss to the owner or operator,
279
to
undertake
a program of actual construction of the source to
be
280
completed within a reasonable time.
281
282
For purposes of this definition:
283
284
“Construction”
shall
be determined as any physical change
or
285
change in
the method of operation, including but not limited
to
286
fabrication, erection, installation,
demolition, or modification
of
287
projects eligible for CASA allowances,
as set forth in Sections
288
225.460
and 225.560.
289
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“A
reasonable time”
shall be
determined
considering
but not
291
limited
to
the
following factors: the nature and
size of the project,
292
the
extent of design
engineering,
the amount of off-site
293
preparation,
whether equipment can
be
fabricated
or can be
294
purchased,
when the project begins (considering
both the seasonal
295
nature
of the construction activity and the existence of other
296
projects
competing
for
construction labor at the same time, the
297
place
of the environmental permit in the sequence
of corporate and
298
overall governmental
approval), and the nature of the project
299
sponsor (e.g., private, public, regulated).
300
301
“Commence
operation”,
for purposes of Subparts
C, D and E, means:
302
303
To have begun
any mechanical, chemical, or electronic
process,
including,
304
for
the purpose of a unit, start-up
of a unit’s combustion chamber, except
305
as
provided in 40
CFR 96.105, 96.205, or 96.305, as incorporated
by
306
reference in Section 225.140.
307
308
For a unit that undergoes
a physical change (other than replacement
of the
309
unit
by a unit at the same source) after the date
the unit commences
310
operation as
set forth in the first paragraph of this
definition,
such date will
311
remain the date
of commencement of operation of the unit, which
will
312
continue to be treated
as the same unit.
313
314
For a unit that
is replaced by a unit at the same
source (e.g., repowered),
315
after the date the
unit commences operation as set forth in
the first
316
paragraph of this definition, such date
will remain the replaced unit’s
date
317
of commencement
of operation, and the replacement
unit will be treated as
318
a separate unit with a separate date
for commencement of operation
as set
319
forth in this definition
as appropriate.
320
321
“Common stack” means a single
flue through which emissions from two
or
more
322
units are
exhausted.
323
324
“Compliance
account”
means:
325
326
For the purposes of Subparts
D
and
E, a CAR
NO
Allowance Tracking
327
System
account,
established by USEPA for a
CAIR
NO
source or CAR
328
NO
Ozone Season
source pursuant to 40 CFR
96, subparts FF and FFFF
329
in which any CAR
NO
allowance or CAR
NO
Ozone
Season
330
allowance allocations for the
CAR
NO
units or CAR
NO
Ozone
331
Season units at the source are initially recorded
and in which are held
any
332
CAR
NO
or CAR
NO
Ozone Season allowances
available
for use for
a
JCAR350225-081 8507r01
333
control period in order to meet the source’s
CAR
NO
or
CAIR
NO
334
Ozone Season emissions limitations
in accordance with Sections 225 .410
335
and 225.5 10, and 40 CFR 96.154
and 96.354, as incorporated by reference
336
in Section
225.140.
CAIR
NO
allowances may
not
be used for
337
compliance with
the
CAIR
NO
Ozone Season Trading Program and
338
CAR
NO
Ozone Season allowances
may not be used for compliance
339
with the CAR
NO
Annual Trading Program;
or
340
341
For the purposes
of
Subpart
C, a “compliance account” means a CAR
342
SO
2 compliance account, established
by the
USEPA for a
CAR SO
2
343
source pursuant to 40 CFR
96, subpart FFF, in which any
SO
2
units
at the
344
source
are initially recorded and in which are held any
SO
2
allowances
345
available for use for a control
period in order to meet the source’s CAIR
346
SO
2
emissions
limitations in accordance with Section 225.3 10 and 40
CFR
347
96.254, as incorporated by reference in
Section
225.140.
348
349
“Control period” means:
350
351
For the CAIR
SO
2
and
NO
Annual
Trading Programs
in Subparts
C and
352
D, the period beginning January 1 of a calendar year, except
as provided
353
in Sections 225.3
10(d)(3) and 225.410(d)(3), and ending on
December31
354
of the same year,
inclusive; or
355
356
For the CAIR
NO
Ozone Season Trading
Program in Subpart E, the
357
-
period
beginning May 1 of a calendar year, except as provided
in Section
358
225.5
10(d)(3), and
ending on September 30 of the same year, inclusive.
359
360
“Designated representative”
means, for the purposes of Subpart B of this
Part, the
361
natural person as defined in 40 CFR 60.4 102, and is
the same natural person
as
362
the
person who is the designated
representative for the CAR trading and
Acid
363
Rain programs.
364
365
“Electric generating
unit” or “EGU” means a fossil fuel-fired stationary
boiler,
366
combustion turbine or combined cycle
system that serves a generator that has
a
367
nameplate
capacity
greater than
25 MWe and produces electricity for
sale.
368
369
“Flue” means a conduit or duct through which
gases or other matter is exhausted
370
to the
atmosphere.
371
372
“Fossil fuel” means natural
gas, petroleum, coal, or any form of solid, liquid,
or
373
gaseous fuel derived from such material.
374
375
“Fossil fuel-fired” means
the combusting of any amount of fossil fuel,
alone or in
JCAR350225-08
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376
combination with
any other fuel in any calendar year.
377
378
uGenerator
means a device that produces electricity.
379
380
“Gross
electrical output”
means the total electrical output from an EGU before
381
making any deductions for energy
output
used in any way related to the
382
production of energy. For an EGU generating
only electricity, the gross electrical
383
output is
the output
from the turbine/generator set.
384
385
“Heat input” means, for the purposes of Subparts
C,
D,
and E, a specified period
386
of
time, the product (in mmBtu/hr)
of the gross calorific value of the fuel (in
387
Btu!lb) divided by 1,000,000 BtulmmBtu and multiplied
by the
fuel
feed rate into
388
a combustion device (in lb of fuelltime),
as measured, recorded and reported to
389
USEPA by
the CAR
designated representative and determined
by
USEPA
in
390
accordance with 40 CFR 96, subpart
HH,
HHH, or
HHHH, if applicable, and
391
excluding the heat derived
from preheated combustion air, recirculated flue
gases,
392
or exhaust from other sources.
393
394
“Higher heating value” or “HHV”
means the total heat liberated per mass of fuel
395
burned (Btu/lb), when fuel and dry air at standard conditions
undergo complete
396
combustion and all resultant
products
are brought to their standard states
at
397
standard conditions.
398
399
“Input mercury” means the mass of mercury that is
contained in the coal
400
combusted
within
an EGU.
401
402
“Integrated gasification combined cycle” or “IGCC”
means a coal-fired electric
403
utility steam generating
unit that
burns a synthetic gas derived from coal
in
a
404
combined-cycle gas turbine. No coal is directly
burned in the unit during
405
operation.
406
407
“Long-term cold storage” means
the complete shutdown of a unit intended
to last
408
for an extended period of time
(at
least two calendar years) where
notice for long-
409
term cold storage is provided under 40
CFR 75.6
1(a)(7).
410
411
“Nameplate capacity” means,
starting from the initial installation of a generator,
412
the maximum electrical generating output (in
MWe) that the generator is capable
413
of producing on a steady-state basis and during continuous
operation (when not
414
restricted
by
seasonal
or other deratings) as of such installation as
specified by the
415
manufacturer of the
generator or, starting from the completion of any
subsequent
416
physical change in the generator resulting in
an increase in the maximum
417
electrical generating output (in MWe) that the generator
is capable of producing
418
on a steady-state
basis
and during continuous operation (when
not restricted by
JCAR350225-081 8507r01
419
seasonal or other
deratings), such increased maximum
amount as of completion
as
420
specified by the person conducting
the physical change.
421
422
“NIST traceable elemental
mercury standards”
means
either:
423
424
j)
Compressed gas
cylinders having known concentrations
of
425
elemental mercury, which have
been prepared according to the
426
“EPA
Traceability Protocol for Assay and Certification
of Gaseous
427
Calibration Standards”;
or
428
429
Calibration gases having
known concentrations of elemental
430
mercury,
produced by a generator that
fully
meets the performance
431
requirements of the
“EPA Traceability Protocol for
Qualification
432
and Certification
of Elemental Mercury Gas Generators.”
433
434
“NIST traceable source of oxidized
mercury” means a
generator
that
is
capable
of
435
providing known concentrations of vapor
phase mercuric chloride (HgCI
2
),
and
436
that fully meets the performance
requirements
of the “EPA Traceability
Protocol
437
for
Qualification
and Certification of
Oxidized Mercury Gas Generators.”
438
439
“Oil-fired
unit” means a
unit combusting fuel oil for more than
15.0 percent of
the
440
annual heat
input in a specified
year and not qualifying as coal-fired.
441
442
“Output-based emission standard” means,
for the purposes of Subpart B of
this
443
Part, a maximum allowable rate of emissions of mercury
per unit of gross
444
electrical output
from an EGU.
445
446
“Potential electrical output capacity”
means 33 percent of a unit’s
maximum design
447
heat input, expressed in mmBtulhr divided
by
3.4
13 mmBtulMWh, and multiplied
448
by 8,760
hr/yr.
449
450
“Project sponsor” means a person
or an entity, including but not limited
to the
451
owner or
operator
of an EGU or a not-for-profit group,
that provides the majority
452
of funding for an energy efficiency and
conservation, renewable energy,
or clean
453
technology project
as listed in Sections 225 .460 and 225.560,
unless another
454
person or entity is designated
by a written agreement as the project
sponsor for
the
455
purpose of applying for
NO
allowances or
NO
Ozone Season allowances
from
456
the CASA.
457
458
“Rated-energy efficiency” means
the percentage of thermal energy
input
that is
459
recovered as useable energy in the form
of gross electrical output, useful
thermal
460
energy, or both that is used for heating, cooling, industrial
processes, or other
461
beneficial
uses as
follows:
JCAR350225-08
1 8507r01
462
463
For
electric generators, rated-energy
efficiency
is calculated
as
one
464
kilowatt
hour
(3,413
Btu) of electricity divided
by the unit’s
design heat
465
rate
using the higher heating
value
of the
fuel, and expressed
as a
466
percentage.
467
468
For combined
heat and power projects,
rated-energy
efficiency is
469
calculated using
the following
formula:
470
REE
= ((GO
+ UTE)/HI)
x
100
471
472
Where:
473
REE
= Rated-energy
efficiency, expressed
as percentage.
GO
=
Gross electrical
output of the system
expressed
in Btu/hr.
UTE
=
Useful thermal output
from the
system
that
is used for
heating,
cooling,
industrial processes or
other beneficial
uses, expressed in Btu/hr.
HI
= Heat
input, based
upon the higher heating
value of fuel,
in
Btulhr.
474
475
“Repowered”
means, for the purposes
of
an EGU,
replacement of a
coal-fired
476
boiler with one
of the following
coal-fired technologies
at the same
source as
the
477
coal-fired boiler:
478
479
Atmospheric
or pressurized
fluidized
bed
combustion;
480
481
Integrated
gasification
combined cycle;
482
483
Magnetohydrodynamics;
484
485
Direct
and indirect
coal-fired turbines;
486
487
Integrated
gasification
fuel cells; or
488
489
As
determined
by
the USEPA in consultation
with
the
United States
490
Department of
Energy, a derivative
of one or more
of the technologies
491
under this definition
and
any other
coal-fired technology
capable
of
492
controlling multiple
combustion
emissions
simultaneously
with
improved
493
boiler or
generation efficiency
and with
significantly
greater waste
494
reduction relative
to the performance
of technology
in widespread
495
commercial
use
as of
January 1, 2005.
496
JCAR350225-081 8507r01
497
“Rolling 12-month basis” means,
for the purposes of SubpartSubparts B and
F of
498
this Part, a
determination
made on a monthly basis
from the relevant data for a
499
particular calendar
month
and
the
preceding 11 calendar months (total of 12
500
months of data), with two exceptions.
For determinations involving one EGU,
501
calendar months in which the EGU does not operate
(zero EGU operating hours)
502
must not be
included
in the determination, and must
be replaced by a
preceding
503
month
or months in which
the EGU does operate, so that the determination is
still
504
based on 12 months of data. For
determinations
involving two or more EGUs,
505
calendar
months
in which none of the EGUs covered
by the determination
506
operates (zero EGU operating
hours) must not be included in the determination,
507
and must be replaced by preceding months in which
at least one of the EGUs
508
covered by the determination does
operate, so that the determination is still based
509
on 12 months
of
data.
510
511
“Total
energy output”
means, with respect to a cogeneration unit, the sum of
512
useful power and useful thermal energy produced
by the cogeneration unit.
513
514
“Useful thermal energy” means, for the
purpose of a cogeneration unit, the
515
thermal energy that is made available to an industrial or commercial process,
516
excluding any heat contained
in condensate return or makeup water:
517
518
Used in a heating application (e.g., space
heating or domestic hot water
519
heating); or
520
521
Used in a space cooling
application (e.g., thermal energy used by an
522
absorption chiller).
523
524
(Source:
Amended at 33 Ill. Reg.
effective
525
526
Section
225.140 Incorporations by Reference
527
528
The following
materials are incorporated
by
reference. These incorporations
do not include any
529
later amendments
or editions.
530
531
a)
Appendix A, Subpart A, and Performance
Specifications 2 and 3 of Appendix
B
532
of 40 CFR 60, 60.17, 60.45a, 60.49a(k)(1) and
(p),
60.50a(h), and
60.4170
533
through
60.4176
(2005).
534
535
})
40 CFR 72.2
(2005).
536
537
th)
40 CFR
75.4,
75.11
through
75.14, 75.16 through 75.19,
75.30,
75.34
through
538
75.37,
75.40
through 75.48,
75.53(e), 75.57(c)(2)(i)
through
75.57(c)(2)(vi),
539
75.60 through 75.67, 75.71,
75.74(c), Sections 2.1.1.5, 2.1.1.2, 7.7, and 7.8
of
JCAR350225-08 1 8507r01
540
Appendix A to
40
CFR 75, Appendix
C to
40
CFR 75, Section 3.3.5 of Appendix
541
F to
40 CFR 75 (2006)40
CFR
75 (2006).
542
543
de)
40 CFR78
(2006).
544
545
e4)
40 CFR 96, CAR
2
SO
Trading Program, subparts AAA (excluding 40
CFR
546
96.204 and 96.206), BBB,
FFF, GGG, and HHH (2006).
547
548
fe)
40 CFR
96,
CAR
NO
Annual Trading Program, subparts AA (excluding
40
549
CFR 96.104, 96.105(b)(2), and 96.106), BB,
FF,
GG,
and HH (2006).
550
551
g4)
40 CFR 96, CAR
NO
Ozone Season Trading
Program, subparts AAAA
552
(excluding 40 CFR 96.304,
96.305(b)(2),
and 96.306), BBBB, FFFF,
GGGG,
and
553
HHHH (2006).
554
555
hg)
ASTM.
The following
methods from the American Society for Testing
and
556
Materials, 100 Barr Harbor Drive,
P.O. Box C700, West Conshohocken PA
557
19428-2959,
(610) 832-9585:
558
559
1)
ASTM D388-77 (approved February 25,
1977), D388-90 (approved
560
March 30, 1990), D388-91a (approved April
15, 1991), D388-95
561
(approved
January 15, 1995), D388-98a (approved September
10, 1998),
562
or D388-99 (approved
September
10, 1999, reapproved in 2004),
563
Classification of Coals
by
Rank.
564
565
2)
ASTM D3173-03,
Standard
Test Method for Moisture in the
Analysis
566
Sample of Coal and Coke (Approved
April 10, 2003).
567
568
3)
ASTM D3684-01, Standard Test
Method for Total Mercury in Coal
by the
569
Oxygen
Bomb CombustionlAtomic Absorption Method
(Approved
570
October 10, 2001).
571
572
4
ASTM D4840-99, Standard Guide for Sampling
Chain-of-Custody
573
Procedures (Reapproved 2004).
574
575
54)
ASTM D5865-04,
Standard
Test Method for Gross Calorific
Value
of
576
Coal and Coke (Approved April
1,
2004).
577
578
65)
ASTM
D6414-01,
Standard
Test Method for Total Mercury
in Coal
and
579
Coal
Combustion Residues by Acid Extraction or Wet
OxidationlCold
580
Vapor Atomic
Absorption (Approved October 10, 2001).
581
JCAR350225-08 1 8507r01
582
76)
ASTM D6784-02, Standard
Test Method for Elemental, Oxidized,
583
Particle-Bound and Total Mercury in Flue
Gas Generated from Coal-Fired
584
Stationary
Sources (Ontario Hydro Method) (Approved April
10,
2002).
585
586
)
ASTM D691 1-03. Standard Guide
for Packaging and Shipping
587
Environmental Samples for Laboratory
Analysis.
588
589
2)
ASTM D7036-04, Standard Practice
for Competence of Air Emission
590
Testing Bodies.
591
592
ih)
Federal Energy Management Program, M&V Guidelines:
Measurement and
593
Verification for Federal Energy Projects,
US
Department of Energy, Office
of
594
Energy Efficiency and Renewable Energy, Version 2.2,
DOE/GO-102000-0960
595
(September 2000).
596
597
(Source: Amended at 33 Iii. Reg.
effective
598
599
SUBPART B: CONTROL OF MERCURY
EMISSIONS
600
FROM COAL-FIRED ELECTRIC GENERATING
UNITS
601
602
Section 225.202 Measurement Methods
603
604
Measurement of mercury must be according to the following:
605
606
a)
Continuous emission monitoring
pursuant
to Appendix B to this Part or an
607
alternative emissions monitoring system, alternative reference
method
for
608
measuring emissions,
or other alternative to the emissions monitoring and
609
measurement requirements of Sections 225.240
through
225.290, if such
610
alternative is submitted
to the Agency in writing and approved in writing
by
the
611
Manager of the Bureau of Air’s Compliance Section.40
CFR 75 (2005).
612
613
b)
ASTM D3173-03, Standard Test Method for Moisture
in the Analysis Sample
of
614
Coal and Coke (Approved April
10, 2003), incorporated by reference in Section
615
225.140.
616
617
c)
ASTM D3684-01, Standard Test Method for
Total Mercury in Coal by the
618
Oxygen Bomb CombustionlAtomic Absorption Method (Approved
October 10,
619
2001), incorporated
by
reference in
Section 225.140.
620
621
d)
ASTM D5865-04, Standard Test Method for
Gross Calorific Value of Coal and
622
Coke
(Approved
April 1, 2004), incorporated
by
reference
in Section 225.140.
623
JCAR350225-081
8507r01
624
e)
ASTM
D6414-01,
Standard Test
Method for Total Mercury in
Coal and Coal
625
Combustion Residues
by
Acid Extraction
or Wet Oxidation/Cold Vapor Atomic
626
Absorption
(Approved October 10, 2001), incorporated
by reference in Section
627
225.140.
628
629
f)
ASTM D6784-02, Standard Test Method for
Elemental, Oxidized, Particle-Bound
630
and
Total Mercury
in Flue Gas Generated from Coal-Fired
Stationary Sources
631
(Ontario Hydro Method) (Approved
April
10, 2002), incorporated
by
reference
in
632
Section 225.140.
633
634
g)
Emissions testing pursuant to Appendix
A of
40
CFR 60.
635
636
(Source: Amended at 33 Iii. Reg.
effective
637
638
Section 225.210 Compliance Requirements
639
640
a)
Permit Requirements.
641
The
owner or operator
of
each
source with one or more EGUs subject to
this
642
Subpart B at the source must apply for a
CAAPP permit that addresses the
643
applicable
requirements
of this Subpart B.
644
645
b)
Monitoring and Testing Requirements.
646
647
1)
The owner or operator of each source and
each EGU at the source must
64.8
comply with
either the monitoring requirements of Sections 225.240
649
through 225 .290
of
this
Subpart B, the periodic emissions testing
650
requirements of Section 225.23
9
of this
Subpart B, or an alternative
651
emissions monitoring
system, alternative reference method for
measuring
652
emissions, or other alternative to the emissions
monitoring and
653
measurement requirements
of Sections 225.240 through 225.290, if
such
654
alternative
is submitted to the Agency in writing
and approved in writing
655
by the Manager of the Bureau
of Air’s Compliance Section.
656
657
2)
The compliance of each EGU with
the mercury requirements of Sections
658
225.230 and 225.237
of this Subpart B must be determined
by the
659
emissions measurements
recorded
and reported in accordance with
either
660
Sections
225.240
through 225.290
of
this
Subpart
B, Section 225.239
of
661
this Subpart B,
or an alternative emissions monitoring
system, alternative
662
reference method
for measuring emissions, or other alternative
to the
663
emissions monitoring
and measurement requirements of Sections 225.240
664
through
225.290,
if such alternative
is submitted to the Agency in writing
665
and approved
in writing
by
the Manager of
the Bureau of Air’s
666
Compliance Section.
JCAR350225-08 1 8507r01
667
668
c)
Mercury Emission Reduction Requirements
669
The owner or
operator
of any EGU subject to this Subpart B must comply with
670
applicable requirements for control
of
mercury
emissions of Section 225.230 or
671
Section 225.237 of this Subpart B.
672
673
d)
Recordkeeping
and
Reporting Requirements
674
Unless otherwise provided, the owner or operator
of a source with one or more
675
EGUs at the source must keep on site at the source each of the documents
listed in
676
subsections
(d)(1) through
(d)(3) of this Section for a period of five years from the
677
date the document is created. This period may be extended, in writing
by the
678
Agency,
for cause, at any time prior
to
the end
of five years.
679
680
1)
All emissions monitoring information gathered in
accordance with
681
Sections
225.240
through 225.290 and all periodic emissions testing
682
information gathered in accordance with Section 225.239.
683
684
2)
Copies of all reports, compliance certifications, and
other submissions and
685
all records made or required or documents necessary to demonstrate
686
compliance with
the requirements of this Subpart B.
687
688
3)
Copies of all documents used to complete a permit application
and any
689
other submission under this Subpart B.
690
691
e)
Liability.
692
693
1)
The owner or operator of each source with one or more EGUs must
meet
694
the requirements of this Subpart B.
695
696
2)
Any provision of this Subpart B that applies
to a
source
must
also
apply
to
697
the owner and operator of such source and to the owner or operator of
698
each EGU at the source.
699
700
3)
Any provision of this Subpart B that applies to an EGU must also apply
to
701
the
owner
or operator
of such EGU.
702
703
f)
Effect on Other Authorities. No provision of this Subpart B may be construed
as
704
exempting or
excluding the
owner or
operator of a source or EGU from
705
compliance with any other provision
of an
approved
State Implementation Plan,
a
706
permit, the Act, or the CAA.
707
708
(Source: Amended at 33 Ill. Reg.
effective
709
JCAR350225-081 8507r01
710
Section 225.220 Clean Air
Act Permit Program (CAAPP) Permit Requirements
711
712
a)
Application
Requirements.
713
714
1)
Each source with one or
more EGUs subject to the requirements of this
715
Subpart B is required to submit
a
CAAPP
permit application that
716
addresses all applicable requirements of this Subpart
B,
applicable
to each
717
EGU at the
source.
718
719
2)
For any EGU that commenced commercial operation:
720
721
A)
on
or
before December 31, 2008, the owner or operator
of
such
722
EGUs must submit an initial permit application
or application for
723
CAAPP
permit modification that meets the requirements of this
724
Section on or before December 31, 2008.
725
726
B)
after December 31, 2008, the owner or operator
of
any
such
EGU
727
must submit
an initial CAAPP permit application or application
for
728
CAAPP modification that meets the requirements
of this Section
729
not later than 180 days before initial startup of the EGU, unless
the
730
construction
permit issued for the EGU addresses the requirements
731
of this Subpart
B.
732
733
b)
Contents of Permit Applications.
734
In addition to other information required for a complete application for CAAPP
735
permit or CAAPP permit modification,
the application must include the following
736
information:
737
738
1)
The ORIS (Office of Regulatory Information Systems)
or facility code
739
assigned to the source
by the
U.S.
Department of Energy, Energy
740
Information Administration, if applicable.
741
742
2)
Identification
of each EGU at the source.
743
744
3)
The
intended
approach
to the monitoring requirements of Sections
745
225 .240 through 225.290 of
this Subpart B, or, in the alternative, the
746
applicant may include its intended approach to the
testing requirement
of
747
Section 225 .239
of this Subpart B.
748
749
4)
The intended approach
to
the
mercury emission reduction requirements
of
750
Section 225.230 or 225.237 of this Subpart B,
as
applicable.
751
752
c)
Permit
Contents.
JCAR350225-081 8507r01
753
754
1)
Each CAAPP permit issued
by
the Agency for a source
with one or more
755
EGUs subject
to the requirements of this Subpart B must contain federally
756
enforceable conditions addressing all applicable
requirements of this
757
Subpart B, which conditions must be a complete
and segregable portion of
758
the source’s entire CAAPP permit.
759
760
2)
In addition to conditions related
to the applicable requirements of this
761
Subpart B, each such CAAPP permit must also contain the information
762
specified under
subsection
(b) of this Section.
763
764
(Source:
Amended at 33 Ill. Reg.
effective
765
766
Section 225.230 Emission Standards for EGUs at Existing Sources
767
768
a)
Emission Standards.
769
770
1)
Except as provided in Sections 225.230(b)
and
(d),
225 .232
through
771
225.234,
225.239, and 225.29 1 through 225.299 of this Subpart
B,
772
beginningBeginning
July
1, 2009, the owner or operator of a source with
773
one or more EGUs
subject to this Subpart B that commenced commercial
774
operation on or before December 31, 2008, must
comply with one of the
775
following standards for each EGU on a rolling 12-month basis:
776
777
A)
An
emission standard of 0.0080 lb mercury/GWh gross electrical
778
output; or
779
780
B)
A minimum 90-percent reduction
of input mercury.
781
782
2)
For an EGU complying with subsection (a)(1)(A)
of this Section, the
783
actual mercury emission rate of the EGU for each 12-month rolling
period,
784
as monitored in accordance with this Subpart
B
and calculated
as follows,
785
must not
exceed
the applicable emission standard:
786
787
ER=E
1
÷O1
788
789
Where:
790
ER = Actual mercury emissions rate of the EGU for the particular
12-
month rolling period, expressed in lbIGWh.
E
= Actual mercury emissions
of the EGU, in ibs, in an individual
month in the 12-month rolling period, as determined
in
JCAR350225-08
1 8507r01
accordance with
the emissions monitoring provisions
of
this
Subpart B.
O
= Gross electrical output of the EGU, in
GWh, in
an individual
month
in
the 12-month
rolling period, as determined in
accordance with Section 225.263
of this Subpart B.
791
792
3)
For an EGU
complying with subsection
(a)(1)(B)
of
this Section,
the
793
actual control efficiency for
mercury emissions achieved by the EGU
for
794
each
12-month
rolling period, as monitored
in accordance with this
795
Subpart B
and calculated as follows, must meet or exceed the applicable
796
efficiency requirement:
797
798
CE=100x{1—(>ZE1
÷I1
)}
799
800
Where:
801
CE
= Actual control efficiency for mercury emissions
of the EGU for
the
particular
12-month
rolling period, expressed as a percent.
E
Actual mercury emissions
of the EGU, in ibs, in an individual
month in the 12-month rolling
period, as determined in
accordance with the emissions monitoring provisions
of this
Subpart B.
I,
= Amount
of mercury in the fuel fired in the EGU, in lbs, in
an
individual month in the 12-month
rolling period, as determined
in
accordance with Section 225.265 of this Subpart B.
802
803
b)
Alternative
Emission
Standards for Single EGUs.
804
805
1)
As
an alternative
to compliance with the emission standards in
subsection
806
(a) of this Section, the owner or operator
of the EGU may comply with
the
807
emission standards
of this Subpart B by demonstrating that the actual
808
emissions
of mercury from the EGU are less
than the allowable emissions
809
of mercury from the EGU
on a rolling 12-month basis.
810
811
2)
For
the purpose
of demonstrating compliance with the alternative
emission
812
standards of this subsection
(b), for each rolling 12-month period, the
813
actual emissions of mercury from
the EGU,
as monitored in accordance
814
with
this
Subpart B, must not exceed the allowable
emissions
of mercury
815
from the
EGU, as further provided
by
the following formulas:
816
817
E
12
A
12
818
JCAR350225-08 1 8507r01
819
E
12
=E
1
820
821
A
12
=A
1
822
823
Where:
824
= Actual mercury emissions
of the EGU for the particular
12-month rolling period.
A
12
= Allowable mercury emissions
of the EGU for the particular
12-month
rolling period.
= Actual mercury emissions of the
EGU
in
an individual
month
in the 12-month rolling period.
= Allowable mercury emissions of the EGU in
an individual
month in
the
12-month
rolling period, based on either the
input mercury to the unit
)
or the electrical
output
from
the EGU
),
as selected by the owner or
operator
of
the
EGU for
that
given
month.
= Allowable mercury emissions of the
EGU in an individual
month based on the input mercury to the EGU, calculated
as 10.0 percent (or 0.100) of the input mercury to the
EGU.
= Allowable
mercury
emissions of the EGU in a particular
month based on the electrical output from the EGU,
calculated
as the product of the output based mercury limit,
i.e., 0.0080 lb/GWh, and the electrical output
from the
EGU,
in GWh.
825
826
3)
If the owner or operator
of an EGU does not conduct the necessary
827
sampling,
analysis,
and recordkeeping, in accordance with Section
828
225 .265 of this Subpart B, to determine
the mercury input to the EGU, the
829
allowable emissions
of the EGU must be calculated based on the electrical
830
output of the EGU.
831
832
c)
If
two or more EGUs are served
by common
stack4s
and the owner or operator
833
conducts monitoring for mercury emissions in the common
stacks, as provided
834
for by
Sections 1.14 through
1.18 of Appendix B to this Part4O CFR 75, subpart
I,
835
such that the mercury emissions
of each EGU are not determined separately,
836
compliance of the EGUs with the applicable
emission standards of this Subpart B
837
must be determined as if the EGUs were a single EGU.
838
839
d)
Alternative Emission Standards
for Multiple EGUs.
840
JCAR350225-08 1 8507r01
841
1)
As an alternative to compliance with the emission standards of subsection
842
(a) of this Section, the owner
or operator of a source
with
multiple EGUs
843
may comply with the emission standards of this Subpart B
by
844
demonstrating
that the actual emissions of mercury from all EGUs
at the
845
source are
less
than the allowable
emissions of mercury from all EGUs
at
846
the source on a rolling 12-month basis.
847
848
2)
For the
purposes of the alternative emission standard of subsection
(d)(1)
849
of this Section, for each rolling 12-month
period, the
actual
emissions of
850
mercury from all the EGUs at the source, as monitored in accordance
with
851
this Subpart B, must not exceed the
sum of the
allowable
emissions of
852
mercury
from all the EGUs at the source, as further provided by the
853
following formulas:
854
855
ESAS
856
857
E
3
=E
858
859
860
861
Where:
862
Es
= Sum
of the actual mercury emissions of the EGUs at the source.
A5
Sum of the allowable mercury emissions of the EGUs
at the source.
E
= Actual
mercury emissions of an individual EGU at the source,
as
determined in accordance with subsection (b)(2)
of this Section.
A
= Allowable mercury
emissions of an individual EGU at the
source, as
determined in accordance with subsection (b)(2) of
this Section.
n
= Number
of
EGUs covered
by the demonstration.
863
864
3)
If an owner or operator of a source
with two or more EGUs that is relying
865
on this subsection (d) to demonstrate compliance fails to meet the
866
requirements
of this
subsection
(d) in a given 12-month rolling period,
all
867
EGUs at such source covered
by
the
compliance
demonstration
are
868
considered out of compliance with the applicable emission standards
of
869
this Subpart B for the entire last month of that period.
870
871
(Source:
Amended at 33 Iii. Reg.
effective
872
873
Section 225.233
Multi-Pollutant
Standards (MPS)
JCAR350225-081
8507r01
874
875
a)
General.
876
877
1)
As an alternative
to compliance with the emissions standards
of Section
878
225.230(a),
the owner
of
eligible
EGUs
may elect for those
EGUs
to
879
demonstrate compliance pursuant to
this Section, which establishes
880
control requirements
and standards for emissions
of
NO
and
SO
2,
as well
881
as for emissions
of mercury.
882
883
2)
For the purpose
of this Section, the following requirements
apply:
884
885
A)
An
eligible
EGU is an EGU that is located in Illinois
and which
886
commenced commercial operation
on or before December 31,
887
2004; and
888
889
B)
Ownership of an
eligible EGU is determined based on direct
890
ownership,
by the holding of a majority interest
in a company
that
891
owns the EGU
or EGUs, or by the common ownership
of the
892
company that owns the EGU, whether
through a parent-subsidiary
893
relationship,
as a sister corporation, or as
an affiliated corporation
894
with the same
parent corporation, provided that
the owner has the
895
right or authority
to submit a CAAPP application on behalf
of the
896
EGU.
897
898
3)
The owner of one
or
more EGUs electing to demonstrate
compliance with
899
this Subpart B pursuant to this
Section must submit an application
for a
900
CAAPP permit modification to the Agency,
as provided in Section
901
225.220, that includes
the
information
specified in subsection
(b) of this
902
Section and which clearly states the owner’s
election to demonstrate
903
compliance pursuant
to
this
Section 225.233.
904
905
A)
If the owner of one or
more EGUs elects to demonstrate
906
compliance
with this Subpart pursuant
to
this
Section,
then all
907
EGUs it owns in Illinois
as of July 1, 2006, as defined in
908
subsection
(a)(2)(B) of this Section, must
be thereafter subject
to
909
the standards and control
requirements of this Section,
except as
910
provided in subsection (a)(3)(B).
Such EGUs must be referred
to
911
as a
Multi-Pollutant
Standard (MPS)
Group.
912
913
B)
Notwithstanding the
foregoing, the owner may exclude
from an
914
MPS Group any EGU scheduled
for permanent shutdown that
the
915
owner
so designates in its CAAPP application
required
to be
916
submitted
pursuant to subsection (a)(3)
of
this
Section,
with
JCAR350225-081 8507r01
917
compliance for such units
to be
achieved
by means of Section
918
225.235.
919
920
4)
When
an EGU is subject to the requirements
of this Section, the
921
requirements
apply to all owners or operators of the EGU,
and to the
922
designated representative
for the EGU.
923
924
b)
Notice
of Intent.
925
The owner of one
or
more EGUs that intends to comply with this
Subpart B by
926
means of this Section must notify the Agency
of its intention by December 31,
927
2007.
The following
information must accompany the notification:
928
929
1)
The identification
of
each
EGU that will be complying with this
Subpart B
930
by means of the multi-pollutant standards contained
in this Section, with
931
evidence that the owner has identified
all EGUs that it owned in Illinois
as
932
of July
1,
2006
and which commenced commercial
operation
on or before
933
December 31, 2004;
934
935
2)
If an EGU identified in
subsection (b)(1) of this Section is also
owned or
936
operated by a person different than
the
owner
submitting the notice
of
937
intent, a demonstration that the submitter has
the right to commit the
EGU
938
or authorization
from the responsible official for the
EGU accepting the
939
application;
940
941
3)
The Base Emission Rates for the EGUs,
with copies of supporting data
942
and
calculations;
943
944
4)
A summary of the current control devices installed
and operating on each
945
EGU and identification
of the additional control devices that will
likely
be
946
needed for
the each EGU to comply with emission
control requirements
of
947
this Section, including identification
of each EGU in the MPS group
that
948
will be addressed
by subsection (c)(1)(B) of this Section,
with information
949
showing that the eligibility criteria for
this
subsection (b) are satisfied;
and
950
951
5)
Identification of each EGU that
is scheduled for permanent shut down,
as
952
provided
by Section 225 .235, which will not
be part of the MPS Group
953
and which will not
be demonstrating compliance with this
Subpart B
954
pursuant to this Section.
955
956
c)
Control
Technology
Requirements
for Emissions of
Mercury.
957
958
1)
Requirements for EGUs in an
MPS
Group.
959
JCAR350225-08
1 8507r01
960
A)
For each EGU in an
MPS
Group other
than
an
EGU that is
961
addressed
by subsection (c)(1)(B) of this Section for the period
962
beginning July
1,
2009
(or
December 31, 2009 for an EGU for
963
which an
SO
2
scrubber
or
fabric filter is being
installed
to be in
964
operation by December 31, 2009), and ending
on
December
31,
965
2014
(or
such earlier date that the EGU is subject to the mercury
966
emission standard in
subsection (d)(1) of this Section), the owner
967
or operator of the EGU must install, to the extent
not already
968
installed,
and properly operate and maintain one of the following
969
emission control devices:
970
971
i)
A Halogenated Activated Carbon Injection
System,
972
complying with the sorbent injection requirements of
973
subsection (c)(2) of this Section, except as may
be
974
otherwise
provided by subsection (c)(4) of this Section,
and
975
followed by a Cold-Side Electrostatic Precipitator
or Fabric
976
Filter;
or
977
978
ii)
If the boiler fires bituminous coal, a Selective Catalytic
979
Reduction
(SCR)
System
and
an SO
2 Scrubber.
980
981
B)
An owner of an EGU in an MPS Group has two options
under this
982
subsection (c). For an MPS Group that contains EGUs smaller
983
than
90 gross MW in capacity, the owner may designate any
such
984
EGUs to be not subject
to
subsection
(c)(1)(A) of this Section.
Or,
985
for an MPS Group that contains EGUs with gross
MW capacity of
986
less than
115 MW, the owner may designate any such EGUs
to be
987
not subject to subsection (c)(1)(A) of this Section,
provided that
988
the
aggregate
gross MW capacity of the designated EGUs does
not
989
exceed 4% of the total gross MW capacity
of
the
MPS
Group. For
990
any EGU
subject to one of these two options, unless the EGU is
991
subject to the emission standards in subsection (d)(2)
of
this
992
Section, beginning
on
January
1,
2013,
and
continuing until such
993
date that the owner or operator of the EGU commits to
comply
994
with the mercury emission standard
in subsection (d)(2) of this
995
Section, the owner or operator of the EGU must install
and
996
properly operate and maintain a Halogenated Activated Carbon
997
Injection
System
that
complies
with
the sorbent injection
998
requirements of subsection (c)(2) of this
Section, except as may
be
999
otherwise provided by subsection (c)(4) of this Section,
and
1000
followed by either a Cold-Side Electrostatic Precipitator
or Fabric
1001
Filter.
The use of a properly installed, operated, and maintained
1002
Halogenated Activated Carbon Injection
System that meets the
JCAR350225-081 8507r01
1003
sorbent injection requirements
of
subsection (c)(2)
of this Section
1004
is defined
as the “principal control technique.”
1005
1006
2)
For each
EGU for which injection of halogenated activated
carbon
is
1007
required
by subsection (c)(1) of this Section, the owner or operator
of the
1008
EGU must inject halogenated activated
carbon in an optimum manner,
1009
which,
except as provided in subsection
(c)(4) of this Section, is defined
as
1010
all of the
following:
1011
1012
A)
The use of an injection system
designed for
effective
absorption
of
1013
mercury,
considering the configuration of the EGU and its
1014
ductwork;
1015
1016
B)
The injection
of halogenated activated carbon manufactured
by
1017
Alstom, Norit, or Sorbent Technologies,
or Calgon Carbon’s
1018
FLUEPAC
MC Plus, or the injection of any other halogenated
1019
activated carbon or sorbent that
the owner or operator of the EGU
1020
has
demonstrated to have similar or better effectiveness
for control
1021
of mercury emissions; and
1022
1023
C)
The
injection of sorbent at the following minimum rates,
as
1024
applicable:
1025
1026
i)
For an EGU firing
subbituminous coal, 5.0 lbs per million
1027
actual cubic feet or, for any
cyclone-fired EGU that will
1028
install
a scrubber and baghouse
by
December
31, 2012,
and
1029
which already meets
an emission rate of 0.020 lbs
1030
mercury/GWh gross electrical output or at least
75 percent
1031
reduction of input
mercury,
2.5 lbs per million actual
cubic
1032
feet;
1033
1034
ii)
For an
EGU firing bituminous coal, 10.0 lbs per million
1035
actual cubic feet for any
cyclone-fired EGU that will install
1036
a scrubber and
baghouse by December
31,
2012, and
which
1037
already meets an emission
rate of 0.020 lb mercury/GWh
1038
gross electrical output or at least
75
percent reduction
of
1039
input mercury,
5.0 lbs per million actual cubic feet;
1040
1041
iii)
For an EGU firing a blend
of subbituminous and
1042
bituminous
coal, a rate that is the weighted average
of the
1043
above
rates,
based on the blend of coal being fired;
or
1044
JCAR350225-081 8507r01
1045
iv)
A rate or
rates set lower
by
the Agency, in writing,
than
the
1046
rate specified
in any
of
subsections
(c)(2)(C)(i),
1047
(c)(2)(C)(ii),
or (c)(2)(C)(iii)
of this Section on
a
unit-
1048
specific
basis,
provided
that the owner or
operator of the
1049
EGU
has demonstrated
that such
rate
or rates are needed
so
1050
that carbon injection
will not increase particulate
matter
1051
emissions
or opacity
so as to threaten
noncompliance
with
1052
applicable requirements
for particulate
matter or opacity.
1053
1054
D)
For the
purposes
of
subsection (c)(2)(C)
of this Section, the
flue
1055
gas
flow rate must be
determined for the point
of sorbent
injection;
1056
provided
that this
flow rate
may be assumed
to be identical to
the
1057
stack
flow rate if the gas
temperatures at the
point
of
injection
and
1058
the stack
are normally within
100°F, or
the flue gas flow rate
may
1059
otherwise
be calculated
from the stack flow
rate, corrected
for the
1060
difference
in gas temperatures.
1061
1062
3)
The owner or
operator of an EGU
that seeks
to
operate an EGU with
an
1063
activated carbon
injection rate
or rates that are set on
a unit-specific
basis
1064
pursuant to subsection
(c)(2)(C)(iv)
of this Section
must submit an
1065
application
to the Agency proposing
such rate
or rates, and must
meet
the
1066
requirements
of subsections
(c)(3)(A) and (c)(3)(B)
of this Section,
subject
1067
to
the limitations
of subsections
(c)(3)(C) and
(c)(3)(D)
of this Section:
1068
1069
A)
The application
must be submitted
as an application
for a new
or
1070
revised federally
enforceable
operating
permit
for the EGU, and
it
1071
must include
a summary of
relevant mercury emission
data for
the
1072
EGU, the
unit-specific injection
rate or rates
that are proposed,
and
1073
detailed
information to support
the proposed injection
rate
or
rates;
1074
and
1075
1076
B)
This
application
must be submitted
no
later
than the date that
1077
activated carbon
must first
be injected. For example,
the owner
or
1078
operator of
an EGU that must inject
activated
carbon pursuant to
1079
subsection (c)(1)(A)
of this
subsection must apply
for unit-specific
1080
injection
rate or rates
by
July 1,
2009.
Thereafter,
the owner or
1081
operator
of the EGU may supplement
its application;
and
1082
1083
C)
Any
decision of the Agency
denying a permit
or granting a
permit
1084
with
conditions that set
a lower injection
rate or rates may
be
1085
appealed
to the Board
pursuant to Section
39 of the Act;
and
1086
JCAR350225-081 8507r01
1087
D)
The owner or operator
of an EGU may operate at the injection rate
1088
or rates proposed in its application until a final decision is made
on
1089
the application, including
a final decision on any appeal to the
1090
Board.
1091
1092
4)
During any
evaluation of the effectiveness of a listed sorbent, an
1093
alternative sorbent, or other technique
to control mercury emissions, the
1094
owner or operator of an EGU need
not
comply with the requirements
of
1095
subsection
(c)(2) of this Section for any system needed to carry out the
1096
evaluation, as further provided as
follows:
1097
1098
A)
The owner or operator
of the EGU must conduct the
evaluation
in
1099
accordance
with a formal evaluation program submitted to the
1100
Agency at least 30 days prior
to
commencement of the evaluation;
1101
1102
B)
The duration and scope of the evaluation may not exceed the
1103
duration
and
scope
reasonably needed to complete the desired
1104
evaluation of the alternative control technique, as initially
1105
addressed
by the owner or operator in a support document
1106
submitted with the evaluation
program;
1107
1108
C)
The owner or operator of the EGU must submit a report to the
1109
Agency no later than 30 days after the conclusion of the evaluation
1110
that describes
the
evaluation
conducted and which provides the
1111
results of the evaluation; and
1112
1113
D)
If the evaluation
of the alternative control technique shows less
1114
effective control of mercury emissions
from the EGU
than
was
1115
achieved with
the principal control technique, the owner or
1116
operator of the EGU must resume use
of
the principal control
1117
technique. If the evaluation
of the alternative control technique
1118
shows comparable effectiveness to the principal control technique,
1119
the owner or operator of the
EGU
may either continue to use the
1120
alternative
control
technique in a manner that is at least as effective
1121
as the principal control
technique,
or it may resume use of the
1122
principal control technique. If the evaluation
of the
alternative
1123
control
technique shows more effective control of mercury
1124
emissions than the control
technique, the owner or operator of the
1125
EGU must continue to use
the alternative control technique in a
1126
manner
that is more effective than the principal control
technique,
1127
so
long
as it continues to be subject to this subsection (c).
1128
JCAR350225-08 1 8507r01
1129
5)
In addition to complying
with
the applicable recordkeeping and
1130
monitoring requirements
in Sections 225.240
through
225.290,
the
owner
1131
or operator of an EGU
that elects to comply with this Subpart B
by means
1132
of
this Section
must also
comply with the following additional
1133
requirements:
1134
1135
A)
For the first
36 months that injection of sorbent is required,
it must
1136
maintain records
of the usage of sorbent, the exhaust gas flow
rate
1137
from
the EGU, and the sorbent feed rate, in pounds
per million
1138
actual cubic feet
of exhaust gas at the injection point, on a weekly
1139
average;
1140
1141
B)
After
the first 36 months that injection of sorbent is required,
it
1142
must monitor activated
sorbent feed rate to the EGU, flue gas
1143
temperature
at the point of sorbent injection, and exhaust
gas flow
1144
rate from the EGU, automatically
recording
this data and the
1145
sorbent
carbon feed rate, in pounds per million actual cubic
feet
of
1146
exhaust gas at the injection point,
on an hourly average; and
1147
1148
C)
If a blend
of bituminous and subbituminous coal is fired in
the
1149
EGU, it must keep
records of the amount of each type of coal
1150
burned and the required injection rate
for injection of activated
1151
carbon, on a weekly basis.
1152
1153
As an alternative
to the CEMS monitoring, recordkeeping, and reporting
1154
requirements in Sections 225.240 through 225.290,
the owner or operator
1155
of an
EGU may elect to comply with the emissions testing, monitoring,
1156
recordkeeping, and reporting requirements
in Section
225.239(c),
(d),
(e),
1157
(f)(1) and
(2), (h)(2),
(i)(3)
and
(4),
and
(j)(1).
1158
1159
7é)
In addition
to
complying
with the applicable reporting requirements
in
1160
Sections 225.240 through 225.290, the owner
or operator of an EGU
that
1161
elects to comply
with this Subpart B by means of this Section must
also
1162
submit quarterly reports for the recordkeeping
and monitoring conducted
1163
pursuant to subsection
(c)(5) of this Section.
1164
1165
d)
Emission Standards for Mercury.
1166
1167
1)
For each EGU in an
MPS
Group
that is not addressed by subsection
1168
(c)(1)(B) of this Section, beginning
January 1, 2015 (or such earlier
date
1169
when
the owner or operator of the EGU notifies
the Agency that it will
1170
comply
with
these
standards)
and continuing thereafter, the
owner or
JCAR350225-0818507r01
1171
operator
of the EGU must comply
with
one of the following standards
on
1172
a rolling 12-month
basis:
1173
1174
A)
An emission standard of
0.0080 lb mercury/GWh gross electrical
1175
output;
or
1176
1177
B)
A minimum 90-percent reduction
of input mercury.
1178
1179
2)
For each EGU
in an MPS Group that has been addressed under subsection
1180
(c)(1)(B) of this Section, beginning
on the date when the owner or
1181
operator of
the EGU notifies the Agency that it will comply with these
1182
standards and continuing thereafter,
the
owner
or operator of the EGU
1183
must comply with
one of the following standards on a rolling 12-month
1184
basis:
1185
1186
A)
An emission standard of 0.0080 lb mercury/GWh
gross
electrical
1187
output; or
1188
1189
B)
A minimum
90-percent reduction of input mercury.
1190
1191
3)
Compliance with the mercury emission standard or
reduction requirement
1192
of this subsection (d) must be calculated in accordance with Section
1193
225.230(a)
or (d).
1194
1195
4)
Until June 30, 2012, as an alternative
to demonstrating compliance with
1196
the emissions standards in this subsection
(d),
the owner or operator
of an
1197
EGU may elect to comply with
the emissions testing requirements in
1198
Section
225.239(c),
(d),
(e),
(f)(1)
and
(2),
(h)(2),
(i)(3)
and
(4),
and
(j)(1)
1199
of this Subpart.
1200
1201
e)
Emission Standards for
NO
and
SO
2.
1202
1203
1)
NO
Emission Standards.
1204
1205
A)
Beginning in calendar
year
2012
and continuing in each calendar
1206
thereafter, for the EGUs in each MPS Group, the owner
and
1207
operator of the
EGUs must comply with an overall
NO
annual
1208
emission rate of no more
than 0.11 lb/million Btu or an emission
1209
rate equivalent to 52 percent of the Base
Annual Rate of
NO
1210
emissions, whichever is more stringent.
1211
1212
B)
Beginning in the 2012
ozone season and continuing in each
ozone
1213
season thereafter, for the EGUs
in each MPS Group, the owner and
JCAR350225-08 1 8507r01
1214
operator of the EGUs must
comply with an overall
NO
seasonal
1215
emission rate
of no more than 0.11 lb/million Btu or an
emission
1216
rate equivalent to
80
percent
of the Base Seasonal Rate of
NO
1217
emissions, whichever is more stringent.
1218
1219
2)
SO
2
Emission Standards.
1220
1221
A)
Beginning in calendar year 2013 and continuing in
calendar year
1222
2014, for the
EGUs in each MPS Group, the owner and operator
of
1223
the EGUs must comply with
an overall SO
2 annual emission
rate
1224
of
0.33
lb/million
Btu
or a rate equivalent to 44 percent of
the Base
1225
Rate of
SO
2
emissions, whichever
is more stringent.
1226
1227
B)
Beginning in calendar year 2015 and continuing in
each calendar
1228
year thereafter,
for the EGUs in each MPS Grouping, the owner
1229
and
operator of the EGUs must comply with an overall
annual
1230
emission rate for
SO
2 of 0.25 lbs/million Btu or a rate equivalent
to
1231
35
percent of the Base Rate of
SO
2
emissions, whichever
is more
1232
stringent.
1233
1234
3)
Compliance with the
NO
and
SO
2
emission standards
must be
1235
demonstrated
in accordance with Sections 225.310, 225.410,
and 225.510.
1236
The owner or
operator of EGUs must complete the demonstration
of
1237
compliance before
March
1 of the following year for annual standards
and
1238
before November 1 for seasonal standards,
by which date a compliance
1239
report must be submitted to the Agency.
1240
1241
f)
Requirements for
NO
and
SO
2
Allowances.
1242
1243
1)
The owner or operator of EGUs in an MPS Group must not
sell or trade
to
1244
any person or otherwise
exchange
with or give to any person
NO
1245
allowances allocated
to the EGUs in the MPS Group for vintage
years
1246
2012 and beyond that would otherwise
be
available
for sale, trade, or
1247
exchange
as a result
of actions taken to comply with the standards
in
1248
subsection (e) of this Section.
Such
allowances
that are not retired for
1249
compliance must be surrendered to the Agency on an annual
basis,
1250
beginning in calendar
year
2013. This provision does not apply
to the use,
1251
sale, exchange, gift, or
trade
of allowances
among the EGUs in an
MPS
1252
Group.
1253
1254
2)
The owners or
operators of EGUs in an MPS Group must not
sell or trade
1255
to any person or otherwise exchange
with or give to any person
SO
2
1256
allowances allocated to the
EGUs in
the
MPS Group for vintage years
JCAR350225-08
1 8507r01
1257
2013 and
beyond that
would otherwise be
available
for
sale or trade as a
1258
result
of actions taken
to comply with
the standards in subsection
(e) of
1259
this Section.
Such
allowances
that
are not
retired for compliance,
or
1260
otherwise
surrendered
pursuant to a consent
decree
to
which
the State
of
1261
Illinois is a party, must
be surrendered
to the Agency on
an annual basis,
1262
beginning
in calendar
year
2014.
This provision does
not apply to the
use,
1263
sale, exchange,
gift, or trade of allowances
among
the EGUs in an MPS
1264
Group.
1265
1266
3)
The provisions
of this subsection
(f) do not restrict
or inhibit the
sale or
1267
trading of allowances
that
become available from
one or more EGUs
in a
1268
MPS Group
as a result of holding
allowances
that represent over-
1269
compliance
with the
NO
or
2
SO standard in subsection
(e) of this Section,
1270
once such a standard
becomes
effective, whether such
over-compliance
1271
results from
control equipment, fuel
changes, changes
in the method
of
1272
operation, unit shut
downs,
or
other reasons.
1273
1274
4)
For purposes of
this
subsection
(f),
NO
and
SO
2
allowances
mean
1275
allowances
necessary
for compliance
with Subpart
W of Section 217
(NOX
1276
Trading Program
for Electrical
Generating Units)Sections
225.310,
1277
225.4 10, or
225.5
10,
40
CFR
72, Subparts or subparts
A through
IA and
1278
AAAA
of 40 CFR
96,
or any future federal
NO
or
SO
2
emissions
trading
1279
programs
that include Illinois
sources.
This Section does not
prohibit
the
1280
owner
or operator of
EGUs in an MPS
Group
from purchasing
or
1281
otherwise
obtaining
allowances from other
sources
as
allowed
by law for
1282
purposes of complying
with
federal
or state requirements,
except
as
1283
specifically set forth
in this Section.
1284
1285
5)
Before March 1,
2010, and continuing
each year thereafter,
the owner
or
1286
operator of EGUs
in an MPS Group
must submit a report
to the
Agency
1287
that
demonstrates
compliance
with the
requirements
of this subsection
(f)
1288
for the previous calendar
year, and
which includes identification
of any
1289
allowances
that
have
been surrendered
to the
USEPA
or to the Agency
and
1290
any allowances that were
sold, gifted,
used,
exchanged,
or traded
because
1291
they
became
available
due to over-compliance.
All
allowances that are
1292
required to be surrendered
must
be
surrendered
by
August
31,
unless
1293
USEPA has not yet
deducted the allowances
from the
previous year.
A
1294
final
report
must
be submitted to the
Agency
by
August 31 of each year,
1295
verifying that
the actions described
in the initial report
have taken
place
1296
or, if such actions
have
not
taken place, an explanation
of all changes
that
1297
have occurred
and the reasons
for
such
changes.
If USEPA has not
1298
deducted
the
allowances
from the previous
year by August 31,
the final
JCAR350225-08 1 8507r01
1299
report must be due, and all
allowances required to be surrendered must
be
1300
surrendered,
within 30 days after such deduction
occurs.
1301
1302
g)
Notwithstanding 35 Ill. Adm.
Code
201 .146(hhh), until an EGU has complied
1303
with the applicable emission standards
of
subsections
(d) and (e) of this Section
1304
for 12
months, the
owner
or
operator of the EGU
must obtain
a construction
1305
permit
for any new or modified
air pollution control equipment that it proposes
to
1306
construct for control of emissions
of mercury,
NOR,
or
SO
2.
1307
1308
(Source: Amended at 33 Ill. Reg.
effective
1309
1310
Section
225.234 Temporary Technology-Based
Standard for EGUs at Existing Sources
1311
1312
a)
General.
1313
1314
1)
At a source with EGUs that
commenced commercial operation on or
1315
before December
31, 2008, for an EGU that meets the eligibility
criteria in
1316
subsection (b) of this Section,
the
owner or operator of the EGU may
1317
temporarily comply with the requirements
of
this Section
through June
30,
1318
2015, as an alternative
to compliance with the mercury emission
standards
1319
in Section 225.230,
as provided in subsections (c), (d), and (e) of this
1320
Section.
1321
1322
2)
An EGU that is complying with the emission control requirements
of this
1323
Subpart B
by operating pursuant to this Section may not be included
in a
1324
compliance demonstration involving
other EGUs during the period that
is
1325
operating pursuant to this Section.
1326
1327
3)
The owner or operator of an EGU that is complying with this
Subpart B
by
1328
means of the temporary
alternative emission standards of this Section
is
1329
not
excused
from any of the applicable monitoring, recordkeeping,
and
1330
reporting requirements
set
forth in
Sections
225 .240
through 225.290.
1331
1332
4
Until June 30, 2012,
as
an alternative
to the CEMS monitoring,
1333
recordkeeping,
and reporting requirements in Sections 225 .240
through
1334
225.290, the owner
or
operator
of an EGU may elect to comply with
the
1335
emissions
testing,
monitoring, recordkeeping, and reporting
requirements
1336
in Section
225 .239(c),
(d),
(e),
(f)(1)
and
(2), (h)(2),
(i)(3) and (4),
and
1337
(j)(1).
1338
1339
b)
Eligibility.
1340
To be eligible to operate an EGU pursuant to this Section,
the following criteria
1341
must be met
for the EGU:
JCAR350225-081 8507r01
1342
1343
1)
The
EGU is equipped and operated with the
air
pollution control
1344
equipment
or systems that include injection of halogenated activated
1345
carbon and either a cold-side
electrostatic precipitator or a fabric filter.
1346
1347
2)
The owner
or operator of the EGU is injecting halogenated activated
1348
carbon in an
optimum manner for control of mercury emissions, which
1349
must include injection of Aistrom,
Norit, Sorbent
Technologies, Calgon
1350
Carbon’s
FLUEPAC MC Plus, or other halogenated activated carbon
that
1351
the owner or operator
of the EGU has demonstrated to have similar or
1352
better effectiveness for control of mercury emissions, at least at the
1353
following rates set forth in
subsections (b)(2)(A) through (b)(2)(D) of this
1354
Section,
unless other provisions for injection of halogenated activated
1355
carbon are established in a federally
enforceable
operating permit issued
1356
for the EGU,
using an injection system designed for effective absorption
1357
of mercury, considering the configuration
of
the EGU and its ductwork.
1358
For the purposes
of this subsection (b)(2), the flue gas flow rate must
be
1359
determined for the point of sorbent injection
(provided,
however,
that this
1360
flow
rate may be assumed to be identical to the stack flow rate if the
gas
1361
temperatures
at the point of injection and the stack are normally within
1362
100° F) or may otherwise be calculated
from the stack flow rate, corrected
1363
for the difference in gas temperatures.
1364
1365
A)
For an EGU firing subbituminous coal, 5.0 lbs per million actual
1366
cubic feet.
1367
1368
B)
For an EGU firing bituminous coal, 10.0 lbs per million actual
1369
cubic feet.
1370
1371
C)
For an EGU firing a blend of subbituminous
and
bituminous
coal,
1372
a
rate that
is the weighted average of the above rates, based on
the
1373
blend of coal being fired.
1374
1375
D)
A rate or rates set on a unit-specific basis that are lower than
the
1376
rate specified
above to the extent that the owner or operator of
the
1377
EGU demonstrates that such rate
or rates are needed so that carbon
1378
injection would not increase particulate matter emissions or
1379
opacity
so as to threaten compliance with applicable regulatory
1380
requirements for particulate matter
or opacity.
1381
1382
3)
The total capacity of the EGUs that operate pursuant to this Section
does
1383
not
exceed the applicable of the following values:
1384
JCAR350225-081
8507r01
1385
A)
For
the
owner or operator
of more than
one existing source
with
1386
EGUs,
25 percent
of the total rated capacity,
in
MW,
of all
the
1387
EGUs at the existing
sources that it
owns or operates, other
than
1388
any
EGUs operating
pursuant
to
Section
225.235
of
this Subpart B.
1389
1390
B)
For the owner
or operator of only
a single existing source
with
1391
EGUs (i.e., City,
Water, Light
& Power, City of
Springfield, ID
1392
167120AA0;
Kincaid Generating
Station,
ID 021814AAB;
and
1393
Southern Illinois
Power Cooperative/Marion
Generating
Station,
1394
ID 199856AAC),
25 percent
of the total rated
capacity, in MW,
of
1395
the all the
EGUs
at the existing
sources, other than
any
EGUs
1396
operating
pursuant to Section 225.235.
1397
1398
c)
Compliance
Requirements.
1399
1400
1)
Emission
Control
Requirements.
1401
The owner or operator
of an EGU
that is operating pursuant
to this
Section
1402
must continue to
maintain and operate
the EGU
to comply
with the criteria
1403
for eligibility for
operation pursuant
to this Section, except
during an
1404
evaluation of the
current
sorbent,
alternative
sorbents
or other
techniques
1405
to control mercury
emissions, as
provided by subsection
(e) of this
1406
Section.
1407
1408
2)
Monitoring
and
Recordkeeping
Requirements.
1409
In addition
to complying
with all applicable
monitoring and
recordkeeping
1410
reporting requirements
in Sections 225 .240
through 225.290
or Section
1411
225.239(c),
(d),
(e), (f)(1)
and
(2), (h)(2),
and
i(3)
and
(4),
the
owner
or
1412
operator of an EGU operating
pursuant
to
this
Section must
also:
1413
1414
A)
Through December
31, 2012, it must
maintain
records
of the usage
1415
of activated
carbon, the exhaust
gas flow rate from the
EGU,
and
1416
the activated
carbon
feed rate, in pounds
per
million
actual cubic
1417
feet of exhaust
gas at the injection
point, on a weekly
average.
1418
1419
B)
Beginning
January 1, 2013, it must
monitor activated
carbon
feed
1420
rate to the EGU,
flue gas temperature
at
the point
of sorbent
1421
injection,
and exhaust gas flow
rate from the EGU, automatically
1422
recording this
data and the
activated carbon feed
rate, in pounds
1423
per million
actual
cubic
feet
of exhaust gas at
the injection point,
1424
on an
hourly average.
1425
1426
C)
If a blend
of bituminous
and subbituminous
coal is fired in the
1427
EGU,
it must maintain
records of the
amount of each type
of
coal
JCAR350225-081 8507r01
1428
burned and the required
injection
rate for injection of halogenated
1429
activated carbon, on a weekly basis.
1430
1431
3)
Notification and Reporting Requirements.
1432
In addition to complying with all applicable
reporting requirements in
1433
Sections 225.240
through 225.290 or Section 225.239(f)(1), (f)(2),
and
1434
(j)(1), the owner or
operator of an EGU operating pursuant to this Section
1435
must also submit the following notifications
and reports to the Agency:
1436
1437
A)
Written notification
prior to the month in which any of the
1438
following events will occur:
1439
1440
i)
The EGU will no longer be eligible to operate under
this
1441
Section due to a change
in operation;
1442
1443
ii)
The type of coal fired in
the EGU will change; the mercury
1444
emission
standard
with which the owner or operator is
1445
attempting to comply
for the EGU will change; or
1446
1447
iii)
Operation
under this Section will be terminated.
1448
1449
B)
Quarterly reports for the recordkeeping
and monitoring or
1450
emissions testing conducted pursuant to subsection (c)(2)
of this
1451
Section.
1452
1453
C)
Annual reports detailing activities
conducted for the EGU to
1454
further improve control of mercury emissions, including the
1455
measures taken during the past
year
and activities planned for the
1456
current year.
1457
1458
d)
Applications
to
Operate
under the Technology-Based Standard
1459
1460
1)
Application Deadlines.
1461
1462
A)
The owner
or operator of an EGU that is seeking to operate the
1463
EGU pursuant to this Section must
submit an application to the
1464
Agency
no later than three months prior to the date on which
1465
compliance with
Section 225.230 of this Subpart B would
1466
otherwise have to be demonstrated.
For example, the owner or
1467
operator of an EGU that is applying
to operate the EGU pursuant
1468
to this Section on June 30, 2010, when compliance with
applicable
1469
mercury emission
standards must be first demonstrated,
must apply
1470
by
March 31, 2010 to
operate under this Section.
JCAR350225-08 1 8507r01
1471
1472
B)
Unless the Agency
finds that the EGU is not eligible to operate
1473
pursuant to this Section or that
the application for operation
1474
pursuant
to
this
Section
does not meet the requirements
of
1475
subsection (d)(2)
of this Section, the owner or operator of the
EGU
1476
is authorized to operate
the
EGU pursuant to this Section
1477
beginning 60 days after receipt
of the application by the Agency.
1478
1479
C)
The owner or
operator of an EGU operating pursuant to this
1480
Section must reapply to operate pursuant
to this Section:
1481
1482
i)
If it operated the EGU pursuant to
this
Section 225.234
1483
during the
period of June 2010 through December 2012
and
1484
it seeks to operate the EGU pursuant to this Section
1485
225.234 during
the
period from January
2013
through
June
1486
2015.
1487
1488
ii)
If it is planning a physical change to or a change
in the
1489
method
of operation of the EGU, control equipment or
1490
practices for injection
of
activated
carbon that is expected
1491
to reduce the level of control of mercury emissions.
1492
1493
2)
Contents of Application.
1494
An application to operate
an EGU pursuant to this Section 225 .234
must
1495
be submitted as an application for a new or revised federally
enforceable
1496
operating
permit
for the EGU, and it must include the following
1497
documents and information:
1498
1499
A)
A formal request
to operate pursuant to
this
Section
showing
that
1500
the EGU is eligible to operate pursuant to this Section and
1501
describing the reason
for the request, the measures that have
been
1502
taken
for control
of mercury emissions, and factors preventing
1503
more effective control
of
mercury emissions
from
the
EGU.
1504
1505
B)
The applicable mercury emission standard
in Section
225
.230(a)
1506
with
which the owner or operator of the EGU is attempting
to
1507
comply and
a summary of relevant mercury emission data for
the
1508
EGU.
1509
1510
C)
If
a unit-specific
rate or rates for carbon injection are proposed
1511
pursuant
to subsection (b)(2) of this Section, detailed information
1512
to support the
proposed injection rates.
1513
JCAR350225-08 1 8507r01
1514
D)
An action plan
describing the measures that will be taken while
1515
operating
under
this Section to
improve control of mercury
1516
emissions.
This plan must address measures such as evaluation
of
1517
alternative forms or
sources of activated carbon, changes
to
the
1518
injection system, changes to
operation of the unit that affect the
1519
effectiveness
of mercury absorption and
collection, changes to the
1520
particulate
matter control device to improve performance,
and
1521
changes to other emission
control devices. For each measure
1522
contained
in the plan, the plan must
provide a detailed description
1523
of the specific
actions that are planned, the reason that the measure
1524
is
being pursued and the range
of improvement in control of
1525
mercury that
is
expected,
and the factors that affect the timing
for
1526
carrying
out the measure, together with the current
schedule
for the
1527
measure.
1528
1529
e)
Evaluation of Alternative Control Techniques
for Mercury Emissions.
1530
1531
1)
During an evaluation of the effectiveness
of the current sorbent,
1532
alternative
sorbent, or other technique to control mercury
emissions, the
1533
owner or operator
of an EGU operating pursuant to this Section need
not
1534
comply with the eligibility
criteria
for operation pursuant to this Section
as
1535
needed to carry out an evaluation of the
practicality and effectiveness
of
1536
such
technique, subject to the following limitations:
1537
1538
A)
The owner or
operator of the EGU must conduct the evaluation
in
1539
accordance with a formal evaluation
program
that it has submitted
1540
to the Agency
at least 30 days prior to beginning the evaluation.
1541
1542
B)
The duration
and scope of the formal evaluation program
must not
1543
exceed the duration and
scope reasonably needed to complete
the
1544
desired evaluation
of the alternative control technique, as
initially
1545
addressed by the owner or owner
in a support document that it
has
1546
submitted with
the formal evaluation program pursuant to
1547
subsection (e)(1)(A) of this Section.
1548
1549
C)
Notwithstanding 35 Ill. Adm.
Code 201.146(hhh), the owner
or
1550
operator
of the EGU must obtain a construction
permit for any new
1551
or modified
air pollution control equipment to be constructed
as
1552
part of the evaluation
of the alternative control technique.
1553
1554
D)
The
owner
or operator of the EGU
must
submit
a report to the
1555
Agency, no
later than 90 days after the conclusion
of the formal
JCAR350225-081
8507r01
1556
evaluation program describing the evaluation
that
was
conducted,
1557
and
providing
the results
of the formal evaluation program.
1558
1559
2)
If the
evaluation of the alternative control technique shows less
effective
1560
control
of mercury
emissions
from the EGU than achieved with the
prior
1561
control technique, the owner or
operator of the EGU must resume use
of
1562
the prior control technique. If the evaluation
of the
alternative
control
1563
technique
shows comparable control effectiveness, the owner or
operator
1564
of the EGU may either continue
to use the alternative control technique
in
1565
an optimum manner or resume use of the prior control technique.
If the
1566
evaluation of
the
alternative
control
technique shows more effective
1567
control of mercury emissions, the owner or operator
of
the EGU
must
1568
continue to use the alternative
control technique in an optimum manner,
if
1569
it continues to operate pursuant to this Section.
1570
1571
(Source:
Amended at
33 Ill. Reg.
effective
1572
1573
Section 225.235 Units
Scheduled
for Permanent Shut Down
1574
1575
a)
The emission standards of Section 225.230(a) are
not
applicable
to an EGU that
1576
will be permanently shut down as described in this Section:
1577
1578
1)
The owner or
operator of an EGU that relies on this Section must
1579
complete the following actions
before June 30, 2009:
1580
1581
A)
Have
notified the Agency that it is planning to permanently
shut
1582
down the EGU
by the applicable date specified in subsection
(a)(3)
1583
or (4)
of this Section. This notification must include a
description
1584
of the actions
that have already been taken to allow the shut down
1585
of
the
EGU and a description of the future actions that must
be
1586
accomplished to complete
the shut down of the EGU, with the
1587
anticipated
schedule for those actions and the anticipated date
of
1588
permanent shut down of the unit.
1589
1590
B)
Have applied for a construction
permit or be actively pursuing
a
1591
federally
enforceable agreement that requires the EGU
to be
1592
permanently
shut
down
in accordance with this Section.
1593
1594
C)
Have applied for revisions to the operating permits for
the EGU
to
1595
include
provisions that terminate the authorization to operate
the
1596
unit in accordance
with this Section.
1597
JCAR35022508
1
8507r01
1598
2)
The
owner or operator
of an EGU
that
relies
on this
Section must,
before
1599
June 30, 2010,
complete the following
actions:
1600
1601
A)
Have
obtained a construction
permit
or
entered into a federally
1602
enforceable
agreement
as described
in subsection (a)(1)(B)
of this
1603
Section;
or
1604
1605
B)
Have obtained revised
operating
permits in accordance
with
1606
subsection
(a)(1)(C)
of this Section.
1607
1608
3)
The plan
for
permanent
shut down of the EGU
must provide
for the
EGU
1609
to be
permanently shut down
by
no later
than the applicable
date
specified
1610
below:
1611
1612
A)
If the owner
or
operator of the EGU
is not constructing
a new EGU
1613
or other generating
unit to specifically
replace the existing
EGU,
1614
by December31,
2010.
1615
1616
B)
If the
owner or
operator of the EGU
is constructing
a new EGU
or
1617
other generating
unit to specifically
replace
the existing
EGU, by
1618
December3l,2011.
1619
1620
4)
The owner
or
operator of the EGU
must
permanently
shut down the
EGU
1621
by the date
specified in subsection
(a)(3) of this
Section, unless the
owner
1622
or operator submits
a demonstration
to the Agency
before the specified
1623
date showing
that circumstances
beyond its
reasonable control (such
as
1624
protracted delays
in construction
activity, unanticipated
outage
of another
1625
EGU, or
protracted shakedown
of a replacement
unit) have occurred
that
1626
interfere with
the
plan for
permanent shut down
of the EGU,
in which
case
1627
the Agency
may
accept the demonstration
as substantiated and extend
the
1628
date for shut
down
of the
EGU as follows:
1629
1630
A)
If the
owner
or operator
of the EGU is not
constructing
a new EGU
1631
or
other generating unit
to specifically
replace
the existing
EGU,
1632
for up
to one
year,
i.e., permanent shut
down of the
EGU
to occur
1633
byno
later than December31,
2011;
or
1634
1635
B)
If
the owner
or
operator of the EGU
is constructing
a new EGU
or
1636
other generating unit
to
specifically
replace the existing
EGU, for
1637
up to 18 months,
i.e., permanent
shutdown of the
EGU to occur
by
1638
no later
than
June 30, 2013; provided,
however,
that afler
1639
December
31, 2012, the existing
EGU must only
operate as a
back-
1CAR350225-081
8507r01
1640
up
unit to address periods when
the
new
generating
units are not
in
1641
service.
1642
1643
b)
Notwithstanding
Sections 225 .230 and 225.232, any
EGU
that
is not required to
1644
comply with Section 225.230
pursuant
to this Section must not be included
when
1645
detennining whether any other
EGUs at the source or other sources are in
1646
compliance with Section 225.230.
1647
1648
c)
If an EGU, for which the owner
or operator of the source has relied upon this
1649
Section in lieu of complying with Section 225.230(a)
is not permanently shut
1650
down as required
by
this Section,
the EGU must be considered to be a new
EGU
1651
subject to the emission standards in Section 225 .237(a) beginning
in the month
1652
after the EGU was required to
be permanently shut down, in addition to any
other
1653
penalties that may
be imposed for failure to permanently shut down the
EGU in
1654
accordance with this Section.
1655
1656
çj
An EGU that has completed the requirements
of subsection (a) of this Section
is
1657
exempt from
the
monitoring and testing requirements in Sections 225 .239
and
1658
225.240.
1659
1660
An EGU that is scheduled for permanent shut down pursuant to Section
1661
225.294(b) is exempt
from the monitoring and testing requirements in
Sections
1662
225.239 and 225 .240.
1663
1664
(Source: Amended at 33 Ill. Reg.
effective
1665
1666
Section
225.237 Emission Standards for New Sources
with EGUs
1667
1668
a)
Standards.
1669
1670
1)
Except as provided in Sections 225.238
and 225.239, theThe owner or
1671
operator of
a source with one or more EGUs, but that previously
had not
1672
had any EGUs that commenced
commercial operation before January
1,
1673
2009, must
comply
with one of the following emission standards
for each
1674
EGU on a rolling 12-month basis:
1675
1676
A)
An emission
standard of 0.0080 lb mercury/GWh gross electrical
1677
output; or
1678
1679
B)
A
minimum 90 percent reduction
of
input mercury.
1680
1681
2)
For this purpose, compliance
may be demonstrated using the equations
in
1682
Section 225.230(a)(2), (a)(3), or (b)(2).
JCAR350225-08
1 8507r01
1683
1684
b)
The
initial 12-month
rolling period
for which compliance with the emission
1685
standards of
subsection (a)(1) of this Section must
be
demonstrated
for a new
1686
EGU will commence
on
the
date that the initial performance testing
commences
1687
under
40
CFR 60.8test for the
mercury emission standard under 40 CFR 60.45a
1688
also commences. The CEMS required
by this Subpart B for mercury emissions
1689
from the
EGU must be certified prior to this date. Thereafier,
compliance must
be
1690
demonstrated on
a
rolling 12-month
basis based on calendar months.
1691
1692
(Source: Amended at
33 III. Reg.
effective
1693
1694
Section 225.238 Temporary
Technology-Based Standard for New Sources with
EGUs
1695
1696
a)
General.
1697
1698
1)
At a source with
EGUs that previously had not had any EGUs that
1699
commenced commercial operation before January
1, 2009, for an EGU
1700
that meets the eligibility
criteria in subsection (b) of this Section,
as an
1701
alternative to compliance with the
mercury emission standards in Section
1702
225.237,
the owner or operator of the EGU may
temporarily comply with
1703
the requirements
of this Section, through December 31, 2018, as
further
1704
provided in subsections
(c), (d), and (e) of this Section.
1705
1706
2)
An EGU that is complying with the
emission control requirements of
this
1707
Subpart B by operating pursuant to this Section
may not
be included in
a
1708
compliance demonstration
involving other EGUs at the source during
the
1709
period that the temporary technology-based
standard is in effect.
1710
1711
3)
The owner or operator of an EGU that
is complying with this Subpart
B
1712
pursuant to this Section
is not excused from applicable monitoring,
1713
recordkeeping, and reporting requirements
of Sections
225.240
through
1714
225.290.
1715
1716
4
Until June 30, 2012, as an alternative
to the CEMS monitoring,
1717
recordkeeping,
and reporting requirements in Sections 225 .240
through
1718
225.290, the owner or
operator of an EGU may elect
to
comply with
the
1719
emissions testing, monitoring, recordkeeping,
and reporting requirements
1720
in
Section
225 .239(c),
(d), (e),
(f)(1) and (2), (h)(2),
(i)(3)
and
(4),
and
1721
(j)(1).
1722
1723
b)
Eligibility.
1724
To be eligible to operate an EGU pursuant
to this Section, the following criteria
1725
must
be met
for
the
EGU:
JCAR350225-08 1 8507r01
1726
1727
1)
The EGU is subject to Best Available Control Technology (BACT)
for
1728
emissions
of
sulfur
dioxide,
nitrogen oxides, and particulate matter,
and
1729
the EGU is equipped and operated with the air pollution
control equipment
1730
or systems specified below, as applicable to the category
of
EGU:
1731
1732
A)
For
coal-fired boilers, injection of sorbent or other mercury control
1733
technique (e.g., reagent) approved
by
the Agency.
1734
1735
B)
For an
EGU
firing
fuel gas produced by coal gasification,
1736
processing of the raw fuel gas prior to combustion for removal
of
1737
mercury with
a system using a sorbent or other mercury control
1738
technique approved by the Agency.
1739
1740
2)
For
an EGU for which injection of a sorbent or other mercury control
1741
technique is required pursuant to subsection (b)(1) of this Section,
the
1742
owner or
operator of the EGU is injecting sorbent or other mercury control
1743
technique in an optimum manner for control of mercury emissions,
which
1744
must include injection of Aistrom, Norit, Sorbent Technologies, Calgon
1745
CarbontsFLUEPAC
MC Plus, or other sorbent or other mercury control
1746
technique that the owner or
operator of the EGU
demonstrates
to have
1747
similar or better effectiveness for control of mercury emissions,
at least at
1748
the rate set forth in the appropriate of subsections (b)(2)(A) through
1749
(b)(2)(C) of this Section, unless other provisions for injection of sorbent
or
1750
other mercury control
technique are established in a federally enforceable
1751
operating permit issued for the EGU, with an injection system
designed
1752
for effective absorption of mercury. For the purposes of this subsection
1753
(b)(2), the flue gas flow rate must
be
determined
for the point of sorbent
1754
injection or other mercury control technique (provided, however, that
this
1755
flow rate may be assumed to be identical
to
the stack flow rate
if the gas
1756
temperatures
at the point of injection and the stack are normally within
1757
100° F), or the flow rate may otherwise be calculated from the
stack flow
1758
rate, corrected for the
difference
in gas temperatures.
1759
1760
A)
For an EGU
firing subbituminous coal, 5.0 pounds per million
1761
actual cubic feet.
1762
1763
B)
For an EGU
firing bituminous coal, 10.0 pounds per million
actual
1764
cubic feet.
1765
1766
C)
For
an EGU firing a blend
of
subbituminous and bituminous
coal,
1767
a
rate
that is the weighted average of the above rates, based
on the
1768
blend of coal
being fired.
JCAR350225-081
8507r01
1769
1770
D)
A rate or rates set
on
a
unit-specific
basis that are lower than
the
1771
rate
specified in subsections (b)(2)(A), (B),
and (C) of this Section,
1772
to the extent that
the owner or operator of the
EGU demonstrates
1773
that such rate or
rates are needed so that sorbent injection
or other
1774
mercury control technique
would
not
increase
particulate
matter
1775
emissions
or opacity so as
to
threaten compliance
with
applicable
1776
regulatory requirements
for particulate matter or opacity
or
cause
a
1777
safety issue.
1778
1779
c)
Compliance Requirements.
1780
1781
1)
Emission Control Requirements.
1782
The owner or
operator of an EGU that is operating pursuant to
this Section
1783
must continue to maintain and operate the
EGU to comply with the criteria
1784
for eligibility for
operation under this Section, except during
an evaluation
1785
of the current sorbent, alternative sorbents,
or other techniques to control
1786
mercury emissions,
as provided by subsection (e) of this Section.
1787
1788
2)
Monitoring and Recordkeeping Requirements.
1789
In addition
to complying with all applicable monitoring and
1790
requirements in Sections 225.240 through
225.290
1791
or Section 225.239(c),
(d), (e), (f)(1)
and
(2), (h)(2),
and (i)(3) and (4),
the
1792
owner or operator of a new EGU
operating pursuant to this Section
must
1793
also:
1794
1795
A)
Monitor sorbent feed rate
to the EGU, flue gas temperature at
the
1796
point
of sorbent injection or other mercury control
technique, and
1797
exhaust gas flow rate from
the EGU,
automatically recording
this
1798
data
and the sorbent feed rate, in pounds per million
actual cubic
1799
feet of exhaust gas at the injection
point, on an hourly average.
1800
1801
B)
If a blend of bituminous and subbituminous
coal is fired in the
1802
EGU, maintain
records of the amount of each type of coal
burned
1803
and the required injection rate for
injection of sorbent, on a weekly
1804
basis.
1805
1806
C)
If a mercury control technique
other than sorbent injection is
1807
approved by the Agency, monitor appropriate
parameter for that
1808
control
technique as specified by the Agency.
1809
1810
3)
Notification and Reporting Requirements.
JCAR350225-081 8507r01
1811
Tn
addition to complying with all applicable
reporting requirements
of
1812
Sections 225.240
through
225.290 or Section 225.239(f)(1) and (2)
and
1813
(j)(1),
the owner
or
operator
of an EGU operating pursuant to this
Section
1814
must
also submit the following notifications and
reports to the Agency:
1815
1816
A)
Written notification
prior
to the month in which any of the
1817
following events will occur:
the
EGU will no longer be eligible
to
1818
operate under this Section due to a change in operation;
the type
of
1819
coal fired
in the EGU will change; the mercury emission
standard
1820
with which the owner or operator
is
attempting
to comply for
the
1821
EGU
will change; or operation under this Section will be
1822
terminated.
1823
1824
B)
Quarterly reports for the recordkeeping and
monitoring or
1825
emissions testing
conducted
pursuant to subsection (c)(2) of
this
1826
Section.
1827
1828
C)
Annual reports detailing activities conducted
for
the
EGU to
1829
further improve
control of mercury emissions, including the
1830
measures taken during the past
year and activities planned for
the
1831
current year.
1832
1833
d)
Applications to Operate
under the Technology-Based Standard.
1834
1835
1)
Application Deadlines.
1836
1837
A)
The owner
or operator of an EGU that is seeking to operate
the
1838
EGU pursuant to this Section must
submit
an application to the
1839
Agency no
later than three months prior to the date that
1840
compliance with Section 225.237 would otherwise have
to be
1841
demonstrated.
1842
1843
B)
Unless the Agency finds that
the EGU is not eligible to operate
1844
pursuant
to this Section or that the application for operation
under
1845
this Section does not
meet
the requirements of subsection (d)(2)
of
1846
this Section, the owner or operator
of the EGU is authorized to
1847
operate the
EGU
pursuant to this Section beginning
60
days
after
1848
receipt of the application
by the Agency.
1849
1850
C)
The owner or operator of an EGU operating
pursuant to this
1851
Section must
reapply to operate pursuant to this Section if it
is
1852
planning a
physical change to or a change in the method of
1853
operation of the EGU, control
equipment,
or practices for injection
JCAR350225-08
1 8507r01
1854
of sorbent
or other mercury control technique that
is expected
to
1855
reduce the level
of control of mercury emissions.
1856
1857
2)
Contents of
Application.
1858
An application to
operate pursuant to this Section must be submitted
as an
1859
application for a new or revised
federally enforceable operating permit
for
1860
the new
EGU, and it must include the following
information:
1861
1862
A)
A formal request
to operate pursuant to this Section showing
that
1863
the
EGU is eligible to operate pursuant to this
Section and
1864
describing
the reason for the request, the measures that have
been
1865
taken
for control of mercury emissions, and factors
preventing
1866
more effective
control
of mercury emissions from the EGU.
1867
1868
B)
The applicable mercury
emission standard in Section 225.237
with
1869
which
the owner or operator of the EGU is attempting
to comply
1870
and a summary of relevant
mercury
emission data for the EGU.
1871
1872
C)
If a unit-specific
rate
or rates for sorbent or other mercury control
1873
technique injection are proposed pursuant
to subsection (b)(2)
of
1874
this
Section, detailed information to support the proposed
injection
1875
rates.
1876
1877
D)
An action plan
describing
the measures that will be taken while
1878
operating pursuant to this Section
to
improve
control
of mercury
1879
emissions.
This plan must address measures such as evaluation
of
1880
alternative forms
or sources of sorbent or other mercury control
1881
technique, changes to the injection system, changes
to operation
of
1882
the unit that affect
the
effectiveness of mercury absorption and
1883
collection,
and changes to other emission control devices.
For
1884
each measure contained in
the plan, the plan must provide a
1885
detailed
description of the specific actions that are planned,
the
1886
reason that the measure is being
pursued
and the range of
1887
improvement
in control of mercury that is expected, and
the factors
1888
that affect the timing for carrying
out the measure, with the current
1889
schedule
for the measure.
1890
1891
e)
Evaluation of Alternative Control Techniques
for Mercury Emissions.
1892
1893
1)
During an evaluation
of the effectiveness of the current
sorbent,
1894
alternative sorbent,
or other technique to control mercury emissions,
the
1895
owner or operator of an
EGU operating pursuant to this Section does
not
1896
need
to comply with the eligibility criteria for
operation pursuant to
this
JCAR350225-081
8507r01
1897
Section
as needed to carry out an
evaluation of the practicality and
1898
effectiveness
of such technique, further subject
to
the
following
1899
limitations:
1900
1901
A)
The owner or operator of the
EGU must conduct the evaluation
in
1902
accordance
with a formal evaluation
program
that it has submitted
1903
to
the
Agency at least 30 days prior to beginning the evaluation.
1904
1905
B)
The
duration and scope of the
formal evaluation program must
not
1906
exceed the
duration and scope reasonably needed to complete
the
1907
desired evaluation of the alternative
control technique, as initially
1908
addressed
by the owner or operator in a support document
that it
1909
has submitted with the formal
evaluation program pursuant to
1910
subsection (e)(1)(A)
of this Section.
1911
1912
C)
Notwithstanding 35 Ill.
Adm. Code 201.146(hhh), the owner
or
1913
operator of the EGU must obtain a construction
permit for any
new
1914
or modified air pollution
control equipment to be constructed
as
1915
part of the evaluation of the alternative
control technique.
1916
1917
D)
The owner
or operator of the EGU must submit a report to
the
1918
Agency no later than
90 days after the conclusion of the formal
1919
evaluation program describing
the evaluation that was conducted
1920
and providing the results of the formal evaluation
program.
1921
1922
2)
If the evaluation of the alternative
control technique shows less effective
1923
control of mercury emissions from the EGU
than
was achieved
with the
1924
prior control technique,
the owner or operator
of the EGU must resume
1925
use of the prior control technique. If the evaluation
of the alternative
1926
control technique shows
comparable effectiveness, the owner or
operator
1927
of the EGU may either continue to use the alternative control
technique
in
1928
an optimum manner or resume use
of the prior control technique. If
the
1929
evaluation of
the alternative control technique shows more effective
1930
control of mercury emissions, the
owner or operator of the EGU must
1931
continue to
use the alternative control technique in an optimum
manner,
if
1932
it continues to operate pursuant
to this Section.
1933
1934
(Source: Amended at 33
Ill.
Reg.
effective
1935
1936
Section
225.239 Periodic Emissions Testing Alternative
Requirements
1937
1938
General.
1939
JCAR350225-081 8507r01
1940
jJ
As an alternative to demonstrating
compliance
with
the emissions
1941
standards of Sections
225.230(a) or 225.237(a), the owner
or
operator
of
1942
an EGU may elect
to demonstrate compliance pursuant to the emission
1943
standards in subsection
(b)
of this
Section
and
the
use of quarterly
1944
emissions testing
as an alternative to the use of
CEMS:
1945
1946
)
The owner or
operator
of an EGU that elects to demonstrate compliance
1947
pursuant to this Section must comply with the testing,
recordkeeping,
and
1948
reporting requirements
of this Section in addition to other applicable
1949
recordkeeping and reporting
requirements
in
this
Subpart:
1950
1951
The alternative method
of compliance provided under this subsection
may
1952
only be
used until June 30, 2012, after which a CEMS certified in
1953
accordance with Section 225.250
of
this
Subpart
B
must be used.
1954
1955
4
If an owner or operator of an EGU demonstrating compliance
pursuant
to
1956
Section 225.230
or
225.237
discontinues use of CEMS before collecting
a
1957
full 12 months of CEMS
data
and elects
to demonstrate compliance
1958
pursuant to this Section, the data collected prior to that point must
be
1959
averaged to
determine compliance for such period. In such case, for
1960
purposes of calculating
an emission standard or mercury control efficiency
1961
using the equations in Section 225.230(a)
or
(b),
the
t?12?I
in the equations
1962
will be replaced by a variable equal to the number of full
and
partial
1963
months for which the owner or operator collected CEMS data.
1964
1965
})
Emission Limits.
1966
1967
j)
Existing Units: Beginning July
1,
2009,
the owner or operator of a source
1968
with one or more EGUs
subject
to this Subpart B that commenced
1969
commercial operation on or before
June 30,
2009,
must comply with
one
1970
of the following standards for each EGU, as determined through
quarterly
1971
emissions testing according to subsections (c),
(d), (e),
and
(f)
of this
1972
Section:
1973
1974
)
An
emission standard of 0.0080 lb
mercury/GWh
gross electrical
1975
output:
or
1976
1977
)
A
minimum
90-percent reduction of input mercury.
1978
1979
)
New Units: Beginning within the first 2,160
hours after the
1980
commencement of commercial operations, the owner or
operator of a
1981
source with one or more EGUs subject to this Subpart B that commenced
1982
commercial
operation after
June
30, 2009, must comply with one of
the
JCAR350225-081
8507r01
1983
following
standards
for each EGU,
as
determined through quarterly
1984
emissions testing
in accordance with subsections (c),
(d),
(e), and
(f)
of
1985
this Section:
1986
1987
An emission
standard of 0.0080 lb
mercury/GWh
gross electrical
1988
output; or
1989
1990
A
minimum
90-percent reduction of input mercury.
1991
1992
c).
Initial Emissions Testing Requirements for New Units. The owner or
operator
of
1993
an EGU that commenced
commercial operation after June 30, 2009, and that is
1994
complying by means of this Section must conduct an initial performance
test in
1995
accordance with the requirements
of subsections
(d)
and
(e)
of this Section within
1996
the
first 2,160 hours
after the commencement of commercial operations.
1997
1998
)
Emissions Testing
Requirements
1999
2000
Subsequent to the initial performance test, emissions tests must
be
2001
performed on a quarterly
calendar basis in accordance with the
2002
requirements of subsections (d), (e), and (f) of this Section;
2003
2004
Notwithstanding
the provisions in subsection
(d)(1),
owners or operators
2005
of EGUs demonstrating
compliance under
Section
225.233
or Sections
2006
225.29 1 through 225.299
must
perform
emissions testing on a semi-annual
2007
calendar basis, where the
periods
consist
of the months of January
through
2008
June
and July through December, in accordance with the requirements
of
2009
subsections
(d), (e),
and
(f)(1)
and (2)
of this Section;
2010
2011
fl
Emissions tests which demonstrate
compliance with this Subpart must
be
2012
performed at least 45 days apart. However, if an emissions test fails
to
2013
demonstrate
compliance
with
this Subpart or the emissions
test
is being
2014
performed
subsequent
to a significant change in the operations of an
EGU
2015
under subsection
(h)(2)
of this Section, the owner or operator
of an EGU
2016
may
perform
additional emissions tests using the same test
protocol
2017
previously submitted in the same period, with less than 45
days in between
2018
emissions
tests;
2019
2020
4
A minimum of three and a maximum of nine emissions
test
runs, lasting
at
2021
least one hour each, shall be conducted and averaged to determine
2022
compliance.
All test runs performed will be reported.
2023
2024
If the EGU shares a common
stack
with
one or more other EGUs, the
2025
owner or operator of the EGU will conduct emissions
testing
in the duct to
JCAR350225-081 8507r01
the common stack
from each unit, unless the owner or operator
of the
EGU considers the combined emissions
measured
at
the common stack
as
the mass emissions
of mercury for the EGUs for recordkeeping
and
compliance purposes.
)
If an
owner
or operator of an EGU demonstrating compliance
pursuant
to
this
Section
later elects to demonstrate compliance pursuant to
the CEMS
monitoring provisions
in
Section 225.240
of this Subpart, the owner
or
operator must comply with the emissions
monitoring
deadlines in Section
225.240(b)(4)
of this Subpart.
ci
Emissions Testing Procedures
j)
The owner or operator
must conduct a compliance test in accordance
with
Method
29,
30A, or 30B of 40 CFR 60, Appendix A, as incorporated
by
reference in Section 225.140;
)
Mercury emissions
or control efficiency must be measured while the
affected unit is operating at or above
90% of
peak
load;
For units complying
with the control efficiency standard of subsection
(b)(1)(B)
or (b)(2)(B)
of this Section, the owner or operator must perform
coal sampling as follows:
)
in accordance with Section 225.265 of this Subpart at least
once
during each day
of testing; and
)
in accordance
with Section 225 .265 of this Subpart, once each
month in those months when emissions testing
is not performed;
4)
For units complying with the output-based emission standard
of
subsection (b)(1’)(A) or (b)(2)(A)
of this Section, the owner or operator
must
monitor
gross electrical output for the duration of the testing.
The
owner or
operator of an EGU may use an alternative
emissions
testing
method
if such alternative
is submitted to the Agency in writing and
approved in writing by the Manager
of
the Bureau
of Air’s Compliance
Section.
Notification Requirements
1)
The owner or operator of an EGU must submit
a
testing
protocol as
described
in USEPA’s Emission Measurement Center’s Guideline
2026
2027
2028
2029
2030
2031
2032
2033
2034
2035
2036
2037
2038
2039
2040
2041
2042
2043
2044
2045
2046
2047
2048
2049
2050
2051
2052
2053
2054
2055
2056
2057
2058
2059
2060
2061
2062
2063
2064
2065
2066
2067
2068
JCAR350225-08
1 8507r01
2069
Document
#42 to the
Agency
at least
45 days prior to a
scheduled
2070
emissions
test,
except
as provided in Section
225.239(h)(2)
and
(h)(3).
2071
Upon written request
directed
to the
Manager of the Bureau
of Air’s
2072
Compliance Section,
the Agency
may, in its sole discretion,
waive
the 45-
2073
day
requirement.
Such waiver shall
only be effective
if it
is
provided
in
2074
writing and
signed by the Manager
of the Bureau
of
Air’s Compliance
2075
Section,
or his
or her designee;
2076
2077
)
Notification
of a scheduled
emissions
test must
be submitted to
the
2078
Agency
in writing,
directed
to the Manager
of the Bureau of Air’s
2079
Compliance
Section, at least
30 days prior to the
expected date
of the
2080
emissions
test.
Upon
written
request directed
to the Manager of the
Bureau
2081
of Air’s
Compliance Section,
the
Agency may,
in its sole discretion,
2082
waive
the
30-day notification
requirement. Such
waiver
shall
only
be
2083
effective if it
is provided
in writing and signed
by the Manager of the
2084
Bureau
of Air’s Compliance Section,
or his or her designee.
Notification
of
2085
the actual date
and expected
time
of testing must
be submitted in writing,
2086
directed
to the Manager of the
Bureau
of
Air’s
Compliance Section,
at
2087
least five
working days prior
to the actual date
of the
test:
2088
2089
J
For
an EGU that has elected
to demonstrate
compliance
by use
of the
2090
emission standards of
subsection
(b)
of this
Section,
if an
emissions
test
2091
performed under
the requirements of this
Section fails to demonstrate
2092
compliance with
the limits of subsection
(b)
of this Section,
the
owner
or
2093
operator
of an EGU
may perform
a new emissions test
using the same
test
2094
protocol previously
submitted in the
same period,
by notifying the
2095
Manager
of the Bureau of Air’s
Compliance Section
or his or her
designee
2096
of the actual
date and
expected time
of testing at
least five working days
2097
prior
to
the
actual date of the test.
The Agency may,
in its sole discretion,
2098
waive this five-day
notification requirement.
Such
waiver shall only
be
2099
effective if it is
provided in writing
and signed by the
Manager
of
the
2100
Bureau of Air’s
Compliance Section,
or his or her
designee;
2101
2102
4
In addition to
the testing protocol
required
by
subsection
(f)(1)
of this
2103
Section, the owner
or operator
of an EGU that has elected
to demonstrate
2104
compliance by
use of the emission
standards
of
subsection
(b)
of this
2105
Section
must submit a Continuous
Parameter Monitoring
Plan
to
the
2106
Agency at least
45
days prior
to a scheduled emissions
test.
Upon
written
2107
request directed
to
the
Manager
of
the
Bureau
of Air’s Compliance
2108
Section,
the
Agency may,
in
its
sole discretion,
waive the 45-day
2109
requirement. Such waiver
shall only be effective
if it
is
provided
in writing
2110
and
signed by the
Manager of the Bureau
of Air’s Compliance
Section, or
2111
his or her designee.
The Continuous
Parameter Monitoring
Plan must
JCAR350225-08
1
8507r01
2112
detail how the EGU will
continue to operate within the parameters
2113
enumerated in the testing protocol
and how those parameters will ensure
2114
compliance with the
applicable mercury limit. For example, the
2115
Continuous Parameter
Monitoring Plan must include coal sampling
as
2116
described in Section 225.239(e)(3)
of this Subpart and must ensure that
an
2117
EGU that performs an emissions test
using
a
blend
of coals continues to
2118
operate using that
same blend of coal. If the Agency disapproves
the
2119
Continuous Parameter Monitoring
Plan, the owner or
operator
of the
EGU
2120
has 30 days from the date of receipt
of the
disapproval
to
submit
more
2121
detailed information
in accordance with the Agency’s
request.
2122
2123
gI
Compliance Determination
2124
2125
fl
Each quarterly emissions
test
shall determine compliance with this
2126
Subpart for that quarter, where the quarterly periods consist of
the months
2127
of January through March,
April through June, July through September,
2128
and October through
December:
2129
2130
J
If emissions testing conducted pursuant to this
Section
fails to demonstrate
2131
compliance,
the owner or operator of the EGU will be deemed
to have
2132
been out of compliance
with this Subpart beginning on the day after
the
2133
most recent emissions
test
that demonstrated compliance or the last
day of
2134
certified
CEMS data demonstrating compliance
on a rolling 12-month
2135
basis,
and the EGU will remain out of compliance until
a subsequent
2136
emissions
test successfully demonstrates compliance with the limits
of this
2137
Section.
2138
2139
)
Operation Requirements
2140
2141
The owner or
operator
of an EGU that has elected to demonstrate
2142
compliance
by use of the emission standards of subsection
(b)
of this
2143
Section must continue
to operate the EGU commensurate with the
2144
Continuous
Parameter Monitoring Plan until another Continuous
2145
Parameter Monitoring Plan is developed
and submitted to the Agency
in
2146
conjunction
with
the next compliance demonstration, in accordance
with
2147
subsection
(f)(4)
of this Section.
2148
2149
)
If the
owner
or operator makes a significant change to the
operations of
an
2150
EGU
subject
to this Section, such as changing from bituminous
to
2151
subbituminous coal,
the
owner
or operator must submit a testing protocol
2152
to the Agency and perform an emissions
test within
seven
operating
days
2153
of the significant change. In addition, the owner
or
operator
of an EGU
2154
that
has elected
to demonstrate compliance by use of the emission
JCAR350225-0818507r01
2155
standards of subsection
(b)
of
this
Section must submit
a
Continuous
2156
Parameter
Monitoring
Plan within
seven
operating
days of the significant
2157
change.
2158
2159
)
If a
blend
of bituminous and
subbituminous
coal is fired in the EGU,
the
2160
owner or
operator of the
EGU must ensure
that
the EGU continues
to
2161
operate
using the
same
blend that was used
during the
most
recent
2162
successful
emissions test.
If
the
blend
of coal changes, the owner
or
2163
operator of the EGU
must re-test in accordance
with
subsections
(d),
(e),
2164
(f),
and (g) of this
Section
within 30 days
of the change in coal
blend,
2165
notwithstanding
the
requirement of
subsection
(d)(3)
of
this Section that
2166
there
must be 45
days between emissions
tests.
2167
2168
recordkeeping
2169
2170
j)
The
owner or operator of
an EGU
and
its designated representative
must
2171
comply
with
all applicable
recordkeeping
and reporting requirements
in
2172
this
Section.
2173
2174
)
Continuous
Parameter
Monitoring. The
owner or operator of
an
EGU
2175
must maintain
records to substantiate
that the EGU is operating
in
2176
compliance with
the parameters listed
in the Continuous
Parameter
2177
Monitoring
Plan, detailing the parameters
that
impact
mercury reduction
2178
and
including
the following records
related
to the
emissions
of mercury:
2179
2180
For an EGU for which
the owner or
operator
is complying
with
2181
this Subpart B
pursuant
to Section 225.239(b)(1)(B)
or
2182
225.239(b)(2)(B),
records of the daily
mercury content of
coal
2183
used
(lbs/trillion Btu)
and the daily and
quarterly input
mercury
2184
(ibs).
2185
2186
For an EGU for which
the owner
or
operator
of an EGU
complying
2187
with
this Subpart
B pursuant to Section
225.239(b)(1)(A)
or
2188
225.239b)(2)(A),
records
of the daily
and quarterly oss
2189
electrical
output
(MWh)
on an hourly basis.:
2190
2191
The
owner or
operator
of
an EGU using activated
carbon
injection
must
2192
also
comply
with the
following requirements:
2193
2194
Maintain records
of
the
usage
of sorbent, the exhaust
gas flow
rate
2195
from the
EGU, and the sorbent
feed rate, in
pounds per million
2196
actual
cubic
feet of exhaust
gas at
the
mi ection
point,
on a weekly
2197
average
JCAR350225-08 1 8507r01
2198
2199
)
If a blend of bituminous
and subbituminous
coal is fired
in
the
2200
EGU, keep
records
of
the
amount
of each type of coal
burned
and
2201
the required
injection
rate for injection
of activated
carbon, on a
2202
weekly basis.
2203
2204
41
The owner or operator
of an
EGU
must retain all records
required by
this
2205
Section
at the
source
unless otherwise
provided in the
CAAPP permit
2206
issued for the source
and
must
make
a copy of any
record available
to the
2207
Agency
promptly
upon request.
2208
2209
)
The owner or
operator
of an EGU
demonstrating
compliance
pursuant
to
2210
this Section must
monitor
and
report the heat input
rate at the unit level.
2211
2212
The owner or operator
of an EGU
demonstrating compliance
pursuant
to
2213
this
Section
must
perform
and report
coal sampling in accordance
with
2214
subsection 225.23
9(e)(3).
2215
2216
Reporting
Requirements
2217
2218
1)
An
owner
or operator of an EGU
shall submit
to
the
Agency a Final
2219
Source Test
Report
for each
periodic emissions
test within 45
days afler
2220
the test
is completed.
The
Final Source Test
Report will be directed
to the
2221
Manager
of the Bureau
of Air’s Compliance
Section, or his or
her
2222
designee, and include
at a minimum:
2223
2224
)
A summary of
results;
2225
2226
A description
of
test methods,
including
a description
of
sampling
2227
points, sampling
train,
analysis
equipment,
and
test schedule,
and a
2228
detailed description
of test
conditions, including:
2229
2230
j).
Process
information, including
but not limited
to modes
of
2231
operation,
process rate,
and fuel or raw material
2232
consumption;
2233
2234
li)
Control
equipment
information
(i.e., equipment
condition
2235
and
operating parameters
during testing);
2236
2237
iiil
A discussion of
any preparatory actions
taken
(i.e.,
2238
inspections,
maintenance,
and repair);
and
2239
JCAR350225-081
8507r01
2240
jy
Data and
calculations, including copies
of all raw data
2241
sheets
and records of laboratory
analyses, sample
2242
calculations,
and data on equipment calibration.
2243
2244
)
The owner or operator of
a
source
with one or more EGUs demonstrating
2245
compliance
with
Subpart B in accordance
with
this Section must submit
to
2246
the Agency a Quarterly
Certification of Compliance within 45
days
2247
following the end of each
calendar quarter. Quarterly certifications
of
2248
compliance
must
certify
whether compliance
existed for each EGTJ for
the
2249
calendar quarter covered
by the certification. If the EGU failed
to comply
2250
during the quarter covered
by
the certification,
the owner or operator must
2251
provide the reasons
the EGU or EGUs failed to comply and a full
2252
description of the noncompliance
(i.e.,
tested emissions
rate, coal sample
2253
data,
etc.).
In addition, for
each EGU, the owner or operator must provide
2254
the
following
appropriate data to the Agency as set
forth
in
this Section.
2255
2256
A list
of all emissions tests performed within
the
calendar
quarter
2257
covered
by the Certification and submitted to the Agency for
each
2258
EGU, including the dates on which
such tests were performed.
2259
2260
)
Any
deviations or exceptions each month and discussion of
the
2261
reasons for such deviations
or exceptions.
2262
2263
c)
All
Quarterly
Certifications of Compliance
required to be
2264
submitted must include the following certification
by
a
responsible
2265
official:
2266
2267
I certify
under penalty of law that this document and all
2268
attachments were prepared under my direction
or supervision in
2269
accordance
with a system designed to assure that qualified
2270
personnel properly gather and evaluate the information
submitted.
2271
Based on my inquiry of the
person or persons directly responsible
2272
for
gathering the information, the information submitted
is, to the
2273
best of my knowledge and
belief, true, accurate, and complete.
I
2274
am aware that there are significant
penalties
for
submitting false
2275
information, including
the possibility of fine and imprisonment
for
2276
knowing
violations.
2277
2278
Deviation Reports.
For each EGU, the owner or operator must promptly
2279
notify
the Agency of deviations
from any of the requirements of this
2280
Subpart B. At a minimum, these notifications
must include a description
2281
of such deviations within 30 days after discovery
of the deviations, and
a
JCAR35O225O8
1 8507r01
2282
discussion of the possible cause
of such deviations, any corrective
actions,
2283
and
any
preventative
measures taken.
2284
2285
(Source: Added at 33 Ill. Reg.
effective
2286
2287
Section 225.240 General Monitoring and
Reporting Requirements
2288
2289
The owner or operator of an EGU must comply with the
monitoring, recordkeeping, and
2290
reporting requirements
as
provided in
this Section, Sections 225.250
through 225.290 of this
2291
Subpart B, and Sections 1.14 through 1.18 of Appendix
B to this PartSubpart I of 40
CFR 75
2292
(sections 75.80
through
75.84),
incorporated
by reference in Section 225.140.
If the EGU
2293
utilizes a common stack with units that are not EGUs and
the owner or operator
of
the
EGU does
2294
not
conduct
emissions monitoring
in
the
duct
to the common stack from
each EGU, the owner
or
2295
operator of the EGU must conduct emissions monitoring
in accordance with Section 1.1 6(b)(2)
2296
of
Appendix B to this Part 40 CFR 75.82(b)(2)
and this Section, including monitoring
in the duct
2297
to the common stack from each unit that is not an EGU, unless
the owner or operator of the
EGU
2298
counts
the combined emissions measured at the
common stack as the mass emissions
of mercury
2299
for the EGUs for recordkeeping and compliance purposes.
2300
2301
a)
Requirements for installation,
certification, and data accounting. The
owner or
2302
operator of each EGU must:
2303
2304
1)
Install all monitoring systems required pursuant
to this Section and
2305
Sections 225.250
through 225.290 for monitoring
mercury mass emissions
2306
(including
all systems required
to monitor mercury concentration,
stack
2307
gas moisture content, stack gas flow rate,
and
CO
2
or
02
concentration,
as
2308
applicable, in accordance
with Sections 1.15 and 1.16
of Appendix B
to
2309
this Part4O CFR 75.81 and 75.82).
2310
2311
2)
Successfully complete all certification
tests required pursuant to
Section
2312
225.250 and meet all
other requirements of this Section,
Sections 225.250
2313
through
225.290,
and Sections 1.14 through
1.18 of Appendix B to
this
2314
Part subpart I of 40 CFR
75 applicable to the monitoring
systems required
2315
under subsection (a)(1) of this Section.
2316
2317
3)
Record, report, and assure the
quality of the data from the monitoring
2318
systems
required
under
subsection (a)( 1) of this
Section.
2319
2320
4)
If the owner or operator elects
to use the low mass emissions excepted
2321
monitoring methodology for
an EGU that emits no more than 464
ounces
2322
(29 pounds) of mercury per year pursuant
to Section
1.15(b)
of Appendix
2323
B to this
Part4O
CFR 75.8 1(b), it must perform emissions
testing in
2324
accordance
with Section
1.15(c)
of Appendix B to this Part 40
CFR
JCAR350225-08
1 8507r01
2325
75.81(c) to demonstrate
that the
EGU is eligible
to use this excepted
2326
emissions
monitoring
methodology,
as well as
comply with all other
2327
applicable requirements
of Section
1.15(b) through
(f)
of Appendix
B to
2328
this Part4O CFR
75.81(b)
through (f). Also, the
owner or
operator
must
2329
submit
a copy of any information
required
to be submitted to the
USEPA
2330
pursuant
to these provisions
to the
Agency.
The initial emissions
testing
2331
to demonstrate
eligibility
of an EGU for the
low
mass emissions
excepted
2332
methodology
must
be
conducted
by the
applicable of
the
following
dates:
2333
2334
A)
If the
EGU
has commenced commercial
operation
before July 1,
2335
2008,
at least
by
jpjyJanuary
1,
2009,
or
45 days
prior to relying
2336
on the
low
mass emissions excepted
methodology,
whichever
date
2337
is later.
2338
2339
B)
If the EGU has
commenced commercial
operation
on or after
July
2340
1, 2008, at least 45
days prior to
the applicable date
specified
2341
pursuant to subsection
(b)(2) of this
Section or 45
days prior
to
2342
relying
on
the low mass emissions
excepted methodology,
2343
whichever date
is later.
2344
2345
b)
Emissions
Monitoring
Deadlines. The owner
or operator must
meet the emissions
2346
monitoring
system certification
and other
emissions monitoring
requirements
of
2347
subsections (a)(1) and
(a)(2)
of
this Section
on or before
the applicable of the
2348
following dates.
The
owner or operator
must record,
report,
and quality-assure
2349
the data from
the emissions monitoring
systems required
under
subsection
(a)(1)
2350
of this Section
on and after
the
applicable of the following
dates:
2351
2352
1)
For the
owner
or operator
of an EGU that commences
commercial
2353
operation
before July 1, 2008,
by
jyJanuary
1, 2009.
2354
2355
2)
For
the owner or operator
of an EGU that
commences commercial
2356
operation
on or after
July
1, 2008, by 90 unit
operating days or
180
2357
calendar
days, whichever
occurs first, after the
date on which
the EGU
2358
commences
commercial
operation.
2359
2360
3)
For the
owner
or operator
of an EGU for which
construction
of a new
2361
stack
or flue or installation
of add-on mercury
emission controls,
a
flue
2362
gas desulfurization system,
a selective catalytic
reduction
system, a fabric
2363
filter,
or
a compact
hybrid particulate collector
system
is completed after
2364
the applicable
deadline
pursuant to
subsection (b)(1) or
(b)(2)
of this
2365
Section, by
90
unit
operating
days or 180 calendar days,
whichever
occurs
2366
first, after the
date on which emissions
first exit
to the atmosphere through
2367
the
new
stack
or flue, add-on
mercury emission
controls, flue gas
2368
2369
2370
2371
2372
2373
2374
2375
2376
2377
2378
2379
2380
2381
2382
2383
2384
2385
2386
2387
2388
2389
2)
2390
2391
2392
2393
2394
2395
2396
2397
2398
2399
2400
2401
2402
2403
2404
2405
2406
2407
2408
2409
JCAR350225-081 8507r01
desulfurization system,
selective catalytic reduction system, fabric
filter,
or compact hybrid particulate collector system.
4
For an owner or operator
of an EGU that originally elected to demonstrate
compliance pursuant to the emissions
testing requirements in Section
225.239,
by the first day of the calendar quarter following
the last
emissions
test
demonstrating
compliance with
Section 225.239.
c)
Reporting Data.
1)
Except as provided in subsection (c)(2)
of
this
Section,
the owner or
operator of an EGU that
does not meet the applicable emissions
monitoring date set forth in subsection
(b)
of this
Section
for
any
emissions monitoring system required
pursuant to subsection (a)( 1)
of this
Section
must begin periodic emissions testing in accordance with
Section
225.239, for each such monitoring
system,
the maximum
-
- fl-n-nm-n-n
fltp
determi,
fl
record, and report
-‘ia1
(or,
the minimum
notential)
values
for mercury concentration, the
stack gas flow rate, the stack gas moisture
content,
d any other parameters required to deteine mercury
mass
emissions in accordance with 40
CFR 75.80(g).
The owner or operator of an EGU that
does not meet the applicable
emissions monitoring
date set forth in subsection
(b)(3) of this Section
for
any emissions monitoring system required pursuant to subsection
(a)(1)
of
this Section must begin
periodic emissions testing in accordance with
Section
225.239, for each such monitoring
system, deteine, record,
and
report
substitute
data using the applicable missing data procedures
as set
forth in 40 CFR 75.80(f), in lieu
of the maximum potential (or, as
appropriate,
minimum potential) values for a parameter, if the
owner or
operator demonstrates that there
is continuity between the data streams
for
1,nf
-nnrnmptpm
pfyp nr1 nftr
f1p
ntrnrHn
installation
pursuant
to
subsection(b)(3) of this Section.
d)
Prohibitions.
1)
No owner or operator of an
EGU
may
use any alternative emissions
monitoring system, alternative reference method for
measuring emissions,
or
other alternative
to the emissions monitoring and measurement
requirements
of this Section
and Sections 225.250 through 225.290,
unless
such alternative is submitted
to
the
Agency in writing and approved in
writing by the Manager of the Bureau
of
Air’s Compliance
Section, or his
or her
designeepromulgated
by
the USEPA and approved
in
writing
by the
JCAR350225-0818507r01
2410
Agency, or the
use of such alternative is approved
in writing by the
2411
Anc’v
and USEPA.
2412
2413
2)
No
owner or operator
of an EGU may operate its
EGU so as to discharge,
2414
or allow to be discharged,
mercury emissions to the atmosphere
without
2415
accounting for all such emissions
in accordance with the applicable
2416
provisions
of this Section, Sections 225.250
through 225.290, and
2417
Sections 1.14
through
1.18 of Appendix B to this Part, unless
2418
demonstrating compliance
pursuant
to Section 225.239, as
2419
applicablesubpart
I of 40 CFR 75.
2420
2421
3)
No owner or operator of an EGU may disrupt the
CEMS,
any portion
2422
thereof,
or any other approved
emission monitoring method, and thereby
2423
avoid monitoring
and recording mercury mass emissions discharged
into
2424
the atmosphere, except for periods
of
recertification
or periods when
2425
calibration,
quality assurance testing, or maintenance is performed
in
2426
accordance with the applicable provisions
of this Section, Sections
2427
225.250 through
225.290, and Sections 1.14 through 1.18
of Appendix B
2428
to this Partsubpart I of 40
CFR ‘75.
2429
2430
4)
No owner or operator of an EGU may retire or permanently
discontinue
2431
use of the
CEMS or any component thereof, or any other approved
2432
monitoring system
pursuant to this Subpart B, except under any one
of the
2433
following circumstances:
2434
2435
A)
The
owner or operator is monitoring emissions from the
EGU with
2436
another certified monitoring
system that has been approved, in
2437
accordance
with the applicable provisions of this
Section, Sections
2438
225.250 through 225.290
of this Subpart B, and Sections 1.14
2439
through
1.18 of Appendix B to this Partsubpart I
of
40
CFR 75,
by
2440
the Agency for use at that
EGU
and that provides emission data
for
2441
the
same
pollutant or parameter as the retired or discontinued
2442
monitoring system; or
2443
2444
B)
The owner or operator or designated
representative submits
2445
notification
of the date of certification
testing
of a replacement
2446
monitoring
system for the retired or discontinued monitoring
2447
system in accordance with Section 225.250(a)(3)(A).
2448
2449
The
owner or operator is demonstrating compliance
pursuant
to the
2450
applicable
subsections
of Section 225.239.
2451
2452
e)
Long-term Cold Storage.
JCAR350225-081 8507r01
2453
The owner or operator of an EGU that is in
long-term cold storage is subject to
2454
the provisions
of
40
CFR
75.4
and
40
CFR 75.64, incorporated
by
reference
in
2455
Section 225.140, relating to monitoring, recordkeeping,
and reporting for units
in
2456
long-term cold storage.
2457
2458
(Source:
Amended at 33 Ill. Reg.
effective
2459
2460
Section 225.250 Initial
Certification
and Recertification Procedures for Emissions
2461
Monitoring
2462
2463
a)
The
owner or operator
of an EGU must comply with the following initial
2464
certification and recertification procedures
for
a
CEMS (i.e., a CEMS or an
2465
excepted monitoring system
(sorbent trap monitoring system) pursuant to
Section
2466
1.3 of Appendix B to this Part4O CFR 75.15, incorporated
by reference in Section
2467
225.140) required
by
Section 225.240(a)(1).
The owner or operator of an
EGU
2468
that qualifies for, and for which the owner or operator elects to
use, the low-mass-
2469
emissions excepted methodology pursuant
to Section 1.15(b) of Appendix B
to
2470
this
Part4O
CFR 75.8 1(b), incorporated
by
reference in Section 225.140,
must
2471
comply
with
the procedures
set forth in subsection (c) of this Section.
2472
2473
1)
Requirements for Initial Certification. The
owner or operator of an EGU
2474
must ensure that, for each CEMS required
by
Section 225.240(a)(1)
2475
(including the automated data acquisition and handling system),
the
owner
2476
or operator successfully
completes all of the initial certification testing
2477
required pursuant to Section 1.4
of Appendix B to this Part4O CFR
2478
75.80(d), incorporated by reference in Section 225.140,
by
the
applicable
2479
deadline in Section 225.240(b).
In addition, whenever the owner or
2480
operator of an EGU installs a monitoring
system to meet the requirements
2481
of
this Subpart B in a
location where no such monitoring system was
2482
previously installed, the owner or operator
must successfully complete
the
2483
initial certification requirements
of Section 1.4 of Appendix B to this
2484
Part4O
CFR 75.80(d).
2485
2486
2)
Requirements for Recertification. Whenever the owner or
operator of
an
2487
EGU
makes a replacement,
modification, or change in any certified
2488
CEMS,
or an excepted monitoring system
(sorbent
trap
monitoring
2489
system)
pursuant to
Section 1.3 of Appendix B to this Part4O CFR
75.15,
2490
and required by Section 225 .240(a)(1),
that may significantly affect
the
2491
ability of the system to accurately
measure
or record mercury mass
2492
emissions or heat
input rate or to meet the quality-assurance
and quality
2493
control requirements
of Section 1.5 of Appendix B to this Part 40
CFR
2494
75.21 or Exhibit B to Appendix
B to this PartAppendix B to 40
CFR 75,
2495
each incorporated by reference
in Section
225.140,
the
owner or operator
JCAR350225-08
1 8507r01
2496
of an EGU must recertify the
monitoring system in accordance
with
2497
Section
1.4(b) of Appendix B to this Part4O
CFR
75.20(b),
incorporated
2498
by reference in Section 225.140.
Furthermore, whenever the
owner or
2499
operator
of an EGU makes a replacement,
modification,
or change
to the
2500
flue gas
handling system or the EGU’s operation
that may significantly
2501
change the
stack flow or concentration profile, the
owner
or operator must
2502
recertify each CEMS, and
each excepted monitoring system
(sorbent trap
2503
monitoring system) pursuant to Section
1.3 to Appendix B to this Part4O
2504
CFR
75.15, whose accuracy is potentially affected
by the change, all in
2505
accordance with Section 1.4(b)
to
Appendix B to this Part4O
CFR
2506
75.20(b).
Examples of changes to a CEMS that
require recertification
2507
include, but are not limited to,
replacement of the analyzer, complete
2508
replacement
of an existing CEMS, or change in location
or orientation
of
2509
the sampling probe or site.
2510
2511
3)
Approval Process for Initial Certification
and Recertification. Subsections
2512
(a)(3)(A) through
(a)(3)(D) of this Section apply to both initial
2513
certification and recertification of
a CEMS required by Section
2514
225.240(a)(1).
For recertifications, the words “certification
and “initial
2515
certification” are to
be read as the word “recertification”, the word
2516
“certified” is to be read as the word
“recertified”, and the procedures
set
2517
forth
in Section
1.4(b)(5)
of Appendix
B to this Part 40 CFR 75.20(b)(5)
2518
are
to be followed in lieu of the procedures set
forth in subsection
2519
(a)(3)(E)
of this Section.
2520
2521
A)
Notification of Certification.
The
owner
or operator must submit
2522
written
notice
of the dates of certification testing
to the Agency
2523
directed to the Manager
of the Bureau of Air’s Compliance
2524
Section,
USEPA Region 5, and the Administrator
of the USEPA
2525
written notice of the dates
of certification testing, in accordance
2526
with
Section
225
.270.
2527
2528
B)
Certification Application.
The owner or operator must
submit
to
2529
the
Agency a certification application
for each monitoring
system.
2530
A complete
certification application must include
the information
2531
specified in 40 CFR 75.63,
incorporated by reference in Section
2532
225.140.
2533
2534
C)
Provisional Certification
Date. The provisional certification
date
2535
for a monitoring system
must be determined in accordance
with
2536
Section
1.4(a)(3)
of Appendix
B to
this Part4O
CFR 75.20(a)(3),
2537
incorporated
by reference in Section 225.140.
A
provisionally
2538
certified monitoring
system maybe used pursuant
to
this
Subpart
B
JCAR350225-08 1 8507r01
2539
for a period not to exceed 120
days after receipt by the Agency
of
2540
the complete
certification
application for the monitoring
system
2541
pursuant to subsection
(a)(3)(B) of this Section. Data
measured
2542
and recorded by the provisionally
certified monitoring system, in
2543
accordance
with
the requirements of Appendix
B to this Part4O
2544
CFR 75, will
be considered valid quality-assured data
(retroactive
2545
to the date and time
of
provisional
certification), provided
that the
2546
Agency does not invalidate the provisional
certification
by
issuing
2547
a notice of disapproval
within 120 days after the date
of receipt
by
2548
the Agency of the complete certification
application.
2549
2550
D)
Certification Application Approval
Process. The Agency
must
2551
issue a written notice
of approval or disapproval of
the certification
2552
application
to the owner or operator within
120 days after receipt
2553
of the complete certification
application required by subsection
2554
(a)(3)(B)
of this Section. Tn the event the Agency
does not issue
a
2555
written notice of approval or
disapproval within the 120-day
2556
period,
each
monitoring system that meets
the applicable
2557
performance requirements
of Appendix B to this Part 40
CFR 75
2558
and which is included in the certification
application will
be
2559
deemed certified for use pursuant
to
this
Subpart
B.
2560
2561
i)
Approval
Notice. If the certification application
is
2562
complete and
shows that each
monitoring system
meets
the
2563
applicable performance
requirements of Appendix B
to
this
2564
Part4O
CFR 75, then the Agency
must issue a written
notice
2565
of approval
of
the
certification application within 120
days
2566
after receipt.
2567
2568
ii)
Incomplete
Application
Notice.
If the certification
2569
application is not complete,
then
the Agency must
issue a
2570
written
notice of incompleteness that
sets a reasonable
date
2571
by which the owner
or operator must submit the additional
2572
information
required to complete the certification
2573
application. If the owner
or operator does not comply
with
2574
the
notice of incompleteness
by the specified date, the
2575
Agency may
issue a notice of disapproval
pursuant to
2576
subsection (a)(3)(D)(iii)
of this Section. The 120-day
2577
review period will not begin
before
receipt of a complete
2578
certification
application.
2579
2580
iii)
Disapproval
Notice. If the certification application
shows
2581
that any monitoring
system does not meet the performance
JCAR350225-08
1 8507r01
2582
requirements
of Appendix B to this
Part4O CFR
75, or if
2583
the certification
application is incomplete and
the
2584
requirement
for disapproval pursuant
to subsection
2585
(a)(3)(D)(ii)
of this Section is met, the
Agency must issue
a
2586
written notice
of disapproval of the certification
2587
application.
Upon issuance of such notice of
disapproval,
2588
the
provisional certification is invalidated,
and the data
2589
measured
and recorded by each uncertified
monitoring
2590
system will not
be considered valid quality-assured
data
2591
beginning
with
the date and hour
of provisional
2592
certification (as
defined pursuant to Section 1
.4(a)(3) of
2593
Appendix
B to this Part4O CFR 75.20(a)(3)).
The owner
or
2594
operator must follow
the procedures for loss of
certification
2595
set forth
in subsection (a)(3)(E) of this
Section for each
2596
monitoring system that
is disapproved for initial
2597
certification.
iv)
Audit
Decertification.
The Agency
may
issue a notice
of
disapproval of
the certification status of a monitor
in
accordance with Section 225 .260(b).
E)
Procedures for
Loss of Certification. If the
Agency issues a
notice
of disapproval
of
a certification
application
pursuant
to subsection
(a)(3)(D)(iii) of this Section
or a notice of disapproval
of
certification
status pursuant to subsection
(a)(3)(D)(iv) of this
Section, the
owner or operator
must fulfill
the following
requirements:
The owner or operator
must substitute the following
values
for
each disapproved monitoring
system and for each
hour
of EGU operation during
the period of invalid data
specified
pursuant to
40
CFR 75.20(a(4)(iii)
or 75.21(e),
continuing until the applicable
date and hour specified
pursuant
to
40
CFR 75.20(a(5)(i), each
incorporated
by
reference in Section 225.140.
For a disapproved
mercury
pollutant
concentration monitor
and disapproved flow
monitor, respectively,
the maximum potential
concentration
of mercury and the maximum
potential
flow rate,
as
defined in sections 2.1.7.1
and
2.1.4.1
of appendix A
to 40
CFR
75, incorporated by reference
in Section 225.140.
For
a disapproved
moisture monitoring system and
disapproved
diluent gas monitoring
system, respectively, the
minimum
potential moisture percentage
and either the maximum
2598
2599
2600
2601
2602
2603
2604
2605
2606
2607
2608
2609
2610
2611
2612
2613
2614
2615
2616
2617
2618
2619
2620
2621
2622
2623
2624
JCAR350225-08 1 8507r01
2625
potential
CO
concentration
or the minimum potential
O
2626
concentration
(as applicable), as defined in sections 2.1.5,
2627
2.1.3.1, and 2.1.3.2
of appendix Ato 40 CFR 75,
2628
incorporated by reference in Section 225.140.
For a
2629
disapproved
excepted monitoring system (sorbent trap
2630
monitoring
system) pursuant to 40 CFR 75.15 and
2631
disapproved flow monitor,
respectively, the maximum
2632
potential concentration of mercury
and
maximum
potential
2633
flow
rate, as defined in sections 2.1.7.1 and 2.1.4.1 of
2634
appendix A to 40 CFR 75,
incorporated by reference in
2635
Section 225.140.
2636
2637
ii4)
The
owner or operator must submit a notification of
2638
certification retest dates and a new certification
application
2639
in accordance with subsections
(a)(3)(A) and (B) of this
2640
Section.
2641
2642
iii4)
The owner or operator must repeat all certification
tests or
2643
other requirements
that were failed by the monitoring
2644
system, as indicated in the
Agency’s
notice of disapproval,
2645
no later than 30 unit operating
days after the date of
2646
issuance of the notice of disapproval.
2647
2648
b)
Exemption.
2649
2650
1)
If an
emissions
monitoring system has been previously certified
in
2651
accordance with Appendix B
to
this
Part
40
CFR 75 and the applicable
2652
quality assurance and quality control requirements
of Section 1.5 and
2653
Exhibit B to Appendix B to this
Part
40
CFR 75.21 and appendix B
to 40
2654
CFR 75
are
fully met, the monitoring system will
be
exempt
from the
2655
initial certification requirements of this
Section.
2656
2657
2)
The recertification provisions of this
Section apply to an emissions
2658
monitoring
system required by Section 225.240(a)(1) exempt
from initial
2659
certification requirements pursuant to
subsection (a)(1) of this Section.
2660
2661
c)
Initial
certification
and recertification
procedures for EGUs using the mercury
low
2662
mass emissions excepted
methodology pursuant
to Section
1.15(b)
of Appendix
B
2663
to this Part4O
CFR
75.8 1(b). The owner or operator that
has elected to use the
2664
mercury-low-mass-emissions-excepted
methodology
for a
qualified EGU
2665
pursuant to
Section 1.15(b)
to Appendix B to this Part 40 CFR 75.81(b)
must
2666
meet the applicable certification and
recertification requirements in Section
JCAR350225-081
8507r01
2667
1.15(c) through
(f)
to Appendix B to this Part4O
CFR
75.81(c)
through
(,
2668
incorporated by reference in Section 225.140.
2669
2670
d)
Certification Applications.
The owner or operator
of
an
EGU
must
submit an
2671
application to the Agency
within
45
days after completing all initial certification
2672
or recertification tests required pursuant
to this Section, including the information
2673
required pursuant to 40 CFR 75.63, incorporated
by
reference
in Section 225.140.
2674
2675
(Source: Amended at 33 Ill. Reg.
effective
2676
2677
Section
225.260 Out of Control Periods and
Data
Availability for Emission Monitors
2678
2679
Out of control periods must be determined
in accordance with Section 1.7 of
2680
Appendix
B.
2681
2682
ha)
Monitor data
availability
must
be determined on a calendar quarter basis in
2683
accordance with Section 1.8 of Appendix BWhenever
any emissions monitoring
2684
system fails to meet the quality assurance and quality control requirements
or
2685
data validation requirements
of
40
CFR 75, incorporated by reference in Section
2686
225.140, data must be substituted using the applicable
missing data procedures
in
2687
subparts D and I of 40 CFR 75, each incorporated
by
reference in
Section 225.140
2688
following initial certification of the required
2
CO
Q
2,
flow monitor, or mercury
2689
concentration or moisture
monitoring system(s) at a particular unit or stack
2690
location.
Compliance with the
percent reduction standard in Section
2691
225.230(a)(1)(B)
or
225.237(a)(1)(B)
or the emissions
concentration standard
in
2692
Section
225.23
0(a)(1)(A)
or 225
.237(a)(1)(A)
can only be demonstrated if
the
2693
monitor data availability
is equal to or greater than 75 percent; that is, quality
2694
assured
data must be recorded by a certified primary monitor, a certified
2695
redundant or non-redundant
backup monitor, or reference method for that unit
at
2696
least 75 percent of the time the unit is in operation.
2697
2698
cb)
Audit Decertification. Whenever both an audit of an emissions monitoring
2699
system and a review of the initial certification
or recertification application reveal
2700
that any
emissions
monitoring system should not have been certified or
recertified
2701
because it did not meet a particular performance
specification
or other
2702
requirement pursuant to Section 225.250 or the applicable provisions
of Appendix
2703
B to
this Part4O CFR
75, both at the time of the initial certification or
2704
recertification application submission and
at the time of the audit, the Agency
2705
must issue a notice of disapproval of the certification
status of such monitoring
2706
system. For the purposes of this subsection (cb), an audit must
be
either
a field
2707
audit
or an audit of
any information submitted to the Agency. By issuing the
2708
notice of disapproval, the Agency revokes
prospectively the certification status
of
2709
the emissions monitoring system. The data
measured and recorded by the
JCAR350225-081
8507r01
2710
monitoring system must not
be
considered
valid quality-assured data from the
2711
date of issuance
of the notification of the revoked certification
status until the date
2712
and time that the owner or
operator completes subsequently approved initial
2713
certification
or recertification tests for the
monitoring system. The owner or
2714
operator must follow
the applicable initial certification
or recertification
2715
procedures in Section
225
.250
for each disapproved
monitoring
system.
2716
2717
(Source:
Amended at 33 Ill. Reg.
effective
2718
2719
Section
225.261
Additional Requirements
to Provide Heat Input Data
2720
2721
The owner or operator of an EGU that monitors
and reports mercury mass emissions using
a
2722
mercury
concentration monitoring
system and a flow monitoring system must also
monitor and
2723
report the heat input rate at the EGU level using the procedures
set forth in Appendix B to this
2724
Part4O CFR 75, incorporated
by
reference
in
Section 225.140.
2725
2726
(Source: Amended at 33 Iii.
Reg.
effective
2727
2728
Section
225.265 Coal Analysis
for Input Mercury Levels
2729
2730
a)
The owner or operator of an EGU
complying with this Subpart B by means
of
2731
Section 225.230(a)(12),-ef using input
mercury
levels
(Ii)
and complying
by
2732
means of Section 225.230(b) or (d) or Section 225.232, electing
to comply with
2733
the
emissions testing,
monitoring, and recordkeeping requirements
under
Section
2734
225.239, or demonstrating compliance
under Section 225.233 or Sections
225.291
2735
through 225.299 must fulfill the following
requirements:
2736
2737
1)
Perforni daily sampling
of the coal combusted in the EGU for mercury
2738
content.
The owner or operator of such EGU must collect
a minimum
of
2739
one 2-lb grab sample per day
of operation from the belt feeders anywhere
2740
between the crusher
house or breaker building and the boiler.
The sample
2741
must be taken in a manner that provides
a representative mercury content
2742
for the coal burned
on that day. EGUs complying
by
means of
Section
2743
225.233 or Sections 225.291 through 225.299
of this Subpart must
2744
perform such coal
sampling at least once per month; EGUs complying
by
2745
means of the emissions testing,
monitoring,
and recordkeeping
2746
requirements under Section 225.239 must perform
such coal sampling
2747
according to the schedule
provided in Section 225.239(e)(3) of
this
2748
Subpart; all other EGUs subject
to this requirement must perform
such
2749
coal sampling on a
daily
basis.
2750
2751
2)
Analyze the
grab coal sample for the following:
2752
JCAR350225-08
1 8507r01
2753
A)
Determine
the heat content using ASTM D5865-04
or an
2754
equivalent method
approved in writing by the Agency.
2755
2756
B)
Determine
the moisture content using ASTM
D3173-03 or an
2757
equivalent
method approved in writing by the Agency.
2758
2759
C)
Measure the mercury content
using ASTM
D6414-01,
ASTM
2760
D3684-01,
or an equivalent method approved in writing
by the
2761
Agency.
2762
2763
3)
The owner
or
operator
of multiple EGUs at the same source using the
2764
same crusher house or breaker building may take
one
sample
per crusher
2765
house or breaker building,
rather than one per EGU.
2766
2767
4)
The owner or operator of an
EGU must use the data analyzed pursuant
to
2768
subsection
(b) of this Section to determine the mercury content in terms
of
2769
lbs/trillion Btu.
2770
2771
b)
The
owner or operator of
an EGU that must conduct sampling and analysis
of coal
2772
pursuant to subsection (a) of this Section
must
begin
such activity by the
2773
following date:
2774
2775
1)
If
the
EGU is in daily service, at least 30 days before the start of the
month
2776
for which such activity
will be required.
2777
2778
2)
If the EGU is not in daily service, on the day that the EGU resumes
2779
operation.
2780
2781
(Source:
Amended at
33
Ill.
Reg.
effective
2782
2783
Section 225.270
Notifications
2784
2785
The
owner or
operator of a source with one
or
more EGUs
must submit written notice to the
2786
Agency
according to the provisions in 40 CFR 75.61, incorporated
by
reference in Section
2787
225.140 (as a
segment of 40 CFR 75), for each
EGU or group of EGUs monitored at a common
2788
stack and each
non-EGU monitored pursuant to Section 1.16(b)(2)(B) of Appendix
B to this
2789
Part4O CFR
75.82b)(2)(ii), incorporated
by reference in Section 225.140.
2790
2791
(Source:
Amended at 33 Ill. Reg.
effective
2792
2793
Section
225.290
Recordkeeping and
Reporting
2794
2795
a)
General Provisions.
JCAR350225-08 1 8507r01
2796
2797
1)
The owner or
operator of an EGU and its designated representative
must
2798
comply with all applicable
recordkeeping and reporting requirements
in
2799
this Section and with all applicable
recordkeeping and reporting
2800
requirements
of Section 1.18 to Appendix
B
to this Part4O CFR
75.84,
2801
incorporated
by reference in Section 225.140.
2802
2803
2)
The owner or operator of an EGU must maintain
records for each month
2804
identifying
the
emission standard in Section 225 .230(a) or 225 .237(a)
of
2805
this Section with which
it is complying or that is applicable for the EGU
2806
and
the following
records related to the emissions of mercury
that
the
2807
EGU is allowed to emit:
2808
2809
A)
For an EGU for which the owner or operator
is complying with
2810
this Subpart
B by means of Section 225.230(a)(i2)ç or
2811
225
.237(a)(1)(B) or using input mercury levels to determine
the
2812
allowable emissions
of the EGU, records of the daily mercury
2813
content of coal used (lbs/trillion
Btu)
and the daily
and monthly
2814
input
mercury (ibs), which must be kept in the file pursuant
to
2815
Section 1.18(a) of
Appendix B to this
Part4O
CFR 75.84(a).
2816
2817
B)
For an EGU for which the owner or operator of an
EGU complying
2818
with this Subpart B by means of Section 225.23 0(a)(1)
or
2819
225 .237(a)(1)(A)
or using electrical output to determine the
2820
allowable emissions
of the EGU, records of the daily and monthly
2821
gross electrical output (GWh), which must
be kept in the file
2822
required pursuant
to Section 1.18(a) of Appendix B to this
Part4O
2823
CFR 75.84(a).
2824
2825
3)
The owner or operator of an EGU must maintain
records of the following
2826
data for each EGU:
2827
2828
A)
Monthly emissions
of mercury from the EGU.
2829
2830
B)
For an
EGU
for which
the owner or operator is complying
by
2831
means of Section 225.230(b) or
(d) of
this
Subpart B, records
of
2832
the
monthly
allowable emissions of mercury from the
EGU.
2833
2834
4)
The owner or operator of an EGU
that
is participating in an Averaging
2835
Demonstration pursuant to Section 225.232
of this Subpart B must
2836
maintain records identifying all sources and EGUs covered
by the
2837
Demonstration for each
month and, within 60 days after the end
of each
2838
calendar month, calculate and
record the actual and allowable mercury
JCAR350225-08 1 8507r01
2839
emissions of the EGU
for the month and the applicable 12-month rolling
2840
period.
2841
2842
5)
The owner or operator
of
an
EGU must maintain the following records
2843
related to quality assurance activities
conducted for emissions monitoring
2844
systems:
2845
2846
A)
The results
of
quarterly
assessments
conducted pursuant to
2847
Sectionsection 2.2 of Exhibit B
to
Appendix
B to this Partappendix
2848
B of 40
CFR 75, incorporated by reference in Section 225.140;
and
2849
2850
B)
Daily/weekly
system integrity checks pursuant to Sectionseet4en
2851
2.6
of Exhibit B to Appendix B to
this
Partappendix
B of
40
CFR
2852
75, incorporated
by
reference
in Section
225.140.
2853
2854
6)
The owner or operator of an
EGU must maintain an electronic copy
of all
2855
electronic
submittals
to the USEPA pursuant to Section 1.18(f)
to
2856
Appendix B to this Part4O
CFR 75.84(f), incorporated by reference in
2857
Section
225.140.
2858
2859
7)
The owner or operator
of an EGU must retain all records required
by this
2860
Section
at the source unless
otherwise provided in the CAAPP permit
2861
issued for the source and must make
a copy of any record available to
the
2862
Agency upon request.
2863
2864
b)
Quarterly Reports. The owner or
operator of a source with one or more EGUs
2865
must submit quarterly reports to the Agency as follows:
2866
2867
1)
These reports must include the following information
for operation of
the
2868
EGUs during the quarter:
2869
2870
A)
The total operating
hours
of each EGU and the mercury
CEMS, as
2871
also
reported in accordance with Appendix B to this Part4O
CFR
2872
75, incorporated
by
reference
in Section
225.140.
2873
2874
B)
A discussion
of any significant changes in the measures used
to
2875
control emissions of mercury from
the
EGUs or the coal supply
to
2876
the
EGUs, including changes in the source
of coal.
2877
2878
C)
Summary information
on the perfonnance of the mercury
CEMS.
2879
When the mercury CEMS
was not inoperative, repaired, or
2880
adjusted, except for routine zero and
span checks, this must be
2881
stated
in
the report.
JCAR350225-08 1 8507r01
2882
2883
D)
If the
CEMS downtime was more than
5.0
percent
of the total
2884
operating time
for the EGU: the date and time identifying each
2885
period
during which the
CEMS was inoperative, except for routine
2886
zero and
span checks; the nature
of CEMS repairs or adjustments
2887
and a summary
of quality assurance data consistent with Appendix
2888
B to this Part4O
CFR 75, i.e., the dates and results of the Linearity
2889
Tests
and any RATAs during the
quarter; a listing of any days
2890
when
a required
daily calibration
was not performed; and
the date
2891
and duration
of any periods when the CEMS was out-of-control
as
2892
addressed
by Section 225 .260.
2893
2894
Recertification
testing that has been performed for any
CEMS and
2895
the
status of the results.
2896
2897
2)
The
owner
or operator must submit each quarterly
report to the Agency
2898
within 45 days following
the end of the calendar quarter covered
by the
2899
report.
2900
2901
c)
Compliance Certification. The
owner or operator of a source with one or more
2902
EGUs must submit to the Agency a compliance
certification
in support of each
2903
quarterly report
based
on reasonable inquiry of those
persons with primary
2904
responsibility for ensuring
that all of the EGUs’ emissions are correctly
and fully
2905
monitored. The certification
must
state:
2906
2907
1)
That the monitoring data submitted were recorded
in accordance with
the
2908
applicable requirements
of this Section, Sections 225.240 through 225
.270
2909
and Section 225.290 of this Subpart B,
and Appendix B to this Part4O
2910
CFR 75, including
the quality assurance procedures and specifications;
2911
and
2912
2913
2)
For an EGU with add-on mercury emission
controls, a flue gas
2914
desulfurization system,
a selective catalytic reduction system, or
a
2915
compact
hybrid
particulate collector system and
for
all hours where
2916
mercury data is missing thatare
substituted
in accordance with 40
CFR
2917
75.34(a)(1):
2918
2919
A
That:
2920
2921
4)
The mercury add-on emission controls,
flue gas desulfurization
2922
system,
selective catalytic reduction
system, or compact hybrid
2923
particulate collector
system was operating
within the range of
2924
parameters listed
in the quality assurance/quality control
program
JCAR350225-081 8507r01
2925
pursuant to Exhibit B to
Appendix B to this Partappendix B to 40
2926
CFR75;or
2927
2928
i4)
With regard to a flue gas
desulfurization system or a selective
2929
catalytic
reduction system,
quality-assured SO
2 emission data
2930
recorded in accordance
with Appendix
B to
this Part 40
CFR 75
2931
document that the flue
gas desulfurization system was operating
2932
properly, or quality-assured
NO
emission data recorded in
2933
accordance with
Appendix B
to
this Part 40
CFR
75
document that
2934
the selective catalytic reduction
system was operating properly,
as
2935
applicable;
and
2936
2937
The substitute
data
values do not
vstematically
underestimate
2938
mercury emissions.
2939
2940
d)
Annual Certification of Compliance.
2941
2942
1)
The owner or operator of a
source with one or more EGUs subject to
this
2943
Subpart B must submit to the Agency an Annual Certification
of
2944
Compliance
with
this Subpart B no later than May 1 of each year
and must
2945
address compliance
for the previous calendar year. Such certification
2946
must be submitted to the Agency,
Air Compliance and Enforcement
2947
Section, and the Air Regional Field Office.
2948
2949
2)
Annual Certifications
of Compliance must indicate whether compliance
2950
existed for each EGU for each
month in the year covered by the
2951
Certification and it must certify to that effect. In addition,
for each
EGU,
2952
the
owner or operator
must provide the following appropriate data as
set
2953
forth in subsections (d)(2)(A) through (d)(2)(E)
of
this Section,
together
2954
with
the data set forth
in subsection (d)(2)(F) of this Section:
2955
2956
A)
If complying with this
Subpart
B by means of Section
2957
225 .230(a)(1
)(A) or 225.23 7(a)(1 )(A):
2958
2959
i)
Actual emissions rate, in lb/GWh, for each 12-month
2960
rolling
period
ending in the year covered by the
2961
Certification;
2962
2963
ii)
Actual emissions, in ibs, and gross electrical output,
in
2964
GWh, for each 12-month rolling period ending in the
year
2965
covered
by
the Certification;
and
2966
JCAR350225-081 8507r01
2967
iii)
Actual emissions,
in ibs, and gross electrical output, in
2968
GWh, for each month in the
year covered by
the
2969
Certification and
in the previous year.
2970
2971
B)
If complying
with
this Subpart
B by means of Section
2972
225
.230(a)(1
)(B)
or
225
.237(a)(1 )(B):
2973
2974
i)
Actual control efficiency
for emissions for each 12-month
2975
rolling
period ending in the year covered
by
the
2976
Certification, expressed
as a percent;
2977
2978
ii)
Actual emissions, in
lbs,
and mercury content in the fuel
2979
fired
in such EGU, in ibs, for each 12-month rolling
period
2980
ending in the year covered
by the Certification; and
2981
2982
iii)
Actual emissions, in ibs, and
mercury content in the fuel
2983
fired in
such EGU, in ibs, for each month in the year
2984
covered by the Certification
and in the previous year.
2985
2986
C)
If complying with this
Subpart
B by means of Section 225.23
0(b):
2987
2988
i)
Actual emissions and allowable
emissions
for each 12-
2989
month rolling period ending in the year covered
by the
2990
Certification;
and
2991
2992
ii)
Actual emissions and allowable
emissions, and which
2993
standard
of compliance the owner or operator was
utilizing
2994
for each month in the
year covered by the Certification
and
2995
in the
previous year.
2996
2997
D)
If complying with
this Subpart B by means of Section 225.230(d):
2998
2999
i)
Actual emissions
and allowable emissions for all
EGUs at
3000
the source for each 12-month rolling
period
ending in the
3001
year covered
by the Certification; and
3002
3003
ii)
Actual
emissions and allowable emissions,
and which
3004
standard
of
compliance
the
owner or operator was
utilizing
3005
for each month in the
year covered by the Certification
and
3006
in the previous year.
3007
3008
E)
If complying with
this Subpart B
by
means of Section 225
.232:
3009
JCAR350225-0818507r01
3010
i)
Actual emissions and allowable
emissions for
all
EGUs at
3011
the source
in an Averaging Demonstration for each 12-
3012
month rolling period
ending in
the
year covered by the
3013
Certification; and
3014
3015
ii)
Actual emissions
and allowable emissions, with the
3016
standard of compliance
the
owner
or operator was utilizing
3017
for each EGU at the source in an Averaging Demonstration
3018
for each
month for all EGUs at the source in an Averaging
3019
Demonstration in the year covered
by the
Certification
and
3020
in the
previous year.
3021
3022
F)
Any deviations, data
substitutions, or exceptions each month and
3023
discussion of the reasons for such deviations, data substitutions,
or
3024
exceptions.
3025
3026
3)
All Annual Certifications of
Compliance required to be submitted must
3027
include
the following certification by a responsible official:
3028
3029
I certify under penalty of law that
this
document and
all attachments were
3030
prepared under my direction or supervision in accordance with a
system
3031
designed
to assure that qualified personnel properly gather and evaluate
3032
the
information submitted.
Based on my inquiry of the person or persons
3033
directly responsible for gathering
the information, the information
3034
submitted is, to the best of my knowledge and belief, true,
accurate, and
3035
complete. I am aware that there are significant penalties for submitting
3036
false information, including
the possibility of fine and imprisonment
for
3037
knowing violations.
3038
3039
4)
The owner or operator of an EGU must submit its first Annual
3040
Certification of Compliance
to address calendar year 2009 or the calendar
3041
year in
which
the EGU commences commercial operation, whichever
is
3042
later. Notwithstanding subsection (d)(2)
of
this
Section, in the Annual
3043
Certifications
of Compliance that are required to be submitted
by May
1,
3044
2010, and
May 1, 2011,
to
address
calendar years
2009
and 2010,
3045
respectively, the owner or operator is not required to provide 12-month
3046
rolling data for
any period that ends before June 30, 2010.
3047
3048
e)
Deviation Reports. For each EGU, the owner or operator
must
promptly
notify
3049
the Agency of deviations from requirements of this Subpart B. At a minimum,
3050
these notifications must
include a description of such deviations within
30 days
3051
after discovery of the deviations,
and a
discussion
of the possible cause of such
3052
deviations, any corrective actions, and any preventative
measures taken.
JCAR350225-08
1 8507r01
3053
3054
f)
Quality
Assurance RATA
Reports.
The
owner or operator
of
an
EGU must
3055
submit
to the Agency,
Air Compliance
and Enforcement
Section, the quality
3056
assurance
RATA report
for each EGU
or group
of
EGUs monitored at a
common
3057
stack and each non-EGU
pursuant
to Section 1.16(b)(2)(B)
of Appendix
B to this
3058
Part4O
CFR
75.82(b)(2)(ii),
incorporated
by reference
in Section 225.140,
within
3059
45 days after
completing a quality
assurance
RATA.
3060
3061
(Source:
Amended
at 33 Ill. Reg.
effective
3062
3063
Section
225.291
Combined Pollutant
Standard:
Purpose
3064
3065
The
purpose of Sections
225.29
1 through 225.299
(hereinafter
referred
to as the Combined
3066
Pollutant
Standard
(CPS”))
is
to
allow
an
alternate means of compliance
with
the emissions
3067
standards
for mercury
in
Section
225.230(a)
for
specified EGUs
through
permanent
shut-down,
3068
installation
of ACT, and the application
of pollution
control technology
for
NON,
PM, and
SO
2
3069
emissions
that
also reduce
mercury
emissions as
a
co-benefit
and to establish permanent
3070
emissions
standards for those
specified
EGUs.
Unless otherwise
provided
for
in the CPS,
3071
owners
and operators of those
specified
EGUs
are not excused
from
compliance
with
other
3072
applicable
requirements
of Subparts B,
C,
D,
and E.
3073
3074
(Source: Added
at 33 Ill. Reg.
effective
3075
3076
Section
225.292
Applicability
of the Combined
Pollutant
Standard
3077
3078
As an alternative to
compliance
with
the emissions standards
of Section
3079
225.23
0(a),
the
owner or operator
of specified EGUs
in the CPS located
at Fisk,
3080
Crawford, Joliet, Powerton,
Waukegan,
and Will
County power plants
may
elect
3081
for all of those
EGUs as a group
to demonstrate compliance
pursuant
to
the
CPS,
3082
which establishes control
requirements
and emissions
standards
for
NO.fI,
3083
SQ2,
and mercury.
For this purpose,
ownership of
a specified EGU is
determined
3084
based on direct ownership,
by holding
a majority interest
in
a company
that
owns
3085
the EGU or EGUs,
or by the common
ownership
of
the company that owns
the
3086
EGU, whether through
a parent-subsidiary
relationship,
as a sister
corporation,
or
3087
as an affiliated
corporation with
the
same parent corporation,
provided that
the
3088
owner or operator has
the right or
authority to submit
a CAAPP application
on
3089
behalf of the EGU.
3090
3091
A
specified EGU
is
a
coal-fired
EGU listed in Appendix
A, irrespective
of
any
3092
subsequent
changes in
ownership
of the EGU
or power plant,
the operator, unit
3093
designation,
or name of unit.
3094
JCAR35O225O8l 8507r01
3095
ç
The owner or
operator
of each of the specified EGUs electing
to
demonstrate
3096
compliance with Section 225.230(a) pursuant
to the CPS must submit an
3097
application for
a CAAPP permit modification
to
the Agency,
as
provided
for in
3098
Section 225.220, that includes
the information specified in Section 225.293
that
3099
clearly states the owner’s or operator’s
election to demonstrate compliance with
3100
Section 225.230(a) pursuant to the CPS.
3101
3102
ci
If an owner or operator
of
one
or more specified EGUs elects to demonstrate
3103
compliance with Section 225.230(a)
pursuant to the CPS, then all specified EGUs
3104
owned or
operated
in Illinois by the owner or operator as of December
31,
2006,
3105
as defined in subsection (a) of this
Section,
are thereafter subject to the standards
3106
and control
requirements
of the CPS. Such EGUs are referred to as a Combined
3107
Pollutant Standard (CPS) group.
3108
3109
If an EGU is subject to the requirements
of
this
Section, then the requirements
3110
apply to all owners and operators
of the EGU, and to the CAIR designated
3111
representative for the EGU.
3112
3113
(Source: Added at 33 Ill. Reg.
effective
3114
3115
Section 225.293
Combined Pollutant
Standard: Notice of Intent
3116
3117
The
owner or
operator of one or more specified
EGUs that intends to comply with Section
3118
225.230(a) by
means of the CPS must notify the Agency
of its intention on or before December
3119
31, 2007.
The following information must accompany the notification:
3120
3121
The identification of each EGU that
will be complying with Section 225.23(
3122
pursuant to the CPS,
with evidence
that the owner or operator has identified
all
3123
specified EGUs that it owned or
operated in Illinois as of December 31, 2006,
and
3124
which commenced commercial operation on or before December 31, 2004;
3125
3126
If an EGU
identified
in
subsection
(a)
of this Section is also owned or operated
by
3127
a person different than the owner or operator submitting
the notice of intent, a
3128
demonstration that the submitter
has the right to commit the EGU or authorization
3129
from the responsible official for the EGU submitting
the
application;
and
3130
3131
A
summary of the current control
devices installed and operating on each EGU
3132
and
identification of the additional control devices
that
will
likely
be needed for
3133
each EGU to comply with emission control requirements of the
CPS.
3134
3135
(Source:
Added at
33
Ill. Reg.,_____
effective
3136
JCAR350225-08
1
8507r01
3137
Section 225.294 Combined Pollutant Standard:
Control Technology Requirements and
3138
Emissions
Standards
for Mercury
3139
3140
Control Technology Requirements
for Mercury.
3141
3142
II
For
each
EGU in a CPS group other than an EGU
that
is
addressed by
3143
subsection
(b)
of this Section, the owner or operator of the
EGU must
3144
install, if not already installed,
and properly operate and maintain, by the
3145
dates
set
forth in subsection (a)(2)
of
this Section,
ACT equipment
3146
complying with
subsections (g),
(h),
(i),
(I),
and
(k)
of this Section,
as
3147
applicable.
3148
3149
)
By
the
following dates, for the EGUs listed in subsections (a)(2)(A)
and
3150
(B), which include hot and
cold side ESPs, the owner or operator must
3151
install, if not
already
installed, and begin operating ACT equipment
or the
3152
Agency must be given written
notice that the EGU will be shut down on
or
3153
before the
following dates:
3154
3155
Fisk 19, Crawford 7, Crawford
8,
Waukegan
7, and Waukegan 8
3156
on or
before July 1,
2008:
and
3157
3158
Powerton 5, Powerton
6, Will County 3, Will County 4, Joliet
6,
3159
Joliet 7, and Joliet
8
on or before July 1,2009.
3160
3161
Notwithstanding subsection
(a) of this Section, the following EGUs are not
3162
required to install ACI equipment
because
they will be permanently shut down,
as
3163
addressed by Section 225.297, by the date specified:
3164
3165
D
EGUs that are required to permanently shut down:
3166
3167
On or before December 31, 2007, Waukegan
6;
and
3168
3169
)
On or
before December 31, 2010, Will County 1 and Will
County
3170
2.
3171
3172
Any other specified EGU
that is permanently shut down by December
31,
3173
2010.
3174
3175
Beginning on January
1,
2015,
and continuing thereafter, and measured on
a
3176
rolling 12-month basis
(the
initial
period is January 1, 2015, through December
3177
31, 2015, and, then, for every 12-month period thereafter),
each specified EGU,
3178
except
Will
County 3, shall achieve one of the following
emissions standards:
3179
JCAR350225-08 1 8507r01
3180
II
An
emissions
standard of
0.0080 lbs mercury/GWh gross electrical
output:
3181
3182
3183
)
A
minimum 90 percent reduction
of input mercury.
3184
3185
Beginning on January 1, 2016,
and continuing thereafter, Will
County 3 shall
3186
achieve
the
mercury emissions
standards
of subsection (c) of this Section
3187
measured
on a rolling 12-month basis (the initial
period is January 1, 2016,
3188
through December 31, 2016,
and, then, for every 12-month
period thereafter).
3189
3190
Compliance with
Emission Standards
3191
3192
II
At any time
prior to the dates required for
compliance in subsections (c)
3193
and
(d)
of this Section, the owner
or operator
of a specified EGU. upon
3194
notice to the Agency,
may elect to comply with the emissions
standards
of
3195
subsection
(c) of this Section measured
on either:
3196
3197
a rolling 12-month basis,
or:
3198
3199
semi-annual
calendar
basis pursuant to the emissions testing
3200
requirements in Section 225.239(c),
(d), (e), (f)(1)
and (2),
(h)(2),
3201
and
(i)(3)
and
(4)
of this
Subpart until June 30, 2012.
3202
3203
Once an EGU
is
subject
to the mercury emissions standards
of subsection
3204
(c)
of this Section, it
shall
not be subject to the requirements of
3205
subsections
(g),
(h), (i),
(i)
and (k)
of this Section.
3206
3207
Compliance with the mercury emissions
standards or reduction requirement
of
3208
this
Section must be calculated
in accordance with Section 225.230(a)
or
(b).
3209
3210
g
For
each EGU for which injection
of halogenated activated carbon is required
by
3211
subsection
(a)(1)
of this Section, the owner
or operator of the EGU must inject
3212
halogenated activated carbon
in an optimum manner, which, except
as provided in
3213
subsection (h) of this Section, is defined as all
of the following:
3214
3215
fl
The use of an injection
system for effective absorption of mercury,
3216
considering the configuration
of
the EGU
and its
ductwork:
3217
3218
The injection of halogenated
activated
carbon manufactured
by
Aistom,
3219
Norit, or Sorbent Technologies,
or Calgon Carbon’s FLUEPAC MC
Plus,
3220
or the
injection
of any other halogenated activated
carbon
or sorbent that
3221
the owner or
operator of the EGU has demonstrated
to have similar or
3222
better effectiveness for
control of mercury
emissions:
and
JCAR350225-08
1 8507r01
3223
3224
fl
The
injection
of
sorbent at the following minimum rates, as applicable:
3225
3226
For an
EGU firing subbituminous coal,
5.0 lbs per million actual
3227
cubic feet
or, for any cyclone-fired EGU that will install
a scrubber
3228
and baghouse
by December 31, 2012, and which already
meets an
3229
emission
rate
of 0.020
lb mercury/GWh gross electrical output
or
3230
at least
75 percent reduction of input mercury, 2.5
lbs per million
3231
actual cubic
feet;
3232
3233
For an
EGU firing bituminous coal, 10.0 lbs per million
actual
3234
cubic feet or, for any cyclone-fired
EGU
that will install a scrubber
3235
and baghouse
by December 31, 2012, and which already meets
an
3236
emission
rate of 0.020 lb mercury/GWh
gross electrical output or
3237
at least 75
percent reduction of input mercury, 5.0 lbs per million
3238
actual
cubic feet;
3239
3240
c)
For
an EGU firing a blend of subbituminous
and
bituminous
coal,
3241
a rate that
is the weighted average of the rates
specified
in
3242
subsections (g)(3)(A)
and
(B),
based on the blend of coal being
3243
fired;
or
3244
3245
A rate
or rates set lower by the Agency, in writing, than
the rate
3246
specified
in
any of subsection (g)(3)(A),
(B),
or
(C)
of this
Section
3247
on a unit-specific basis,
provided
that the owner or operator
of the
3248
EGU has demonstrated that such rate
or rates are needed so that
3249
carbon injection
will
not increase particulate matter emissions
or
3250
opacity so as to threaten noncompliance
with
applicable
3251
requirements for
particulate matter or opacity.
3252
3253
4
For purposes of subsection
(g)(3) of this Section, the flue gas flow rate
3254
must be determined
for the point sorbent injection;
provided that this flow
3255
rate maybe assumed
to be identical to the stack flow rate if the gas
3256
temperatures
at the point of
injection
and the stack
are normally within
3257
100°F, or the flue gas
flow rate may otherwise be calculated from the
stack
3258
flow
rate,
corrected for the difference in
gas temperatures.
3259
3260
The owner or operator of an
EGU that seeks to operate an EGU with an activated
3261
carbon injection rate or rates that are set on
a unit-specific basis pursuant to
3262
subsection (g)(3)(D) of this Section must submit
an application to the Agency
3263
proposing
such rate
or rates, and must meet the
requirements
of subsections (h)(1)
3264
and
(h)(2)
of this Section,
subject to the limitations of subsections (h)(3) and
3265
(4)
of this Section:
JCAR350225-08 1 8507r01
3266
3267
)
The application
must be submitted as an application for a new
or
revised
3268
federally enforceable operation
permit for the EGU, and it must include
a
3269
summary of relevant mercury emissions
data for the EGU, the unit-
3270
specific injection
rate or rates that are proposed,
and
detailed information
3271
to
support
the proposed
injection
rate or rates; and
3272
3273
This application must be submitted no later
than
the date
that activated
3274
carbon
must first be
injected.
For example, the owner or operator
of an
3275
EGU that must inject activated carbon
pursuant to subsection
(a)(1)
of this
3276
Section
must
apply for unit-specific injection rate or rates
by
July
1,
2008.
3277
Thereafier, the owner or
operator
may supplement
its
application; and
3278
3279
)
Any decision of the Agency denying
a permit or
granting
a permit with
3280
conditions that set
a
lower
injection
rate or rates may be appealed to
the
3281
Board pursuant to Section 39 of the Act; and
3282
3283
4
The owner or operator of an EGU may operate
at
the injection
rate or rates
3284
proposed in its application until a final decision is made on the application
3285
including a final decision on
any appeal to the Board.
3286
3287
During any evaluation of the effectiveness of a listed sorbent, alternative
sorbent,
3288
or other technique to control mercury emissions, the owner or operator of
an EGU
3289
need not comply with the requirements of subsection
(g)
of this Section for
any
3290
system needed to carry out the evaluation,
as further
provided
as follows:
3291
3292
j)
The
owner
or operator of the EGU must conduct the evaluation in
3293
accordance with a formal evaluation
program
submitted
to the Agency at
3294
least
30 days prior to commencement of the
evaluation;
3295
3296
The duration
and scope of the evaluation may not exceed the duration
and
3297
scope
reasonably needed to complete the desired evaluation
of the
3298
alternative control techniques,
as initially addressed by the owner or
3299
operator in a support document submitted with the evaluation
program;
3300
3301
3302
The owner or operator of the EGU must submit a report to the Agency
no
3303
later than
30 days after the conclusion of the evaluation that describes
the
3304
evaluation conducted and which
provides
the results of the
evaluation;
and
3305
3306
4
If the evaluation of alternative control techniques shows less effective
3307
control
of mercury
emissions from the EGU than was achieved with
the
3308
principal control techniques,
the
owner
or operator of the EGU must
JCAR350225-081
8507r01
3309
resume use
of the principal control
techniques.
If
the evaluation
of the
3310
alternative
control
technique shows
comparable effectiveness to the
3311
principal
control technique, the owner or operator
of the EGU may either
3312
continue to use
the alternative control technique in a manner that
is at least
3313
as
effective
as the principal
control technique or it may resume use
of the
3314
principal
control
technique. If the evaluation
of the alternative control
3315
technique
shows more effective control of mercury emissions
than the
3316
control technique,
the owner or operator of the EGU must continue
to use
3317
the alternative control technique in
a
manner
that is more effective than
3318
the principal
control technique, so long as it continues to
be subject to this
3319
Section.
3320
3321
j)
In addition to complying with the applicable
recordkeeping and monitoring
3322
requirements in Sections 225.240
through
225.290,
the owner or operator
of an
3323
EGU that elects
to comply with Section 225.230(a)
by means of the CPS must
3324
also comply with the following
additional
requirements:
3325
3326
jj
For the first
36 months that
injection
of sorbent is required, it must
3327
maintain records of the usage
of
sorbent,
the exhaust gas flow rate from
3328
the EGU,
and the
sorbent feed rate, in pounds per million
actual cubic feet
3329
of exhaust
gas at the
injection
point, on a weekly average;
3330
3331
)
After the first 36 months that
injection
of sorbent is required, it must
3332
monitor activated sorbent feed rate
to
the
EGU, flue gas temperature
at the
3333
point of sorbent injection, and exhaust gas flow rate
from the EGU,
3334
automatically recording
this data and the sorbent carbon feed rate, in
3335
pounds per million actual cubic
feet of
exhaust
gas at the
injection
point,
3336
on
an hourly average;
and
3337
3338
)
If a blend of
bituminous and subbituminous coal is fired in the EGU,
it
3339
must keep records of the amount
of
each
type of coal burned and the
3340
required injection rate
for
injection
of activated carbon on a weekly
basis.
3341
3342
In addition to complying with
the applicable reporting requirements in Sections
3343
225.240 through
225.290,
the owner or operator of an EGU
that elects to comply
3344
with Section 225.23
0(a)
by means of the CPS must also submit quarterly
reports
3345
for the recordkeeping and monitoring
conducted pursuant to subsection
ii)
of
this
3346
Section.
3347
3348
As an alternative to the
CEMS monitoring, recordkeeping, and reporting
3349
requirements in Sections 225.240
through
225.290,
the owner or operator
of an
3350
EGU may elect to comply with the emissions testing,
monitoring, recordkeeping,
JCAR350225-08
1 8507r01
3351
and reporting requirements in Section 225.239(c), (d), (e), (f)(1) and (2), (h)(2),
3352
(i)(3) and (4),
and
(fl(1).
3353
3354
(Source:
Added at 33 Iii. Reg.
effective
3355
3356
Section
225.295 Combined-Pollutant Standard: Emissions
Standards for
NOX
and
3357
SO
2
Trcatment of Mcrcury Allowances
3358
3359
Any
mercury allowances allocated
to
the Agency
by the USEPA must be treated as follows:
3360
3361
a
No
such allowances
may be
allocated
to any owner or operator of an EGU or
3362
other sources of mercury emissions into the atmosphere or discharges
into the
3363
waters of the State.
3364
3365
b
The Agency must hold all allowances allocated
by the USEPA to the State. At
3366
the
end of each calendar year, the Agency must instruct the USEPA to retire
3367
permanently all such allowances.
3368
3369
Emissions Standards for
NO
and
Reporting Requirements.
3370
3371
jj
Beginning with calendar year 2012 and continuing in each calendar
year
3372
thereafter, the CPS group, which includes all specified EGUs that have
not
3373
been permanently shut down by December 31 before the applicable
3374
calendar year, must
comply with
a CPS group average annual
NO
3375
emissions rate of no more than
0.11
lbs/mmBtu.
3376
3377
Beginning with ozone season
control period
2012
and continuing in each
3378
ozone season control period
(May
1 through September
30)
thereafter,
the
3379
CPS
group, which includes
all specified EGUs that have not been
3380
permanently shut down by December 31 before the applicable ozone
3381
season, must comply with a
CPS group
average
ozone season
NO
3382
emissions rate of no more than 0.11 lbs/mmBtu.
3383
3384
The
owner or operator of the specified EGUs in the CPS group must
file,
3385
not later than one year after
startup of any selective SNCR on such EGU,
a
3386
report with the Agency describing the
NO
emissions reductions that
the
3387
SNCR has
been
able to
achieve.
3388
3389
!
Emissions Standards for
SO
2.
Beginning
in
calendar year 2013
and continuing in
3390
each calendar year thereafter, the CPS group must comply with the applicable
3391
CPS group average
annual
2
SO emissions rate listed as follows:
3392
3393
lbs/nimBtu
JCAR350225-08 1 8507r01
3394
3395
2013
0.44
3396
2014
0.41
3397
2015
028
3398
2016
0.195
3399
2017
0.15
3400
2018
0.13
3401
2019
0.11
3402
3403
c)
Compliance with the
NO
and
SO
2 emissions standards must be demonstrated
in
3404
accordance
with
Sections 225.310, 225.410, and 225.5 10. The owner
or operator
3405
of the specified EGUs must complete
the demonstration of compliance
pursuant
3406
to Section
225 .298(c)
before March 1 of the following year for annual
standards
3407
and
before November 30 of the particular
year
for ozone
season
control periods
3408
(May
1 through September
30)
standards, by which date a compliance report
must
3409
be
submitted to the Agency.
3410
3411
The CPS group average annual
2
SO
emission rate,
annual
NO
emission rate
and
3412
ozone season
NO
emission rates shall be determined as follows:
3413
3414
n
n
3415
ERavb = 2
(SO
orNOtons)/
(HI
1)
3416
i=1
i=l
3417
3418
Where:
3419
ER = average
annual or ozone season emission rate in
lbs/mmBbtu of all EGUs in the CPS group.
HI,
= heat input
for the
annual
or ozone control period of each
EGU, in mmBtu.
= actual annual
SO
2
tons of each
EGU in the CPS group.
NQi
= actual annual or ozone season
NO
tons of each EGU
in
the CPS group.
n
= number
of EGUs that are in the CPS group
i
each EGU
in the CPS group.
3420
3421
(Source:
Amended at
33
Ill. Reg.
effective
3422
3423
Section
225.296 Combined Pollutant Standard: Control Technology
Reiuirements
for
3424
QQ2,
and PM
Emissions
3425
3426
Control Technology Requirements
for
NO
and SO
2.
3427
JCAR350225-081 8507r01
3428
j)
On
or before December 31, 2013, the owner
or
operator must either
3429
permanently
shut
down
or install and have operational FGD equipment
on
3430
Waukegan
7;
3431
3432
)
On or before
December 31, 2014, the owner or operator must either
3433
permanently
shut
down or
install and
have
operational FGD equipment
on
3434
Waukegan
8;
3435
3436
)
On or before
December 31,
2015,
the
owner or operator must either
3437
permanently
shut down or install and have operational
FGD
equipment
on
3438
Fisk 19;
3439
3440
4)
If Crawford
7
will
be operated after December 31, 2018, and not
3441
permanently
shut down by this date, the owner or operator must:
3442
3443
)
On or before December 31, 2015, install and have operational
3444
SNCR or equipment capable
of
delivering essentially
equivalent
3445
Q<
reductions on Crawford
7;
and
3446
3447
j)
On or before December 31, 2018, install
and
have operational
FGD
3448
equipment on Crawford
7;
3449
3450
)
If Crawford
8
will
be operated afier December 31, 2017 and not
3451
permanently shut down
by this date, the owner or operator must:
3452
3453
)
On or before December 31, 2015, install and have operational
3454
SNCR or
equipment capable of delivering essentially equivalent
3455
emissions reductions on Crawford
8;
and
3456
3457
j)
On or before December 31, 2017, install and have operational
FGD
3458
equipment on Crawford
8.
3459
3460
k)
Other Control Technology Requirements for
SO
2.Owners or operators of
3461
specified EGUs must either permanently shut down or install FGD equipment
on
3462
each
specified EGU
(except
Joliet
5),
on
or before December 31, 2018, unless
an
3463
earlier date is specified in subsection
(a)
of this Section.
3464
3465
Control Technology Requirements for
PM. The owner or operator of the two
3466
specified EGUs listed in this subsection that
are equipped with a hot-side ESP
3467
must replace the hot-side ESP with a cold-side ESP, install an appropriately
3468
designed fabric
filter,
or
permanently shut down the EGU
by
the dates specified.
3469
Hot-side ESP means an ESP
on a coal-fired boiler that is installed before the
3470
boiler?s
air-preheater where the operating
temperature is typically at least 5 50°F,
JCAR350225-08
1 8507r01
3471
as distinguished from a cold-side
ESP
that is installed
after
the
air
pre-heater
3472
where
the
operating
temperature is typically no more than 350°F.
3473
3474
Waukegan 7 on or before December 31, 2013; and
3475
3476
)
Will
County
3 on or before December 31,
2015.
3477
3478
Beginning on December 31, 2008, and annually thereafter up to and including
3479
December 31,
2015,
the owner or operator of the Fisk power plant must submit in
3480
writing to the Agency a report
on any
technology
or
equipment
designed
to affect
3481
air quality that has been considered or explored for the Fisk power plant in the
3482
preceding 12 months. This report will not obligate the owner or
operator to install
3483
any equipment
described
in the report.
3484
3485
Notwithstanding
35 Ill. Adm. Code
20l.146(hhh),
until an EGU has complied
3486
with the applicable requirements of subsections
225.296(a),
(b),
and
(c),
the
3487
owner or
operator
of the EGU must
obtain
a construction permit for any new or
3488
modified air pollution control equipment that it proposes to construct for
control
3489
of emissions of mercury,
NOR,
PM, or
SO
2.
3490
3491
(Source:
Added at 33 Ill. Reg.
effective
3492
3493
Section
225.297 Combined Pollutant Standard: Permanent Shut-Downs
3494
3495
The
owner or operator
of the following EGUs must permanently shut down the
3496
EGU by
the dates specified:
3497
3498
Waukegan
6
on
or
before December 31, 2007; and
3499
3500
)
Will County 1
and
Will County 2 on or before December 31, 2010.
3501
3502
j
No
later thasi 8 months before the date that a specified EGU will be permanently
3503
shut down, the
owner
or operator must submit a report to the Agency that includes
3504
a
description of the actions that have already been taken to allow the shutdown
of
3505
the EGU
and
a description of the future actions that must be accomplished to
3506
complete
the shutdown
of
the EGU, with the anticipated schedule
for those
3507
actions and the anticipated date of permanent shutdown of the unit.
3508
3509
ç).
No later
than six months before
a specified
EGU
will be permanently shut down,
3510
the
owner or operator shall apply
for
revisions to the operating permits for
the
3511
EGU to include provisions that terminate the authorization to operate the
unit
on
3512
that date.
3513
JCAR350225-08
1 8507r01
3514
If after applying
for
or
obtaining
a construction
permit
to install
required control
3515
equipment,
the
owner or
operator
decides to permanently
shut-down
a
Specified
3516
EGU
rather
than install
the
required
control
technology, the owner
or operator
3517
must
immediately
notify
the Agency in writing
and thereafter
submit the
3518
information
required
by subsections
(b)
and
(c) of this Section.
3519
3520
ç
Failure to permanently
shut
down
a
specified
EGU
by
the required date shall
be
3521
considered
separate
violations of the
applicable emissions
standards
and
control
3522
technology requirements
of the CPS
for
NON,
PM,
SO,,
and mercury.
3523
3524
(Source:
Added at
33 Ill. Reg.
effective
3525
3526
Section
225.298 Combined
Pollutant
Standard: Requirements
for
NO
and SO
2
3527
Allowances
3528
3529
The
following
requirements
apply to
the owner, the operator,
and the
designated
3530
representative with
respect
to SO
2
and
NO
allowances:
3531
3532
j
The owner,
operator, and
designated representative
of specified EGUs
in a
3533
CPS group
is permitted
to
sell,
trade,
or
transfer
SO,
and
NO
emissions
3534
allowances
of any vintage
owned, allocated
to, or earned by
the specified
3535
EGUs
(the
“CPS
allowances”)
to its affiliated
Homer City,
Pennsylvania,
3536
generating
station
for as long as the Homer
City Station needs
the
CPS
3537
allowances
for
compliance.
3538
3539
)
When and if
the Homer City Station
no longer requires
all
of the CPS
3540
allowances,
the owner, operator,
or designated representative
of
specified
3541
EGUs in a CPS
group may sell
any and all remaining
CPS allowances,
3542
without restriction,
to any person
or entity located
anywhere,
except
that
3543
the owner or
operator may not directly
sell, trade,
or
transfer CPS
3544
allowances to
a unit
located
in
Ohio,
Indiana, Illinois,
Wisconsin,
3545
Michigan, Kentucky,
Missouri, Iowa,
Minnesota, or
Texas.
3546
3547
In no event shall
this subsection
(a)
require or be interpreted
to require
any
3548
restriction whatsoever
on
the
sale, trade, or exchange
of the CPS
3549
allowances by
persons or entities who
have acquired
the CPS allowances
3550
from the
owner, operator, or designated
representative
of specified
EGUs
3551
maCPS
group.
3552
3553
j
The owner,
operator,
and designated
representative
of EGUs in a specified
CPS
3554
group
is
prohibited from purchasing
or using
SO
2
and
NO
allowances for
the
3555
purposes
of
meeting the
SO, and
NO
emissions
standards set forth
in Section
3556
225.295.
JCAR350225-08
1 8507r01
ç).
Before March 1, 2010, and
continuing each year thereafler, the designated
representative
of the EGUs in a
CPS group must
submit
a report to the Agency
that demonstrates
compliance with
the requirements of this Section
for the
previous calendar year and
ozone season control period (May 1 through
September 30), and includes identification
of any
NO
or
SO
2
allowances that
have been
used for compliance with
any
NO
or
SO
2
trading
programs, and any
or
SQ
allowances
that
were sold, gifted, used, exchanged,
or traded. A final
report must be submitted to
the Agency by August 31 of each year, providing
either verification
that the actions described in the initial report have
taken place,
or, if such actions have not
taken place, an explanation of the changes that
have
occurred and
the reasons for such changes.
(Source:
Added at
33
Iii.
Reg.
effective•
Section
225.299 Combined Pollutant
Standard: Clean Air Act Requirements
The
SO
2
emissions
rates
set forth in
the CPS shall be deemed to be best available retrofit
technology (
11
BART”) under the Visibility
Protection
provisions of the CAA (42
USC 7491),
reasonably available control technology (BRACT”) and reasonably available
control measures
(
11
RACM”) for
achieving
fine
particulate
matter
(“PM”)
requirements under NAAOS
in effect
on August 31,
2007, as required
by the CAA (42
USC
7502).
The Agency may use the
SO, and
NO
emissions
reductions required under
the CPS in
developing
attainment demonstrations
and
demonstrating
reasonable further progress
for PM and 8 hour ozone standards, as required
under
the CAA. Furthermore, in developing rules, regulations,
or State Implementation Plans
designed to comply
with PM and
8 hour ozone
NAAOS,
the Agency, taking into
account all
emission
reduction efforts and other appropriate
factors, will use best efforts to seek
SO
2
and
NQ
emissions rates
from
other EGUs that are equal to or less than the rates
applicable to the
CPS
group and
will seek
SO
2
and NO reductions
from other sources before seeking additional
emissions reductions
from any
EGU in the CPS group.
(Source:
Added at
33
Iii.
Reg.
effective
SUBPART F:
COMBiNED POLLUTANT STANDARDS
Section 225.600
Purpose (Repealed)
The puose of
this Subpart F is to allow an alternate means
of compliance with the emissions
standards
for mercury
in
Section 225.23
0(a)
for specified EGUs
through permanent shut down,
installation of ACT,
and the application
of pollution control technology for
NON,
PM, and
SO
emissions that also
reduce mercury
emissions as a co benefit and to establish permanent
emissions
standards for those specified
EGUs. Unless
othevise
provided for in this Subpart
F,
3557
3558
3559
3560
3561
3562
3563
3564
3565
3566
3567
3568
3569
3570
3571
3572
3573
3574
3575
3576
3577
3578
3579
3580
3581
3582
3583
3584
3585
3586
3587
3588
3589
3590
3591
3592
3593
3594
3595
3596
3597
3598
t.
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JCAR350225-08 1 8507r01
4082
Section 225.APPENDIX A Specified
EGUs
for Purposes
of the CPSSubpart F (Midwest
4083
Generation’s
Coal-Fired Boilers as of July 1, 2006)
4084
Plant
Permit
Number
Crawford
031 600AIN
Boiler
Permit designation
7
Unit
7 Boiler BLR1
8
Unit 8 Boiler BLR2
çSubpar-tF
Designation
Crawford
7
Crawford 8
19
Unit 19 Boiler BLR19
71
Unit 7 Boiler BLR71
72
Unit 7 Boiler BLR72
81
Unit 8 Boiler BLR81
82
Unit 8 Boiler BLR82
5
Unit 6 Boiler BLR5
Powerton
179801AAA
51
Unit 5 Boiler BLR5 1
52
Unit
5
Boiler BLR52
61
Unit 6 Boiler BLR61
62
Unit 6 Boiler BLR62
Powerton
5
Powerton
5
Powerton
6
Powerton
6
Waukegan
097190AAC
17
Unit 6 Boiler BLR17
7
Unit
7
Boiler BLR7
8
Unit 8 Boiler BLR8
Waukegan
6
Waukegan
7
Waukegan
8
4085
Will
County
19781 OAAK
1
2
3
4
Unit 1 Boiler BLR1
Unit 2 Boiler BLR2
Unit
3
Boiler BLR3
Unit 4 Boiler BLR4
Will County
1
Will
County 2
Will County
3
Will
County 4
Fisk
031600AM1
Joliet
197809AA0
Fisk
19
Joliet
7
Joliet 7
Joliet
8
Joliet 8
Joliet
6
4086
(Source:
Amended at 33 Ill. Reg.
effective
JCAR350225-081
8507r01
4087
Section 225.APPENDIX B Continuous Emission
Monitoring Systems for Mercury
4088
4089
Section 1.1 Applicability
4090
4091
The provisions of this Appendix apply to sources subject to
35 Iii. Adm. Code
225
mercury
(Hg)
4092
mass emission reduction program.
4093
4094
Section 1.2 General Operating Requirements
4095
4096
Primary
Equipment Performance
Requirements. The owner or
operator
must
4097
ensure that each continuous mercury emission
monitoring system required by this
4098
Appendix meets the equipment,
installation and performance specifications
in
4099
Exhibit
A
to
this Appendix and is maintained according
to the quality assurance
4100
and quality control procedures in Exhibit B
to this Appendix.
4101
4102
Heat Input Rate Measurement Requirement.
The owner or operator must
4103
determine and record
the heat input rate, in units of mmBtu/hr,
to
each
affected
4104
unit for every hour or
part
of an hour
any fuel is combusted following the
4105
procedures in Exhibit
C
to this Appendix.
4106
4107
Primary Equipment Hourly
Operating Requirements. The owner or operator
must
4108
ensure that all continuous mercury emission
monitoring
systems required by
this
4109
Appendix are in operation and monitoring unit emissions
at all times that the
4110
affected unit combusts any fuel except during periods
of
calibration,
quality
4111
assurance, or preventive
maintenance, performed pursuant to Section 1.5
of this
4112
Appendix and Exhibit B to this Appendix,
periods
of repair, periods of backups
of
4113
data from the data acquisition and handling system,
or
recertification
performed
4114
pursuant to Section 1.4 of this
Appendix.
4115
4116
fl
The owner or operator
must ensure that each continuous emission
4117
monitoring
system is capable of completing
a
minimum
of one cycle of
4118
operation (sampling, analyzing
and data recording) for each successive
15-
4119
minute interval.
The owner or operator must reduce all volumetric
flow,
4120
çQ2concentration,
02
concentration
and mercury concentration data
4121
collected
by
the
monitors to hourly averages. Hourly averages
must be
4122
computed using at least
one data point in each 15 minute quadrant
of an
4123
hour,
where
the unit combusted fuel
during that quadrant of an hour.
4124
Notwithstanding
this requirement, an hourly average may be
computed
4125
from at least two
data points separated
by
a minimum of 15 minutes
4126
(where the unit operates
for more
than one quadrant of an
hour)
if data
are
4127
unavailable as a result of the performance
of calibration, quality assurance,
4128
or
preventive
maintenance activities pursuant
to Section 1.5 of this
4129
Appendix and Exhibit
B to this Appendix, or backups of data
from the
JCAR350225-08 1 8507r01
4130
data acquisition
and handling
system,
or
recertification,
pursuant
to
4131
Section 1.4 of this
Appendix. The owner or operator
must use all
valid
4132
measurements or data
points collected during an hour to calculate
the
4133
hourly averages. All data
points collected during an hour must be, to
the
4134
extent
practicable, evenly
spaced over the hour.
4135
4136
)
Failure
of
a
2
CO
or
02
emissions
concentration
monitor, mercury
4137
concentration monitor, flow monitor
or a
moisture
monitor to acquire
the
4138
minimum
number of data points for calculation of an hourly
average in
4139
subsection
(c)(1)
of
this
Section must
result in the failure to obtain
a valid
4140
hour of data and the loss of such component data for
the
entire
hour. For
a
4141
moisture monitoring
system consisting of one or more oxygen analyzers
4142
capable of measuring
02
on a wet-basis and a dry-basis,
an hourly average
4143
percent moisture value is
valid only if the
minimum
number of data
points
4144
is acquired for both the wet-and dry-basis measurements.
4145
4146
Optional Backup Monitor Requirements. If the owner or operator chooses
to use
4147
two or more continuous mercury emission
monitoring
systems, each of which
is
4148
capable of monitoring the same stack or duct at a specific affected
unit, or group
4149
of units using a
common
stack, then the owner or operator must designate
one
4150
monitoring system
as
the
primary monitoring system, and must record this
4151
information in the monitoring
plan,
as
provided
for in
Section
1.10 of this
4152
Appendix. The owner or operator must designate the other monitoring
systems
as
4153
backup
monitoring systems in the monitoring plan. The backup monitoring
4154
systems
must be designated as redundant backup monitoring
systems,
non-
4155
redundant backup monitoring
systems, or
reference
method
backup systems,
as
4156
described in Section
1.4(d)
of this Appendix. When the certified primary
4157
monitoring
system is
operating and not out-of-control as defined in Section
1.7 of
4158
this Appendix, only data from the certified primary monitoring
system must be
4159
reported
as
valid, quality-assured
data. Thus, data from the backup monitoring
4160
system may be reported as valid, quality-assured data only when the
backup is
4161
operating and not out-of-control
as defined in
Section
1.7 of this Appendix
(or
in
4162
the applicable reference method in appendix A of 40 CFR
60,
incorporated
by
4163
reference in Section 225.140)
and when the certified primary monitoring system
4164
is not operating (or is operating but
out-of-control).
A particular monitor
may
be
4165
designated
both as a certified
primary monitor for one unit and as a certified
4166
redundant backup monitor for another unit.
4167
4168
Minimum
Measurement
Capability Requirement. The owner or operator must
4169
ensure
that
each continuous
emission monitoring system is capable of accurately
4170
measuring,
recording and reporting
data, and must
not incur
an exceedance of
the
4171
full scale range, except as provided in Section 2.1.2.3 of Exhibit
A to this
4172
Appendix.
JCAR350225-081
8507r01
4173
4174
fi
Minimum
Recording
and Recordkeeping
Requirements.
The
owner or
operator
4175
must record and the
designated representative
must report
the hourly, daily,
4176
quarterly
and
annual
information collected
under the requirements
as specified
in
4177
subpart
G
of 40
CFR 75, incorporated
by
reference in
Section 225.140,
and
4178
Section
1.11 through
1.13 of
this
Appendix.
4179
4180
Section 1.3 Special Provisions
for
Measuring
Mercury
Mass Emissions Using
the
Excepted
4181
Sorbent Trap Monitoring
Methodology
4182
4183
For
an affected coal-fired
unit under
35
Iii. Adm. Code
225,
if the owner or
operator
elects
to use
4184
sorbent trap monitoring
systems
(as
defined
in Section 225.130)
to quantify mass
emissions,
the
4185
guidelines
in subsections (a)
through
(1)
of this Section must
be followed for this excepted
4186
monitoring
methodology:
4187
4188
For
each sorbent
trap monitoring
system
(whether
primary or redundant
backup),
4189
the
use of paired
sorbent traps, as
described in Exhibit
D to this Appendix,
is
4190
required;
4191
4192
Each sorbent
trap must have
a main section, a
backup section and
a third section
4193
to
allow spiking with a calibration
gas of known
mercury concentration,
as
4194
described
in
Exhibit
D to this Appendix;
4195
4196
A certified flow monitoring
system
is required;
4197
4198
Correction
for stack gas moisture
content is required, and
in some cases,
a
4199
certified
07
or
CO
2
monitoring
system is required
(see
Section 1.15(a)(4));
4200
4201
Each sorbent trap
monitoring
system must be installed
and operated in
accordance
4202
with Exhibit
D to this Appendix.
The automated
data
acquisition and
handling
4203
system must ensure
that the sampling
rate
is proportional
to the stack gas
4204
volumetric
flow rate.
4205
4206
At
the beginning and
end of each
sample collection period,
and at least
once
in
4207
each unit operating
hour during the collection
period,
the gas flow meter
reading
4208
must be recorded.
4209
4210
g
After each
sample collection
period,
the
mass
of mercury adsorbed in
each
4211
sorbent
trap (in all three
sections)
must be determined
according
to the applicable
4212
procedures
in Exhibit D
to this Appendix.
4213
4214
The
hourly mercury mass
emissions for
each collection period
are determined
4215
using the results of the
analyses
in conjunction
with contemporaneous
hourly
data
JCAR350225-081
8507r01
4216
recorded by a certified stack
flow monitor, corrected for the stack
gas moisture
4217
content.
For
each
pair of sorbent traps analyzed,
the
average
of the 2 mercury
4218
concentrations must
be used for reporting purposes under Section
1.18(f)
of this
4219
Appendix. Notwithstanding this
requirement, if, due to circumstances
beyond the
4220
control
of the owner or operator,
one of the paired traps is accidentally lost,
4221
damaged
or
broken
and cannot be analyzed,
the
results
of the analysis of the
other
4222
trap may be used for
reporting purposes, provided that the other
trap has met all
of
4223
the applicable quality-assurance
requirements
of this Part.
4224
4225
All unit operating
hours for which valid mercury concentration
data are obtained
4226
with the primary sorbent trap monitoring
system
(as
verified using the quality
4227
assurance procedures
in Exhibit D to this Appendix) must be reported in
the
4228
electronic quarterly report under Section 1.18(f)
of this Appendix. For hours
in
4229
which data from the primary
monitoring system are
invalid,
the owner or
operator
4230
may, in accordance with Section 1.4(d) of this Appendix,
report valid mercury
4231
concentration data from:
a certified redundant backup CEMS or sorbent trap
4232
monitoring
system a certified non-redundant backup
CEMS or sorbent trap
4233
monitoring
system:
or
an applicable reference method under Section 1.6
of this
4234
Appendix.
4235
4236
Initial certification requirements
and additional quality-assurance requirements
4237
for the sorbent trap monitoring
systems are found in Section 1
.4(c)(7),
in
Section
4238
6.5.6 of Exhibit A to this Appendix,
in Sections 1.3 and 2.3 of Exhibit B to this
4239
Appendix, and in Exhibit D to this Appendix.
4240
4241
ç)
During each RATA
of a sorbent trap monitoring system, the type of sorbent
4242
material used by the traps must
be the
same
as
for
daily operation of the
4243
monitoring
system.
A new pair of traps must be used for each RATA run.
4244
However, the size of the traps used
for the
RATA
may be smaller than the traps
4245
used for
daily operation
of the system.
4246
4247
Whenever the type of
sorbent material used by the traps is changed, the owner
or
4248
operator must conduct a diagnostic RATA of the modified
sorbent trap
4249
monitoring system within
720 unit or stack operating hours after the date and
hour
4250
when the new sorbent material is first used. If the
diagnostic RATA is passed,
4251
data from
the modified
system may be reported as quality-assured, back
to the
4252
date and hour when the new
sorbent material was first used. If the RATA is
4253
failed, all data from the modified system must be invalidated,
back
to the date
and
4254
hour when the new sorbent material was first used, and data
from the system
must
4255
remain
invalid
until
a subsequent RATA is passed. If the required RATA
is not
4256
completed within 720 unit or
stack operating hours, but is passed on the first
4257
attempt,
data from the modified system
must
be invalidated beginning with the
4258
first
operating hour after the 720 unit or stack operating
hour
window
expires,
and
JCAR350225-0818507r01
4259
data
from the
system
must
remain invalid
until the date
aid
hour of completion
of
4260
the
successful
RATA.
4261
4262
Section
1.4 Initial
Certification
and
Recertification
Procedures
4263
4264
Initial Certification
Approval
Process.
The
owner or
operator
must
ensure
that
4265
each
continuous
mercury
emission
monitoring
system
required by
this Appendix
4266
meets
the
initial
certification
requirements
of this Section.
fri addition,
whenever
4267
the
owner
or operator
installs
a
continuous
mercury
emission
monitoring
system
4268
in order
to meet
the
requirements
of Section
1.3
of this
Appendix
and 40
CFR
4269
sections
75.11 through
75.14
and 75.16
through
75.18,
incorporated
by
reference
4270
in Section
225.140,
where
no
continuous
emission
monitoring
system was
4271
previously
installed,
initial
certification
is required.
4272
4273
]j
Notification
of initial
certification
test dates.
The
owner
or operator
or
4274
designated
representative
must submit
a written
notice
of the dates
of
4275
initial certification
testing
at the
unit as specified
in
40 CFR
75.6 1(a)(1),
4276
incorporated
by
reference
in Section
225.140.
4277
4278
Certification
application.
The
owner
or
operator
must
apply for
4279
certification
of
each
continuous
mercury
emission monitoring
system.
4280
The owner
or
operator
must
submit the
certification
application
in
4281
accordance
with
40
CFR
75.60, incorporated
by
reference
in
Section
4282
225.140,
and
each complete
certification
application
must
include
the
4283
infonnation
specified
in
40
CFR
75.63,
incorporated
by
reference
in
4284
Section
225.140.
4285
4286
)
Provisional
approval
of
certification
(or
recertification)
applications.
Upon
4287
the
successful
completion
of the
required
certification
(or
recertification)
4288
procedures
of this Section,
each continuous
mercury
emission
monitoring
4289
system
must
be deemed
provisionally
certified
(or
recertified)
for
use for a
4290
period
not
to exceed
120
days following
receipt
by
the Agency
of the
4291
complete certification
(or
recertification)
application
under
subsection
4292
(a)(4)
of
this
Section.
Data
measured
and recorded
by
a provisionally
4293
certified
(or
recertified)
continuous
emission
monitoring
system,
operated
4294
in
accordance
with
the
requirements
of Exhibit
B to
this
Appendix,
will
be
4295
considered
valid
quality-assured
data
(retroactive
to
the
date and time
of
4296
provisional
certification
or recertification),
provided
that
the Agency
does
4297
not invalidate
the
provisional
certification
(or
recertification)
by
issuing
a
4298
notice
of
disapproval
within 120
days
of receipt
by
the
Agency
of the
4299
complete
certification
(or recertification)
application.
Note
that
when the
4300
conditional
data
validation
procedures
of subsection
(b)(3)
of this Section
4301
are
used for the
initial
certification
(or
recertification)
of a continuous
JCAR350225-081 8507r01
4302
emissions monitoring
system, the date and time of provisional certification
4303
(or recertification)
of
the CEMS
may be
earlier
than the date and time
of
4304
completion
of the required certification (or recertification) tests.
4305
4306
Certification (or recertification)
application formal approval process.
The
4307
Agency will issue a notice of approval
or
disapproval
of the certification
4308
(or
recertification)
application to the owner or operator within 120
days
4309
after receipt
of the complete certification
(or recertification)
application.
In
4310
the event the Agency does not issue
such a
notice within 120
days after
4311
receipt, each
continuous emission monitoring system that meets
the
4312
performance requirements
of
this
Part and
is
included in the certification
4313
(or
recertification)
application will be deemed certified (or recertified)
for
4314
use under 35 Ill. Adm. Code 225.
4315
4316
Approval notice. If the certification (or recertification)
application
4317
is complete
and shows that each continuous emission monitoring
4318
system meets the performance requirements
of
this
Part, then the
4319
Agency
will issue a notice of approval of the certification
(or
4320
recertification) application
within
120
days after receipt.
4321
4322
Incomplete application notice. A certification (or recertification)
4323
application
will
be considered complete when all of the applicable
4324
information
required to be submitted in 40 CFR 75.63,
4325
incorporated
by
reference
in Section
225.140,
has been received
by
4326
the Agency. If the certification
(or
recertification)
application is
4327
not
complete,
then the Agency will issue a notice of
4328
incompleteness that provides
a reasonable timeframe for the
4329
designated representative to submit the additional information
4330
required
to complete
the certification
(or
recertification)
4331
application. If the designated representative has not
complied with
4332
the notice of incompleteness
by a
specified
due date, then the
4333
Agency may issue a notice of disapproval specified under
4334
subsection
(a)(4)(C)
of this Section. The 120day
review period
4335
will
not
begin prior to receipt of a complete application.
4336
4337
Disapproval notice. If the certification
(or
recertification)
4338
application
shows that any continuous emission monitoring
system
4339
does not meet the performance requirements
of this Part, or if
the
4340
certification
(or recertification)
application
is incomplete and the
4341
requirement for disapproval under subsection (a)(4)(B)
of this
4342
Section
has been met, the Agency must issue a written notice
of
4343
disapproval
of the certification
(or recertification)
application
4344
within 120 days after receipt.
By
issuing
the notice of disapproval,
JCAR350225-08 1 8507r01
4345
the provisional
certification
(or recertification)
is invalidated
by the
4346
Agency,
and the data measured and recorded
by
each uncertified
4347
continuous emission
or opacity monitoring system must not
be
4348
considered valid
quality-assured data as follows: from the hour of
4349
the
probationary calibration error test that began the initial
4350
certification
(or
recertification) test period (if the conditional
data
4351
validation procedures
of subsection (b)(3) of this Section were
4352
used to retrospectively validate
data);
or from the date and time of
4353
completion of the invalid certification or recertification
tests
(if
the
4354
conditional data
validation procedures of subsection (b)(3) of this
4355
Section
were not used). The owner or operator must follow
the
4356
procedures for loss
of
initial
certification in subsection
(a)(5)
of
4357
this Section for each continuous emission or opacity monitoring
4358
system
that is disapproved for
initial certification. For each
4359
disapproved
recertification, the owner or operator must follow
the
4360
procedures of subsection
(b)(5)
of
this Section.
4361
4362
)
Procedures for loss of certification.
When
the Agency issues a notice of
4363
disapproval
of a certification application or a notice of disapproval
of
4364
certification
status
(as
specified in subsection (a)(4) of this
Section),
then:
4365
4366
)
Until such time, date and hour as the continuous
mercury emission
4367
monitoring system can be adjusted, repaired or replaced
and
4368
certification tests successfully completed
(or,
if the conditional
4369
data validation
procedures in subsections
(b)(3)(B)
through
(I)
of
4370
this Section are used, until a probationary
calibration error test is
4371
passed following corrective actions in accordance with
subsection
4372
(b)(3)(B) of this Section),
the
owner
or operator must perform
4373
emissions testing pursuant to Section 225 .239.
4374
4375
The designated representative must submit a notification of
4376
certification retest dates
as
specified in
Section
225.250(a)(3)(A)
4377
and a new certification application according to the procedures
in
4378
Section
225.250(a)(3)(B):
and
4379
4380
The owner or operator
must repeat all certification tests or other
4381
requirements that were failed by the continuous
mercury emission
4382
monitoring
system, as indicated in the Agency’s notice of
4383
disapproval,
no
later
than 30 unit operating days after the date
of
4384
issuance of the notice of disapproval.
4385
4386
Recertification
Approval Process. Whenever the owner or operator makes
a
4387
replacement, modification
or change in a certified continuous mercury emission
JCAR350225-08 1
8507r01
4388
monitoring
system
that may significantly
affect the ability of the system
to
4389
accurately measure
or record the gas volumetric flow rate,
mercury concentration,
4390
percent moisture, or to meet the
requirements of Section 1.5
of
this
Appendix
or
4391
Exhibit
B to this Appendix, the owner
or operator must recertify the continuous
4392
mercury emission
monitoring
system, according
to
the
procedures in this
4393
subsection. Examples
of changes that require recertification
include: replacement
4394
of the analyzer; change
in location or orientation of the sampling probe
or site;
4395
and complete replacement of an existing
continuous
mercury emission monitoring
4396
system. The owner
or operator
must also recertify the continuous
emission
4397
monitoring
systems
for
a
unit
that has recommenced commercial operation
4398
following
a period of long-term cold storage
as
defined
in Section
225.130.
Any
4399
change to a flow monitor or
gas monitoring system for which a RATA is
not
4400
necessary will not
be considered a recertification event.
In addition, changing
the
4401
polynomial coefficients or K factors
of a flow monitor will require a 3-load
4402
RATA, but is not considered
to be a recertification event; however,
records
of the
4403
polynomial coefficients or K factors
currently in use must be maintained on-site
4404
in
a
format suitable
for inspection. Changing the coefficient or
K factors of a
4405
moisture monitoring system will
require a RATA, but is not considered
to be a
4406
recertification
event;
however, records of the coefficient
or K factors currently
in
4407
use
by
the moisture monitoring
system must be maintained on-site in
a format
4408
suitable
for inspection. In
such cases, any other tests that are necessary
to ensure
4409
continued
proper operation of
the monitoring system (e.g., 3-load flow RATAs
4410
following changes to flow monitor polynomial coefficients,
linearity checks,
4411
calibration error tests, DAHS verifications, etc.) must be
performed as diagnostic
4412
tests,
rather than
as
recertification
tests. The data validation procedures
in
4413
subsection
(b)(3)
of this Section
must be applied to RATAs associated with
4414
changes to flow or moisture monitor coefficients, and to linearity
checks,
7-day
4415
calibration error tests and
cycle time tests when these are required as
diagnostic
4416
tests. When the data
validation
procedures
of subsection
(b)(3)
of this Section
are
4417
applied in this manner,
replace
the word “recertification” with the word
4418
“diagnostic”.
4419
4420
jj
Tests required. For all recertification testing, the owner
or operator must
4421
complete all initial certification
tests in subsection
(c)
of this Section
that
4422
are applicable to the monitoring system, except
as
otherwise
approved
by
4423
the Agency. For diagnostic
testing after changing the flow rate
monitor
4424
polynomial coefficients, the owner
or operator must complete a 3-level
4425
RATA. For
diagnostic
testing after changing the K
factor
or mathematical
4426
algorithm
of a moisture
monitoring
system, the owner or
operator must
4427
complete
a RATA.
4428
4429
)
Notification of recertification test dates. The
owner, operator or designated
4430
representative must
submit notice of testing dates for
recertification under
JCAR350225-081
8507r01
4431
this subsection
as specified
in 40 CFR 75.61(a)(l)(ii),
incorporated
by
4432
reference
in Section 225.140,
unless
all
of the tests in subsection
(c) of this
4433
Section
are
required
for recertification, in which
case
the
owner
or
4434
operator
must provide
notice in accordance
with the notice provisions
for
4435
initial certification testing
in 40
CFR
75.61(a)(l)(i),
incorporated
by
4436
reference
in Section
225.140.
4437
4438
Recertification
test period requirements
and data validation.
The data
4439
validation
provisions
in subsections
(b)(3)(A)
through
(I)
of this Section
4440
will apply to
all mercury CEMS
recertifications and
diagnostic testing.
4441
The provisions
in subsections
(b)(3)(B) through
(I)
of this Section may
4442
also be applied
to initial certifications
(see
Sections
6.2(a), 6.3.1(a),
4443
6.3.2(a),
6.4(a)
and
6.5(f)
of Exhibit
A to this Appendix)
and may be
used
4444
to supplement
the linearity check
and RATA data validation
procedures
in
4445
Sections 2.2.3(b)
and
2.3.2(b)
of Exhibit
B to
this Appendix.
4446
4447
The
owner or operator must
report emission
data using a reference
4448
method
or another monitoring
system that has
been certified or
4449
approved
for use under this
Part,
in the
period extending from
the
4450
hour
of the replacement,
modification
or change
made
to
a
4451
monitoring system
that triggers the need
to perform recertification
4452
testing,
until
either: the hour of successful
completion of
all of
the
4453
required recertification
tests;
or
the hour in which a probationary
4454
calibration error
test (according
to subsection (b)(3)(B)
of this
4455
Section)
is performed and passed,
following all necessary
repairs,
4456
adjustments
or reprogramming
of the monitoring
system. The
first
4457
hour of quality-assured
data for
the recertified
monitoring system
4458
must
either be
the hour after
all recertification tests
have been
4459
completed
or, if conditional
data validation
is used, the first
4460
quality-assured
hour must
be determined in accordance
with
4461
subsections
(b)(3)(B)
through
(I)
of this Section.
Notwithstanding
4462
these
requirements,
if the replacement,
modification
or change
4463
requiring
recertification of the
CEMS
is such
that the historical
4464
data stream is
no longer representative
(e.g., where
the mercury
4465
concentration
and stack flow rate
change
significantly
after
4466
installation
of a wet
scrubber),
the owner or operator
must estimate
4467
the
mercury
emissions over
that time period
and notify the Agency
4468
within
15 days after the replacement,
modification
or change
4469
requiring
recertification
of the CEMS.
4470
4471
Once
the modification
or change to
the CEMS has been completed
4472
and all of the associated
repairs,
component replacements,
4473
adjustments, linearization
and reprogramming
of
the CEMS have
JCAR350225-08 1 8507r01
4474
been
completed, a
probationary calibration error test is required
to
4475
establish the beginning point
of the
recertification test period.
In
4476
this instance, the
first successful calibration error test of the
4477
monitoring system
following completion of all necessary repairs,
4478
component replacements,
adjustments,
linearization
and
4479
reprogramming
must be the probationary calibration error
test. The
4480
probationary
calibration
error test must be passed before any
of the
4481
required recertification
tests are commenced.
4482
4483
c)
Beginning
with
the hour of commencement of a recertification
test
4484
period, emission
data
recorded
by
the mercury
CEMS
are
4485
considered
to be conditionally valid, contingent upon the results
of
4486
the
subsequent recertification tests.
4487
4488
L’)
Each required recertification test must be completed no later
than
4489
the following
number of unit operating hours
(or
unit operating
4490
days) after the probationary calibration error test that initiates
the
4491
test
period:
4492
4493
For a linearity check and/or cycle time test, 168
4494
consecutive unit operating hours, as defined in 40 CFR
4495
72.2,
incorporated by reference in Section 225.140, or,
for
4496
CEMS
installed on common stacks or bypass stacks, 168
4497
consecutive
stack
operating hours,
as defined in
40
CFR
4498
72.2;
4499
4500
I)
For
a
RATA
(whether
normal-load or
multiple-load), 720
4501
consecutive unit operating hours, as defined in 40 CFR
4502
72.2, incorporated
by
reference in
Section
225.140,
or, for
4503
CEMS installed on common stacks or bypass stacks, 720
4504
consecutive
stack operating hours,
as defined in 40 CFR
4505
72.2;
and
4506
4507
jjjj
For a 7-day calibration error test, 21 consecutive unit
4508
operating
days,
as defined in 40 CFR 72.2,
incorporated
by
4509
reference in Section 225.140.
4510
4511
All recertification tests must be performed hands-off.
No
4512
adjustments
to the calibration of the mercury CEMS,
other than the
4513
routine calibration
adjustments
following daily calibration error
4514
tests
as described in Section
2.1.3
of Exhibit B to this Appendix,
4515
are permitted
during
the recertification
test period. Routine daily
4516
calibration error tests must be
performed
throughout the
O
t;
j•
CD
0
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Co
00
C
C
JCAR350225-08
1 8507r01
4560
(or stack)
operating hours. The
new recertification
test
4561
sequence must
not
be commenced
until
all necessary
4562
maintenance
activities, adjustments,
linearization
and
4563
reprogramming
of the CEMS
have been completed;
4564
4565
jj)
If
a linearity check,
RATA or cycle
time test is failed or
4566
aborted due to a problem
with the mercury
CEMS, all
4567
conditionally
valid
emission
data recorded
by
the
CEMS
4568
are invalidated, from
the hour of
commencement of the
4569
recertification
test period to the hour
in which the
test is
4570
failed or aborted,
except for the
case
in which a multiple-
4571
load
flow
RATA
is
passed
at one or
more load levels,
failed
4572
at a subsequent load
level, and the
problem that caused
the
4573
RATA
failure
is corrected without re-linearizing
the
4574
instrument. In that
case, data
invalidation
will be
4575
prospective,
from
the hour of failure
of the RATA until
the
4576
commencement of
the new recertification
test period.
Data
4577
from
the CEMS
remain invalid until
the hour in which
a
4578
new recertification
test period is
commenced, following
4579
corrective action,
and a probationary
calibration
error
test is
4580
passed, at
which time the conditionally
valid
status
of
4581
emission
data from the CEMS
begins again;
4582
4583
jjj
If a 7-day
calibration
error test is failed within
the
4584
recertification
test period,
previously-recorded
4585
conditionally
valid
emission data from the
mercury
CEMS
4586
are
not invalidated.
The conditionally
valid data status
is
4587
unaffected, unless the
calibration error on
the day
of the
4588
failed
7-day calibration
error test exceeds
twice the
4589
performance specification
in Section 3 of
Exhibit
A to
this
4590
Appendix,
as described
in subsection
(b)(3)(G)(iv)
of
this
4591
Section.
4592
4593
jy)
If a daily calibration
error test is failed during
a
4594
recertification
test period
(i.e.,
the results
of the test exceed
4595
twice the performance
specification in Section
3 of Exhibit
4596
A
to this
Appendix),
the CEMS is out-of-control
as
of the
4597
hour in which the calibration
error
test is failed. Emission
4598
data from the CEMS
will
be
invalidated
prospectively
from
4599
the hour of
the failed calibration
error test until
the hour of
4600
completion
of a subsequent
successful calibration
error
test
4601
following
corrective action,
at which time the
conditionally
4602
valid status
of data from
the
monitoring
system
resumes.
JCAR350225-08 1 8507r01
4603
Failure
to perform a required daily calibration error test
4604
during a recertification test
period
will also cause data
from
4605
the CEMS to be invalidated prospectively, from the hour in
4606
which the calibration
error test was due until the hour of
4607
completion of a subsequent
successful
calibration
error
test.
4608
Whenever a calibration error test is failed or missed during
4609
a
recertification
test period, no further recertification tests
4610
must be performed
until the required
subsequent
calibration
4611
error test has been
passed,
re-establishing the conditionally
4612
valid
status
of data from the monitoring
system.
If a
4613
calibration error test failure occurs while
a
linearity check
4614
or RATA is still in progress, the linearity check or RATA
4615
must be re-started.
4616
4617
y)
Trial
gas
injections
and trial RATA runs are permissible
4618
during the recertification
test
period,
prior to commencing a
4619
linearity check or RATA, for the purpose of optimizing the
4620
performance
of the
CEMS.
The
results of such gas
4621
injections
and trial runs will not affect the status of
4622
previously-recorded conditionally valid data or result in
4623
termination
of the recertification test period, provided that
4624
they meet the following
specifications
and conditions: for
4625
gas injections, the stable, ending monitor response
is within
4626
±
5 percent or within 5 ppm of the tag value of the
4627
reference
gas; for RATA trial runs, the average reference
4628
method reading and the
average CEMS
reading
for the run
4629
differ by no more than
±
10%
of the average reference
4630
method value or ± 15 ppm, or + 1.5% H
20or ± 0.02
4631
lb/mmBtu from the average reference method value,
as
4632
applicable;
no adjustments to the calibration of the CEMS
4633
are made following the trial injections or runs, other than
4634
the adjustments permitted
under
Section 2.1.3
of Exhibit B
4635
to this Appendix and the CEMS is not repaired, re
4636
linearized or
repro-ammed
(e.g., changing flow monitor
4637
polynomial coefficients,
linearity
constants or K-factors)
4638
after the
trial injections
or runs.
4639
4640
y
If the results of any trial gas injections or RATA runs
are
4641
outside the limits in subsection
(b)(3)(G)(v)
of this Section
4642
or if
the
CEMS
is repaired,
re-linearized or reprogrammed
4643
after the trial injections or runs,
the
trial injections
or runs
4644
will be counted as a failed linearity check or RATA
4645
attempt.
If this occurs, follow the procedures pertaining
to
JCAR350225-081
8507r01
4646
failed
and
aborted
recertification
tests in
subsections
4647
(b)(3)(G)(i)
and
(ii)
of this
Section.
4648
4649
ff
If any required
recertification
test
is not completed
within
its
4650
allotted time
period,
data validation
must be
done
as
follows.
For
a
4651
late linearity
test, RATA
or
cycle
time test
that
is
passed
on
the
4652
first
attempt,
data
from the
monitoring
system
will
be
invalidated
4653
from
the hour
of
expiration
of the
recertification
test
period until
4654
the hour
of
completion
of the
late test.
For a
late
7-day calibration
4655
error
test, whether
or not
it is passed
on the
first attempt,
data
from
4656
the
monitoring
system
will
also be invalidated
from
the hour
of
4657
expiration
of the
recertification
test
period
until the
hour of
4658
completion
of the
late test.
For a late
linearity
test, RATA
or
cycle
4659
time
test that is
failed
on
the first
attempt
or aborted
on the first
4660
attempt
due to
a
problem with
the monitor,
all conditionally
valid
4661
data
from the
monitoring
system
will be
considered
invalid back
to
4662
the hour
of the first
probationary
calibration
error test
that initiated
4663
the
recertification
test
period.
Data
from
the
monitoring
system
4664
will
remain
invalid
until the
hour of
successful
completion
of
the
4665
late
recertification
test and
any
additional
recertification
or
4666
diagnostic
tests
that are
required as
a
result
of changes
made
to the
4667
monitoring
system
to correct
problems
that caused
failure
of the
4668
late recertification
test.
4669
4670
If any required
recertification
test of a
monitoring
system
has
not
4671
been completed
by
the
end
of a
calendar quarter
and if
data
4672
contained
in the
quarterly
report
are
conditionally
valid
pending
4673
the
results
of tests
to be completed
in a
subsequent
quarter,
the
4674
owner
or operator
must indicate
this by
means
of a suitable
4675
conditionally
valid
data flag
in
the
electronic
quarterly
report,
and
4676
notification
within
the quarterly
report
pursuant
to Section
4677
225
.290(b)(1’)(E),
for
that quarter.
The owner
or operator
must
4678
resubmit
the report
for that quarter
if the
required
recertification
4679
test
is
subsequently
failed.
If
any
required
recertification
test is
not
4680
completed
by
the
end
of a particular
calendar
quarter but
is
4681
completed
no later
than
30
days
after
the
end
of that quarter
(i.e.,
4682
prior
to the
deadline
for submitting
the
quarterly
report
under 40
4683
CFR
75.64,
incorporated
by
reference
in Section
225.140),
the
test
4684
data
and results
may be submitted
with
the
earlier quarterly
report
4685
even
though
the
test dates
are from
the
next calendar
quarter.
In
4686
such instances,
if
the recertification
tests are passed
in accordance
4687
with the
provisions
of subsection
(b)(3)
of
this Section,
4688
conditionally
valid data
may be
reported as
quality-assured,
in lieu
JCAR350225-08 1 8507r01
4689
of reporting a conditional data
flag. In addition, if the owner or
4690
operator uses a conditionally
valid data flag in any of the four
4691
quarterly reports for a given
year, the owner or operator must
4692
indicate
the final status of the conditionally
valid
data
(i.e.,
4693
resolved
or
unresolved)
in the annual compliance certification
4694
report required under 40
CFR 72.90 for that year. The Agency may
4695
invalidate
any conditionally valid
data that
remains unresolved at
4696
the end
of a particular calendar year.
4697
4698
4)
Recertification application. The designated
representative must apply for
4699
recertification of
each continuous mercury emission monitoring system.
4700
The
owner
or operator must submit the recertification
application in
4701
accordance with 40 CFR
75.60, incorporated by reference in Section
4702
225.140, and
each complete recertification application
must
include
the
4703
information specified in 40 CFR
75.63, incorporated by reference in
4704
Section 225.140.
4705
4706
)
Approval
or disapproval of request for recertification.
The
procedures
for
4707
provisional certification
in subsection (a)(3) of this Section apply to
4708
recertification applications. The Agency will
issue a notice of approval,
4709
disapproval
or incompleteness according to the procedures
in subsection
4710
(a)(4) of
this
Section. Data from the monitoring system remain invalid
4711
until all required recertification
tests
have
been
passed
or until a
4712
subsequent probationary calibration
error test is passed, beginning a
new
4713
recertification test period. The owner or operator
must repeat all
4714
recertification
tests or other requirements, as indicated in the Agency’s
4715
notice of disapproval, no
later than 30 unit operating days after the date
of
4716
issuance of the notice of disapproval. The designated representative
must
4717
submit a notification of the
recertification retest dates, as specified in 40
4718
CFR
75.61(a)(1)(ii),
incorporated
by
reference in Section 225.140,
and
4719
must submit a new recertification
application according to the procedures
4720
in subsection
(b)(4) of this Section.
4721
4722
Initial
Certification
and Recertification Procedures. Prior to the applicable
4723
deadline in 35 Ill. Adm. Code 225 .240(b), the
owner or operator must conduct
4724
initial
certification
tests and in accordance with 40 CFR
75.63,
incorporated
by
4725
reference in Section 225.140,
the designated representative must submit an
4726
application to demonstrate that the continuous
emission monitoring
system
and
4727
components of the system meet the specifications in Exhibit
A to this Appendix.
4728
The
owner
or
operator must compare reference method values
with output from
4729
the
automated
data
acquisition
and handling system that is part of the continuous
4730
mercury emission monitoring system
being tested. Except as otherwise specified
4731
in subsections
(b)(1),
(d) and (e) of this Section,
and in Sections 6.3.1 and 6.3.2
of
JCAR350225-08 1 8507r01
4732
Exhibit A to this Appendix, the owner
or operator must perform the following
4733
tests
for
initial
certification
or recertification of continuous emission
monitoring
4734
systems or components according
to the requirements of Exhibit B to this
4735
Appendix:
4736
4737
LI
For each mercury concentration monitoring system:
4738
4739
A 7-day calibration error test;
4740
4741
)
A linearity check,
for
mercury monitors, perform this check with
4742
elemental mercury stmdards;
4743
4744
A relative accuracy test audit must be done on a ig!scm
basis;
4745
4746
A bias
test;
4747
4748
A cycle time
test;
4749
4750
For
mercury monitors a 3-level
system
integrity check,
using a
4751
NIST-traceable
source of oxidized mercury, as described in
4752
Section 6.2 of Exhibit
A to this Appendix. This test is not required
4753
for
a mercury monitor that does not
have a
converter.
4754
4755
For each
flow
monitor:
4756
4757
j
A 7-day calibration error
test;
4758
4759
Relative accuracy
test
audits, as follows:
4760
4761
A
single-load
(or
single-level)
RATA at the normal load
(or
4762
level),
as defined in Section
6.5.2.1(d)
of Exhibit
A to this
4763
Appendix,
for a flow
monitor
installed
on a peaking unit
or
4764
bypass stack, or for a flow monitor exempted from
4765
multiple-level RATA testing under
Section 6.5.2(e) of
4766
Exhibit
A to this Appendix;
4767
4768
jI
For all other flow monitors, a RATA at each
of the three
4769
load levels
(or
operating
levels)
corresponding to the
three
4770
flue
gas velocities described in Section
6.5.2(a)
of Exhibit
4771
A to this
Appendix;
4772
4773
A bias test for the single-load
(or
single-level) flow RATA
4774
described
in subsection
(c)(2)(B)(i)
of this Section; and
JCAR350225-0818507r01
4775
4776
)
A bias test (or bias
tests) for the 3-level flow
RATA
described
in
4777
subsection (c)(2)(B)(ii)
of this Section, at the following load or
4778
operational
levels:
4779
4780
j)
At each
load level designated as normal under Section
4781
6.5.2.1(d)
of
Exhibit
A to this Appendix, for units that
4782
produce electrical or thermal
output, or
4783
4784
)
At the operational level
identified as normal in Section
4785
6.5.2.1(d)
of Exhibit A to this Appendix, for units
that do
4786
not produce electrical or
thermal output.
4787
4788
)
For each diluent
gas monitor used only to monitor
heat input rate:
4789
4790
)
A
7-day calibration error test;
4791
4792
)
A
linearity
check;
4793
4794
c)
A relative accuracy test audit, where,
for an
02
monitor used
to
4795
determine
CO7
concentration, the
CO
2reference method must
be
4796
used
for the RATA; and
4797
4798
j.)
A cycle-time
test.
4799
4800
4)
For each
continuous moisture monitoring system consisting
of wet- and
4801
dry-basis
02
analyzers:
4802
4803
)
A
7-day
calibration
error test of each
02
analyzer;
4804
4805
])
A cycle time
test of each
02
analyzer;
4806
4807
c)
A linearity test
of
each
02
analyzer; and
4808
4809
j)
A RATA directly
comparing the percent moisture measured
by the
4810
monitoring system to a reference
method.
4811
4812
For each continuous moisture
sensor: A RATA directly comparing
the
4813
percent moisture measured
by
the monitor
sensor to a reference method.
4814
4815
)
For
a
continuous
moisture monitoring
system
consisting
of a temperature
4816
sensor and a data
acquisition and handling
system
(DAHS)
software
4817
component programmed with
a
moisture
lookup
table: A demonstration
JCAR350225-0818507r01
4818
that the correct moisture
value for each hour is being
taken from the
4819
moisture lookup tables and applied
to the emission calculations. At a
4820
minimum,
the demonstration must
be made at
three
different
temperatures
4821
covering
the normal
range
of stack temperatures from low to
high.
4822
4823
7)
For each sorbent trap monitoring
system, perform a RATA, on a jig!dscrn
4824
basis, and a bias test.
4825
4826
)
For the automated data acquisition
and handling system, tests designed
to
4827
verify the proper computation of hourly averages for
pollutant
4828
concentrations, flow rate, pollutant
emission rates and pollutant mass
4829
emissions.
4830
4831
)
The owner
or operator must provide
adequate
facilities for initial
4832
certification or recertification testing
that
include:
4833
4834
)
Sampling
ports
adequate for
test methods applicable to such
4835
facility,
such that:
4836
4837
j)
Volumetric
flow rate, pollutant
concentration and pollutant
4838
emission rates can be accurately determined
by applicable
4839
test
methods and procedures; and
4840
4841
jj)
A stack or
duct free of cyclonic flow during performance
4842
tests is available, as demonstrated
by applicable test
4843
methods and procedures.
4844
4845
)
Basic facilities
(e.g., electricity)
for sampling and testing
4846
quipment.
4847
4848
ci)
Initial Certification and Recertification
and Quality Assurance Procedures for
4849
Optional Backup Continuous Emission Monitoring
Systems.
4850
4851
D
Redundant
backups. The owner or operator of an
optional
redundant
4852
backup CEMS must comply with all
the requirements for initial
4853
certification and recertification according to the procedures
specified in
4854
subsections
(a), (b)
and
(c) of this Section. The owner or operator must
4855
operate the redundant
backup CEMS during all periods of unit operation,
4856
except for periods of calibration, quality
assurance,
maintenance
or repair.
4857
The owner or operator must perform upon the redundant backup
CEMS all
4858
quality
assurance
and quality control procedures specified in Exhibit
B to
4859
this Appendix, except
that the daily assessments in Section 2.1 of Exhibit
4860
B to this Appendix are
optional for
days
on which the redundant backup
JCAR350225-08
1 8507r01
4861
CEMS is not
used to report emission data under this Part. For any
day
on
4862
which
a redundant backup CEMS is
used to report emission data, the
4863
system must
meet all of the applicable daily assessment criteria in
Exhibit
4864
B to this Appendix.
4865
4866
)
Non-redundant backups. The owner or operator
of an optional non-
4867
redundant
backup CEMS or like-kind replacement analyzer must
comply
4868
with all of the
following requirements for initial certification, quality
4869
assurance, recertification and data reporting:
4870
4871
Except as provided in subsection (d)(2)(E)
of this Section, for a
4872
regular
non-redundant backup CEMS
(i.e.,
a non-redundant
backup
4873
CEMS that has its own separate probe,
sample
interface and
4874
analyzer), or
a non-redundant backup flow monitor, all of the
tests
4875
in subsection
(c)
of this Section are required for initial
certification
4876
of the system, except
for the 7-day calibration error test.
4877
4878
For
a
like-kind
replacement non-redundant
backup
analyzer
(i.e.,
a
4879
non-redundant backup analyzer
that uses the same probe and
4880
sample interface as a primary monitoring system), no initial
4881
certification
of the analyzer is required.
4882
4883
Each non-redundant backup
CEMS or like-kind replacement
4884
analyzer must comply with the
daily and quarterly quality
4885
assurance and quality control requirements in Exhibit B
to this
4886
Appendix for each
day and quarter that the non-redundant backup
4887
CEMS or like-kind
replacement
analyzer
is used to report data, and
4888
must meet the additional linearity and calibration error test
4889
requirements specified in this
subsection. The owner or operator
4890
must ensure
that each non-redundant backup CEMS or like-kind
4891
replacement analyzer passes a linearity check
(for
mercury
4892
concentration and
diluent gas monitors) or a calibration error
test
4893
(for
flow
monitors)
prior to each use for recording
and reporting
4894
emissions.
When
a
non-redundant
backup CEMS or like-kind
4895
replacement analyzer is brought into service, prior
to conducting
4896
the linearity
test, a probationary calibration error test
(as
described
4897
in subsection (b)(3)(B) of
this
Section),
which will begin a period
4898
of conditionally valid data, may be performed
in order to allow the
4899
validation of data retrospectively as follows. Conditionally
valid
4900
data from the
CEMS or like-kind replacement analyzer are
4901
validated back
to
the
hour of completion of the probationary
4902
calibration error test if the following conditions
are met: if no
4903
adjustments
are made to the CEMS
or
like-kind replacement
JCAR350225-081 8507r01
4904
analyzer
other
than
the allowable
calibration
adjustments
specified
4905
in Section 2.1.3 of Exhibit
B to this
Appendix between
the
4906
probationary calibration
error
test
and the successful
completion
of
4907
the
linearity test;
and if the linearity
test
is
passed
within
168 unit
4908
(or stack)
operating hours of the
probationary calibration
error test.
4909
However, if the
linearity
test
is performed within
168
unit or
stack
4910
operating
hours but is either
failed or aborted
due to a problem
4911
with the
CEMS or like-kind
replacement
analyzer,
then all of
the
4912
conditionally
valid
data
are invalidated back
to the hour
of
the
4913
probationary
calibration error
test, and data
from the non-
4914
redundant
backup
CEMS
or from the primary
monitoring
system
4915
of which
the like-kind replacement
analyzer,
is a part remain
4916
invalid until
the hour
of
completion of a successful
linearity
test.
4917
Notwithstanding
this requirement,
the conditionally
valid
data
4918
status may
be re-established
after a failed or
aborted linearity
4919
check,
if corrective action
is taken and a calibration
error test
is
4920
subsequently
passed.
However,
in no case will
the use of
4921
conditional
data validation
extend for more
than 168 unit or stack
4922
operating
hours
beyond
the date and time of
the original
4923
probationary
calibration
error test when
the analyzer was brought
4924
into
service.
4925
4926
For
each
parameter
monitored (i.e.,QQ
2
,
Hg or
flow
rate) at
4927
each unit or
stack,
a regular non-redundant
backup CEMS
may not
4928
be used to
report
data
at that
affected unit
or common
stack for
4929
more than
720 hours in any one
calendar year
(in
accordance
with
4930
40 CFR
75.74(c), incorporated
by reference
in Section
225.140),
4931
unless the
CEMS
passes a RATA
at
that unit
or stack. For each
4932
parameter monitored
at each
unit or stack, the use
of a like-kind
4933
replacement
non-redundant
backup
analyzer
(or
analyzers) is
4934
restricted to 720
cumulative
hours per calendar year,
unless
the
4935
owner
or
operator redesignates
the like-kind replacement
analyzers
4936
as components
of
regular
non-redundant
backup
CEMS and
each
4937
redesignated
CEMS passes a RATA
at that unit
or stack.
4938
4939
For each
regular non-redundant
backup
CEMS,
no more than
eight
4940
successive
calendar quarters
must elapse following
the quarter
in
4941
which the
last
RATA
of
the CEMS was done
at a particular
unit
or
4942
stack,
without performing
a subsequent
RATA. Otherwise, the
4943
CEMS
may not be used
to report
data
from that unit or stack
until
4944
the
hour
of completion
of a passing RATA
at that
location.
4945
JCAR350225-0818507r01
4946
)
Each regular
non-redundant
backup
CEMS
must be
represented
in
4947
the monitoring
plan required
under
Section
1.10 of this
Appendix
4948
as a separate
monitoring
system,
with unique
system
and
4949
component
identification
numbers.
When
like-kind
replacement
4950
non-redundant
backup
analyzers
are
used,
the
owner
or operator
4951
must
represent
each
like-kind
replacement
analyzer
used during
a
4952
particular
calendar
quarter
in the monitoring
plan
required
under
4953
Section
1.10
of this Appendix
as a
component
of a primary
4954
monitoring
system.
The
owner
or operator
must
also assign
a
4955
unique
component
identification
number
to
each
like-kind
4956
replacement
analyzer,
beginning
with the
letters
“LK” (e.g.,
LK1,
4957
LK2,
etc.)
and
must specify
the manufacturer,
model
and
serial
4958
number of
the
like-kind replacement
analyzer.
This
information
4959
may
be added,
deleted
or updated
as necessary,
from
quarter
to
4960
quarter. The
owner
or operator
must
also report
data from
the like-
4961
kind
replacement
analyzer
using the
system
identification
number
4962
of
the
primary
monitoring
system and
the assied
component
4963
identification
number of
the like-kind
replacement
analyzer.
For
4964
the purposes
of
the electronic
quarterly
report required
under
40
4965
CFR
75.64,
incorporated
by
reference
in Section
225.140,
the
4966
owner or operator
may
manually
enter the
appropriate
component
4967
identification
numbers
of any
like-kind
replacement
analyzers
used
4968
for data
reporting
during the
quarter.
4969
4970
)
When
reporting
data from a
certified regular
non-redundant
backup
4971
CEMS,
use
a
method
of determination
code
(MODC)
of”02”.
4972
When
reporting
data from
a
like-kind
replacement
non-redundant
4973
backup
analyzer,
use a MODC
of
??
17
H
(see Table
4a
under
Section
4974
1.11
of this
Appendix).
For
the
purposes
of
the electronic
quarterly
4975
report
required
under
40
CFR 75.64,
incorporated
by reference
in
4976
Section
225.140,
the owner
or
operator
may
manually
enter
the
4977
required
MODC
of” 17”
for a like-kind
replacement
analyzer.
4978
4979
ifi
For
non-redundant
backup
mercury
CEMS
and sorbent
trap
4980
monitoring
systems,
and for
like-kind
replacement
mercury
4981
analyzers,
the
following provisions
apply in
addition
to, or.
in
4982
some
cases,
in
lieu
of, the
general
requirements
in
subsections
4983
(d)(2)(A)
through
(H) of
this Section:
4984
4985
j)
When
a certified
sorbent
trap
monitoring
system
is brought
4986
into
service
as a regular
non-redundant
backup monitoring
4987
system,
the system
must
be operated
according
to the
JCAR350225-081
8507r01
4988
procedures in Section
1.3 of
this
Appendix and Exhibit D
4989
to this Appendix;
4990
4991
When a regular non-redundant backup mercury
CEMS or a
4992
like-kind replacement mercury analyzer is brought into
4993
service,
a linearity check with elemental mercury standards,
4994
as described
in subsection
(c)(1)(B)
of this Section and
4995
Section 6.2 of Exhibit A to this Appendix, and a
single-
4996
point system integrity check, as described in Section 2.6
of
4997
Exhibit
B to
this Appendix,
must be performed.
4998
Alternatively, a 3-level system integrity check, as described
4999
in subsection (c)(1)(E)
of
this Section
and subsection
(g)
of
5000
Section 6.2 in Exhibit A to this Appendix, may be
5001
performed in lieu of these two tests.
5002
5003
liii
The weekly single-point
system
integrity checks described
5004
in
Section
2.6
of Exhibit B to this Appendix are required
as
5005
long as a non-redundant backup mercury CEMS
or
like-
5006
kind replacement mercury analyzer remains in service,
5007
unless
the
daily calibrations
of the mercury analyzer are
5008
done using a NIST-traceable source
or
other
approved
5009
source of oxidized mercury.
5010
5011
Reference method backups. A monitoring system that is operated as
a
5012
reference method backup
system pursuant to the reference method
5013
requirements
of Methods 2, 3A, 30A and 30B in appendix A of 40
CFR
5014
60, incorporated by reference in Section
225.140,
need
not perform
and
5015
pass the certification tests required
by
subsection (c)
of
this
Section
prior
5016
to its use pursuant to this subsection.
5017
5018
Certification/Recertification Procedures for Either Peaking Unit or By-pass
5019
Stack/Duct
Continuous Emission Monitoring Systems. The owner or operator
of
5020
either
a peaking
unit or
by-pass stack/duct continuous emission monitoring
5021
system must comply with all the
requirements
for certification or recertification
5022
according to the
procedures
specified in subsections
(a),
(b) and
(c)
of this
5023
Section,
except
as follows: the owner or operator need only perform
one Nine-run
5024
relative accuracy test audit for certification or recertification of a flow monitor
5025
installed on the by-pass stack/duct or on the stack/duct used only by affected
5026
peaking
units. The relative accuracy
test
audit
must be performed during normal
5027
operation of the peaking units or the by-pass stack/duct.
5028
5029
fi
Certification/Recertification Procedures for Alternative Monitoring
Systems.
The
5030
designated representative representing
the owner or operator of each alternative
JCAR350225-081
8507r01
5031
monitoring
system
approved
by the Agency as equivalent
to or better
than a
5032
continuous emission
monitoring
system according
to
the
criteria in
subpart E of
5033
40
CFR 75, incorporated
by
reference
in Section 225.140,
must
apply for
5034
certification
to the Agency prior
to use of the
system under Subpart
B of
this
Part,
5035
and must apply
for recertification
to the Agency following
a replacement,
5036
modification,
or change according
to the procedures
in
subsection
(c) of this
5037
Section.
The owner or operator
of an alternative
monitoring system
must comply
5038
with the notification
and
application requirements
for certification
or
5039
recertification
according
to the procedures
specified in
subsections
(a)
and
(b)
of
5040
this
Section.
5041
5042
Section
1.5
Quality
Assurance
and Quality Control
Reiuirements
5043
5044
Continuous
Emission
Monitoring
Systems.
The owner or operator
of an affected
5045
unit must
operate, calibrate
and maintain
each continuous mercury
emission
5046
monitoring
system
used
to report mercury emission
data as
follows:
5047
5048
IJ
The
owner
or operator
must operate,
calibrate and maintain
each primary
5049
and redundant
backup continuous
emission monitoring
system according
5050
to the quality assurance
and quality
control procedures
in Exhibit
B to this
5051
Appendix.
5052
5053
)
The owner or
operator must
ensure that each
non-redundant
backup
5054
CEMS meets
the quality
assurance requirements
of Section
1.4(d) of
this
5055
Appendix
for each day
and quarter that
the system is used
to report data.
5056
5057
)
The
owner or
operator
must perform quality
assurance
upon
a reference
5058
method backup monitoring
system
according to the requirements
of
5059
Method
2 or
3A
in appendix A of 40 CFR
60, incorporated
by reference
in
5060
Section 225.140 (supplemented,
as
necessary, by guidance
from
the
5061
Administrator
or
the Agency), or one of
the mercury reference
methods
in
5062
Section
1.6
of this Appendix,
as applicable,
instead of the
procedures
5063
specified
in Exhibit
B of this Appendix.
5064
5065
}
Calibration
Gases. The owner
or operator must
ensure that all calibration
gases
5066
used to
quality assure the operation
of
the
instrumentation required
by
this
5067
Appendix must
meet
the
definition in 40 CFR
72.2,
incorporated
by
reference
in
5068
Section
225.140.
5069
5070
Section
1.6
Reference
Test
Methods
5071
5072
The owner or operator
must use the
following methods,
which
are found
in
5073
appendix A-4 to
40 CFR
60,
incorporated by reference
in
Section
225.140,
or
JCAR350225-08
1 8507r01
5074
have
been
published
by ASTM, to conduct
the
following
tests: monitoring system
5075
tests
for certification or
recertification
of continuous mercury
emission
5076
monitoring systems;
the
emission tests required
under
Section
1.15(c)
and (d)
of
5077
this
Appendix;
and required quality assurance
and
quality control tests:
5078
5079
jJ
Methods
1 or 1A are
the
reference
methods
for selection of sampling
site
5080
and
sample
traverses.
5081
5082
Method
2
or
its allowable
alternatives,
as provided in appendix
A to 40
5083
CFR 60, incorporated
by reference
in Section 225.140,
except for Methods
5084
2B
and 2E, are the
reference methods
for determination of volumetric
5085
flow.
5086
5087
)
Methods
3, 3A or 3B
are the reference methods
for the determination
of
5088
the
dry
molecular weight
07 and CO2
concentrations in the emissions.
5089
5090
4
Method
4
(either
the standard
procedure
described in Section
8.1 of the
5091
method or the moisture
approximation
procedure
described
in Section 8.2
5092
of the
method)
must
be used to correct
pollutant concentrations
from a dry
5093
basis to a wet basis (or
from
a wet
basis to a dry basis) and
must be used
5094
when relative accuracy
test
audits of
continuous moisture
monitoring
5095
systems are
conducted. For the purpose
of
determining
the stack gas
5096
molecular weight,
however,
the
alternative wet bulb-dry
bulb technique
5097
for approximating
the
stack
gas moisture content
described
in Section
2.2
5098
of Method
4 may be used in lieu
of the procedures
in Sections 8.1
and
8.2
5099
of the
method.
5100
5101
ASTM
D6784-02, Standard
Test
Method
for Elemental, Oxidized,
5102
Particle-Bound
and
Total
Mercury in Flue
Gas Generated from
Coal-Fired
5103
Stationary
Sources
(Ontario
Hydro
Method)
(incorporated
by
reference
5104
under Section
225.140)
is the reference method
for determining mercury
5105
concentration.
5106
5107
Alternatively,
Method
29 in appendix A-8
to
40
CFR
60,
5108
incorporated
by
reference
in Section
225.140, may be used,
with
5109
these caveats: The
procedures
for
preparation of mercury
standards
5110
and
sample
analysis
in Sections 13.4.1.1
through 13.4.1.3
ASTM
5111
D6784-02 (incorporated
by reference
under Section 225.140)
must
5112
be
followed instead
of
the
procedures
in Sections
7.5.33 and 11.1.3
5113
of Method
29 in appendix
A-8 to
40
CFR 60,
and the
OAJOC
5114
procedures
in Section 13.4.2
of ASTM D6784-02
(incorporated
by
5115
reference
under
Section
225.140)
must be performed
instead
of the
5116
procedures
in
Section
9.2.3 of Method 29
in appendix A-8 to
40
•
,•
••
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I
JCAR350225-081
8507r01
5160
emission
testing
required
under
Section
1.15(c)
and
(d)
of
this
5161
Appendix,
locate
the reference
method
test points
according
to
5162
Section 8.1
of
Method 30A,
and
if mercury
stratification
testing
is
5163
part of the
test
protocol,
follow
the
procedures
in Sections
8.1.3
5164
through
8.1.3.5
of Method
30A.
5165
5166
j.)
The owner
or operator
may
use
any
of the
following
methods,
which
are
found
in
5167
appendix
A
to
40
CFR
60,
incorporated
by
reference
in Section
225.140,
or have
5168
been
published
by
ASTM,
as a
reference method
backup
monitoring
system
to
5169
provide
quality-assured
monitor
data:
5170
5171
jJ
Method 3A
for
determining
02
or
CO2concentration;
5172
5173
)
Method
2,
or its
allowable
alternatives,
as
provided
in appendix
A to 40
5174
CFR
60, incorporated
by
reference
in Section
225.140,
except
for
Methods
5175
2B
and
2E,
for
determining
volumetric
flow. The
sample points
for
5176
reference
methods
must
be located
according
to the
provisions
of Section
5177
6.5.4
of Exhibit
A to this
Appendix.
5178
5179
)
ASTM D6784-02,
Standard
Test
Method for
Elemental,
Oxidized,
5180
Particle-Bound
and
Total
Mercury
in Flue
Gas
Generated
from Coal-Fired
5181
Stationary
Sources
(Ontario
Hydro
Method)
(incorporated
by reference
5182
under Section
225.140)
for determining
mercury
concentration;
5183
5184
4)
Method
29 in appendix
A-8
to
40
CFR
60,
incorporated
by
reference
in
5185
Section
225.140,
for
determining
mercury
concentration;
5186
5187
)
Method
30A
for
determining
mercury
concentration;
and
5188
5189
)
Method
30B
for
determining
mercury
concentration.
5190
5191
Instrumental
EPA Reference
Method
3A in
appendices
A-2
and A-4
of 40
CFR
5192
60,
incorporated
by
reference
in Section
225.140,
must
be
conducted
using
5193
calibration
gases as defined
in Section
5 of Exhibit
A
to
this
Appendix.
5194
Otherwise,
performance
tests must
be conducted
and data
reduced
in accordance
5195
with the test
methods
and
procedures
of
this Part
unless
the
Agency:
5196
5197
Specifies
or approves,
in
specific cases,
the
use
of a
reference
method
with
5198
minor
changes
in
methodology;
5199
5200
)
Approves the
use
of an
equivalent
method;
or
5201
JCAR350225-08
1 8507r01
5202
Approves shorter sampling
times and smaller
sample
volumes
when
5203
necessitated
by process variables
or
other factors.
5204
5205
Section
1.7
Out-of-Control Periods and System
Bias Testing
5206
5207
If an out-of-control
period occurs to a monitor or continuous
emission
monitoring
5208
system,
the owner
or operator must take corrective action and repeat
the tests
5209
applicable
to the out-of-control parameter
as described in Exhibit B to this
5210
Appendix.
5211
5212
j
For daily calibration error tests,
an out-of-control period occurs when the
5213
calibration error
of a pollutant concentration monitor exceeds the
5214
applicable specification in Section 2.1.4
of
Exhibit
B to this Appendix.
5215
5216
)
For quarterly
linearity checks, an out-of-control period
occurs when the
5217
error in linearity at any
of three gas concentrations
(low,
mid-range
and
5218
high) exceeds
the applicable specification in Exhibit A
to
this
Appendix.
5219
5220
For relative accuracy test audits,
an out-of-control period occurs when
the
5221
relative
accuracy
exceeds the applicable specification in Exhibit
A to this
5222
Appendix.
5223
5224
)
When a monitor or continuous emission
monitoring system is out-of-control,
any
5225
data
recorded by the monitor or monitoring
system are not quality-assured and
5226
must not be used in calculating monitor data availabilities pursuant
to Section
1.8
5227
of
this Appendix.
5228
5229
When
a monitor
or continuous emission monitoring
system
is out-of-control,
the
5230
owner or operator must take one of the following
actions until
the monitor or
5231
monitoring
system has successfully met the relevant criteria in Exhibits
A and B
5232
of this Appendix as demonstrated
by
subsequent tests:
5233
5234
jj
Use a certified backup monitoring
system
or a reference
method
for
5235
measuring and recording
emissions from the affected
units:
or
5236
5237
)
Adjust
the gas discharge paths from the affected units with emissions
5238
normally observed
by
the
out-of-control monitor or monitoring system
so
5239
that all exhaust gases are monitored
by
a certified
monitor or monitoring
5240
system meeting the requirements of Exhibits A and B to this
Appendix.
5241
5242
When the bias test indicates that
a flow monitor, a diluent monitoring system,
a
5243
mercury concentration monitoring system
or a
sorbent
trap monitoring
system
is
5244
biased
low
(i.e.,
the arithmetic mean of the differences between
the reference
JCAR350225-081
8507r01
5245
method
value
and the monitor
or monitoring
system
measurements
in
a
relative
5246
accuracy
test audit
exceed
the
bias statistic
in Section
7
of
Exhibit
A to
this
5247
Appendix),
the
owner or
operator must
adjust
the
monitor
or continuous
emission
5248
monitoring
system to eliminate
the
cause
of bias
such that
it
passes the
bias
test.
5249
5250
Section
1.8
Determination
of Monitor
Data
Availability
5251
5252
Following
initial certification
of
the
required
C0
2
Q
2
flow
monitoring
systems,
5253
Hg concentration
or
moisture
monitoring
systems
at
a
particular
unit or stack
5254
location
(i.e.,
the date
and
time
at which
quality-assured
data
begins
to be
5255
recorded
by
CEMSs
at that
location),
the owner
or
operator
must
begin
5256
calculating
the percent
monitor
data availability
as
described
in
subsection
(a)(1)
5257
of this
Section,
by
means
of
the
automated
data acquisition
and handling
system,
5258
and
the
percent monitor
data
availability
for each
monitored
parameter.
5259
5260
1)
Following
initial
certification,
the
owner or
operator
must use
Equation
8
5261
to
calculate, hourly,
percent
monitor
data availability
for
each calendar
5262
quarter.
5263
5264
Total unit operating
hours
for which
quality-assured
data
Percent
was
5265
recorded
for the calendar
quarter
monitor
data = X
100 (Eq.8)
5266
Availability
Total
unit
operating
hours
for
the
calendar
quarter
5267
5268
When
calculating
percent monitor
data
availability
using Equation
8,
the
5269
owner
or operator
must
include
all unit
operating
hours,
and
all monitor
5270
operating
hours
for which
quality-assured
data
were
recorded
by a
5271
certified primary
monitor;
a certified
redundant
or non-redundant
backup
5272
monitor
or a reference
method
for that
unit.
5273
5274
Section
1.9
Determination
of
Sorbent Trap
Monitorin2
Systems
Data
Availability
5275
5276
If a
primary
sorbent
trap
monitoring
system
has not been
certified
by
the
5277
applicable
compliance
date
specified
under
Subpart
B of
this
Part,
and if quality-
5278
assured mercury
concentration
data
from a
certified
backup
mercury
monitoring
5279
system,
reference
method
or
approved
alternative
monitoring
system
are
5280
unavailable,
the owner
or
operator
must perform
quarterly
emissions
testing
in
5281
accordance
with Section
225.239
until such time
the primary
sorbent
trap
5282
monitoring
system
has
been certified.
5283
5284
For
a
certified sorbent
trap
system,
a missing
data
period
will occur
in
the
5285
following
circumstances,
unless
quality-assured
mercury
concentration
data
from
5286
a
certified backup
mercury
CEMS,
sorbent
trap system,
reference
method
or
5287
approved
alternative
monitoring
system
are available:
JCAR350225-08
1 8507r01
5288
5289
1)
A gas sample
is
not
extracted
from
the
stack
during
unit
operation
(e.g.,
5290
during
a
monitoring
system malfunction
or
when the
system
undergoes
5291
maintenance);
or
5292
5293
The results
of the
mercury
analysis
for
the
paired
sorbent
traps
are
missing
5294
or invalid
(as
detennined
using
the
quality
assurance
procedures
in Exhibit
5295
D
to this Appendix).
The
missing
data
period
begins
with the
hour in
5296
which
the paired
sorbent
traps
for which
the
mercury
analysis
is missing
5297
or
invalid were
put into
service. The
missing data
period
ends at the
first
5298
hour
in which
valid
mercury
concentration
data are
obtained
with
another
5299
pair
of sorbent
traps (i.e.,
the hour
at which this
pair
of traps
was placed
in
5300
service),
or
with
a
certified
backup mercury
CEMS,
reference
method
or
5301
approved
alternative
monitoring
system.
5302
5303
c)
Following
initial certification
of
the
sorbent
trap monitoring
system,
begin
5304
reporting
the
percent monitor
data
availability
in accordance
with
Section 1.8
of
5305
this Appendix.
5306
5307
Section
1.10
Monitoring
Plan
5308
5309
The
owner
or operator
of an
affected
unit
must prepare
and
maintain
a
mercury
5310
emissions
monitoring
plan.
5311
5312
12)
Whenever
the
owner or operator
makes
a replacement,
modification
or change
in
5313
the
certified
CEMS, including
a
change
in the
automated
data
acquisition
and
5314
handling
system
or
in
the flue
gas handling
system, that
affects
information
5315
reported
in the
monitoring
plan
(e.g.,
a change
to a serial
number
for
a component
5316
of a
monitoring
system),
then
the owner
or
operator
must
update the
monitoring
5317
plan, by
the
applicable
deadline specified
in
40 CFR 75.62,
incorporated
by
5318
reference
in Section
225.140,
or
elsewhere
in this
Appendix.
5319
5320
Contents
of Monitoring
Plan
for
Specific
Situations.
The
following additional
5321
information
must
be included
in
the
monitoring
plan for
the
specific
situations
5322
described.
For
each monitoring
system
recertification,
maintenance
or other
5323
event,
the
designated
representative
must include
the following
additional
5324
information
in
electronic
format
in the
monitoring
plan:
5325
5326
1)
Component/system
identification
code;
5327
5328
)
Event
code
or
code
for
required
test;
5329
5330
)
Event begin
date
and
hour;
JCAR350225-08 1 8507r01
5331
5332
4
Conditionally
valid data period begin date and hour
(if
applicable)
5333
5334
)
Date
and hour that last test is successfully completed; and
5335
5336
Indicator of whether conditionally valid
data
were
reported at the end of
5337
the quarter.
5338
5339
Contents of the Mercury Monitoring Plan. The requirements
of subsection
(d)
of
5340
this
Section must be met on and after July 1, 2009. Each monitoring plan
must
5341
contain the information
in subsection
(d)(1)
of this Section in electronic format
5342
and the information in subsection
(d)(2)
of this Section in hardcopy format.
5343
Electronic storage of all monitoring plan information,
including
the hardcopy
5344
portions,
is permissible
provided
that a paper copy of the information can be
5345
furnished upon
request
for audit purposes.
5346
5347
fl
Electronic
5348
5349
The facility
ORISPL
number
developed by the Department of
5350
Energy and used in the National Allowance Data Base (or
5351
equivalent
facility
ID number assigned
by
USEPA, if the facility
5352
does
not have an ORISPL
number).
Also provide the following
5353
information
for each
unit
and
(as
applicable) for each common
5354
stack and/or
pipe,
and each multiple
stack and/or pipe involved in
5355
the monitoring plan:
5356
5357
A representation of the exhaust
configuration
for the units
5358
in
the monitoring plan. Provide the ID number of each
unit
5359
and assign
a
unique ID number
to each common stack,
5360
common pipe, multiple stack and/or
multiple
pipe
5361
associated with the units represented
in the monitoring
5362
plan. For common and multiple stacks and/or pipes,
5363
provide the activation date and
deactivation date
(if
5364
applicable) of each stack andlor pipe;
5365
5366
ii)
Identification of the monitoring
system
locations (e.g.,
at
5367
the unit-level,
on the common stack, at each
multiple
stack,
5368
etc.).
Provide an indicator
(flag) if the monitoring location
5369
is at a bypass stack or in the ductwork (breeching);
5370
5371
jjj
The
stack exit height
(ft)
above ground level and ground
5372
level elevation
above sea level, and the inside cross
5373
sectional area
(ft
2)
at the flue
exit and at the flow
JCAR350225-08
1 8507r01
5374
monitoring
location
(for
units with
flow monitors
only).
5375
Also use
appropriate
codes
to
indicate
the
materials
of
5376
construction
and the shapes
of
the
stack
or duct
cross-
5377
sections at
the flue exit
and
(if
applicable)
at
the
flow
5378
monitor
location;
5379
5380
The
types
of fuels fired
by
each
unit. Indicate
the start
and
5381
(if
applicable)
end
date of combustion
for
each type
of fuel,
5382
and
whether
the
fuel is the
primary,
secondary,
emergency
5383
or
startup
fuel;
5384
5385
y
The
types
of emission
controls
that are
used to reduce
5386
mercury
emissions
from each
unit.
Also provide
the
5387
installation
date, optimization
date
and retirement
date
(if
5388
applicable)
of the emission
controls,
and indicate
whether
5389
the controls
are an
original
installation;
and
5390
5391
yjj
Maximum
hourly
heat input
capacity
of
each unit.
5392
5393
)
For
each monitored
parameter
(i.e.,
mercury concentration,
diluent
5394
concentration
or flow)
at each monitoring
location,
specify
the
5395
monitoring
methodology
for the
parameter.
If the
unmonitored
5396
bypass stack
approach
is used
for a
particular
parameter,
indicate
5397
this by
means of
an appropriate
code.
Provide
the activation
5398
date/hour,
and
deactivation
date/hour
(if
applicable)
for each
5399
monitoring
methodology.
5400
5401
)
For each
required
continuous
emission
monitoring
system and
each
5402
sorbent
trap
monitoring
system
(as
defined
in Section
225.130),
5403
identify
and describe
the major
monitoring
components
in the
5404
monitoring
system
(e.g.,
gas analyzer,
flow
monitor,
moisture
5405
sensor,
DAHS software,
etc.).
Other
important
components
in
the
5406
system
(e.g.,
sample
probe,
PLC,
data
logger,
etc.)
may
also
be
5407
represented
in the
monitoring
plan,
if
necessary.
Provide
the
5408
following
specific
information
about
each
component
and
5409
monitoring
system:
5410
5411
j)
For
each
required monitoring
system,
assign
a unique,
3-
5412
character
alphanumeric
identification
code
to the system;
5413
indicate
the parameter
monitored
by the
system;
designate
5414
the
system
as
a primary,
redundant
backup,
non-redundant
5415
backup,
data
backup or
reference
method
backup
system,
as
5416
provided
in Section
1.2(d)
of this
Appendix:
and
indicate
JCAR350225-08 1 8507r01
5417
the system activation
date/hour and deactivation date/hour
5418
(as applicable).
5419
5420
j)
For
each component
of each
monitoring
system represented
5421
in the
monitoring plan, assign a unique,
3-character
5422
alphanumeric
identification code to the component;
5423
indicate the manufacturer,
model and serial number;
5424
designate the component type;
for gas analyzers, indicate
5425
the
moisture basis of measurement; indicate the
method of
5426
sample acquisition
or operation, (e.g., extractive
pollutant
5427
concentration
monitor or thermal flow monitor);
and
5428
indicate the component
activation
date/hour and
5429
deactivation
date/hour
(as applicable).
5430
5431
)
Explicit formulas,
using the component and
system
identification
5432
codes
for the primary monitoring system,
and containing all
5433
constants and factors
required to
derive
the
required emission
rates,
5434
heat input rates, etc. from the hourly
data recorded by the
5435
monitoring
systems. Formulas using the system and component
ID
5436
codes for backup monitoring
systems are required only if different
5437
formulas for the same parameter
are used for the primary and
5438
backup monitoring systems (e.g., if the
primary system measures
5439
pollutant
concentration
on a different moisture
basis
from
the
5440
backup
system). Provide the equation number or other
appropriate
5441
code for each emissions
formula
(e.g., use code F-i if Equation
F-i
5442
in
Exhibit
C
to this Appendix is used
to calculate
SO
2
mass
5443
emissions).
Also
identify each emissions formula with
a unique
5444
three character alphanumeric
code. The formula effective start
5445
date/hour
and
inactivation
date/hour
(as
applicable)
must
be
5446
included for each formula.
5447
5448
For
each parameter monitored with CEMS,
provide the following
5449
information:
5450
5451
Measurement
scale;
5452
5453
Maximum potential value
(and
method
of
calculation);
5454
5455
jjj
Maximum expected
value
(if
applicable) and method
of
5456
calculation;
5457
5458
jy
Span values and full-scale measurement ranges;
5459
JCAR350225-081 8507r01
5460
y
Daily calibration
units
of measure:
5461
5462
y)
Effective
date/hour, and
(if
applicable) inactivation
5463
date/hour
of each
span
value:
5464
5465
yj)
The default high range
value
(if applicable)
and the
5466
maximum
allowable
low-range value
for this
option.
5467
5468
)
If the monitoring system
or
excepted methodology
provides
for
the
5469
use of
a constant, assumed
or default value
for a parameter
under
5470
specific
circumstances,
then include the following
information
for
5471
each
such value for
each
parameter:
5472
5473
Identification
of the
parameter:
5474
5475
jj
Default, maximum,
minimum,
or
constant value, and
units
5476
of
measure for
the
value:
5477
5478
iii)
Purpose of the
value:
5479
5480
jy)
Indicator of
use, i.e., during
controlled hours,
uncontrolled
5481
hours or all
operating
hours:
5482
5483
y)
Type
of
fuel:
5484
5485
yj
Source
of the
value:
5486
5487
yjj)
Value
effective
date and
hour:
5488
5489
yjji
Date
and hour
value is no longer effective
(if
applicable):
5490
and
5491
5492
)
Unless otherwise
specified
in Section 6.5.2.1 of
Exhibit
A to
this
5493
Appendix,
for each unit
or common stack on
which hardware
5494
CEMS are installed:
5495
5496
j)
Maximum hourly gross
load
(in
MW, rounded to the
5497
nearest
MW, or
steam
load in
1000 lb/hr
(i.e., klb/hr),
5498
rounded
to
the nearest klb/hr, or
thermal
output
in
5499
mmBtu/hr, rounded
to the nearest
mmBtulhr),
for
units
that
5500
produce electrical
or thermal
output:
5501
5502
II)
The
upper and lower boundaries
of
the
range of operation
JCAR350225-0818507r01
5503
(as defined
in
Section 6.5.2.1
of
Exhibit
A to this
5504
Appendix),
expressed
in megawatts,
thousands
of
lb/hr
of
5505
steam,
mrnBtu/hr
of thermal
output
or
ft/sec
(as
5506
applicable);
5507
5508
jjfl
Except
for
peaking units,
identify
the most frequently
and
5509
second most
frequently
used load
(or
operating)
levels
(i.e.,
5510
low,
mid
or
high)
in accordance
with
Section
6.5.2.1
of
5511
Exhibit
A
to this Appendix,
expressed
in megawatts,
5512
thousands
of lb/hr
of steam,
mmBtu/hr
of thermal
output
or
5513
fl/sec
(as
applicable);
5514
5515
jy
An
indicator
of whether
the
second
most
frequently
used
5516
load
(or
operating)
level
is
designated
as normal
in
Section
5517
6.5.2.1
of
ExhibitAto
this Appendix;
5518
5519
y
The date
of the data
analysis used
to determine
the normal
5520
load
(or
operating)
levels and
the
two most
frequently-used
5521
load
(or
operating)
levels
(as applicable);
and
5522
5523
y)
Activation
and
deactivation
dates
and hours,
when
the
5524
maximum
hourly
gross load,
boundaries
of the range
of
5525
operation,
normal
load (or
operating)
levels or two
most
5526
frequently-used
load (or
operating)
levels change
and
are
5527
updated.
5528
5529
fl
For
each unit for
which
CEMS
are
not
installed,
the
maximum
5530
hourly
gross load
(in
MW, rounded
to
the
nearest
MW, or steam
5531
load
in klb/hr,
rounded
to the
nearest
klb/hr
or steam
load in
5532
mmBtu/hr,
rounded
to the nearest
mmBtu/hr);
5533
5534
II
For each
unit
with
a flow monitor
installed
on a rectangular
stack
5535
or
duct,
if a
wall effects
adjustment
factor
(WAY) is
determined
5536
and applied
to the
hourly
flow
rate data:
5537
5538
j)
Stack or duct
width
at the test
location,
ft;
5539
5540
jj)
Stack
or
duct
depth
at the test location,
ft;
5541
5542
liii
Wall
effects adjustment
factor
(WAF).
to
the
nearest
5543
0.0001;
5544
5545
jy
Method
of
determining
the
WAY;
JCAR350225-081
8507r01
5546
5547
y
WAF effective date
and hour;
5548
5549
yj)
WAF no longer
effective
date and
hour
(if
applicable):
5550
5551
yjj)
WAF determination
date:
5552
5553
yjji
Number
of
WAF
test runs;
5554
5555
j)
Number
of Method 1 traverse
points in the
WAF test;
5556
5557
)
Number
of test ports in
the WAF
test;
and
5558
5559
Number
of Method 1 traverse
points in the reference
flow
5560
RATA.
5561
5562
)
Hardcopy
5563
5564
Information,
including
(as
applicable):
Identification
of the test
5565
strategy; protocol
for the relative
accuracy test
audit; other relevant
5566
test information;
calibration
gas levels
(percent
of
span)
for the
5567
calibration
error test
and
linearity check and
span; and
5568
apportionment
strategies under
Sections
1.2
and 1.3 of this
5569
Appendix.
5570
5571
)
Description
of site locations
for each
monitoring component
in the
5572
continuous emission
monitoring
systems, including schematic
5573
diagrams
and engineering
drawings
specified in 40
CFR
5574
75.53(e)(2)(iv)
and
(v),
incorporated
by reference in
Section
5575
225.140
and any
other documentation
that demonstrates
each
5576
monitor location meets
the appropriate
siting
criteria.
5577
5578
c)
A
data flow diagram
denoting the complete
information
handling
5579
path
from output signals
of CEMS
components to final reports.
5580
5581
For
units monitored
by a continuous
emission monitoring
system,
a
5582
schematic diagram
identifying
entire gas handling system
from
5583
boiler
to stack
for all affected units,
using
identification
numbers
5584
for units, monitoring
systems and
components
and stacks
5585
corresponding
to the
identification
numbers provided
in
5586
subsections
(d)(1)(A) and
(C) of this Section.
The schematic
5587
diagram
must depict stack
height
and the
height of any monitor
5588
locations.
Comprehensive
and/or
separate schematic
diagrams
JCAR350225-08
1 8507r01
5589
must be used to
describe groups of units using a
common stack.
5590
5591
)
For units monitored
by a continuous emission monitoring
system,
5592
stack and duct engineering
diagrams showing the dimensions
and
5593
location
of fans, turning vanes, air
preheaters, monitor
5594
components,
probes, reference method
sampling ports and other
5595
equipment
that affects the monitoring system location,
5596
performance or quality
control checks.
5597
5598
Section 1.11 General Recordkeepin2 Provisions
5599
5600
The
owner or operator must meet all of
the applicable recordkeeping
requirements
of Section
5601
225.290 and of this Section.
5602
5603
)
Recordkeeping Requirements
for Affected Sources. The owner
or operator of any
5604
affected source
subject
to the requirements
of this Appendix must maintain
for
5605
each
affected unit
a
file
of all measurements, data, reports and
other information
5606
required by Subpart B of this Part
at the source in a form suitable for inspection
5607
for at least 3 years from the date of each record. The
file must contain the
5608
following information:
5609
5610
The data and information
required
in subsections (b) through
(h)
of this
5611
Section, beginning with the earlier of the
date of provisional certification
5612
or July 1,
2009;
5613
5614
The supporting data
and information used to calculate values required
in
5615
subsections
(b)
through
(g)
of this Section, excluding
the subhourly data
5616
points
used to compute
hourly averages under Section
1.2(c)
of
this
5617
Appendix, beginning with the earlier of the
date of provisional
5618
certification or July
1, 2009;
5619
5620
The data and information
required in Section 1.12 of this Appendix
for
5621
specific situations,
beginning with the earlier of the
date of provisional
5622
certification or July 1, 2009;
5623
5624
4
The certification test
data and information required in Section 1.13
of this
5625
Appendix for tests required under Section 1.4
of this Appendix, beginning
5626
with
the
date of
the first certification test performed,
the quality assurance
5627
and
quality
control
data
and information required in Section
1.13 of this
5628
Appendix for tests,
and the quality assurance/quality control plan
required
5629
under Section 1.5 of this
Appendix
and
Exhibit B to this Appendix,
5630
beginning
with
the date of provisional
certification;
5631
JCAR350225-08 1 8507r01
5632
The current
monitoring plan as
specified in Section 1.10 of this Appendix,
5633
beginning with
the
initial
submission required by
40
CFR
75.62,
5634
incorporated
by reference in
Section
225.140:
and
5635
5636
)
The quality control plan
as described in Section 1
of
Exhibit
B to this
5637
Appendix, beginning with
the date of provisional certification.
5638
5639
)
Operating Parameter
Record
Provisions. The owner or operator
must record for
5640
each hour the following information
on unit operating time, heat input rate
and
5641
load, separately
for each affected unit and also
for
each
group of units utilizing
a
5642
common stack and a common monitoring
system:
5643
5644
II
Date andhour;
5645
5646
7)
Unit operating time
(rounded
up to the nearest fraction of an hour
(in
5647
equal
increments
that
can range from one hundredth to one
quarter of an
5648
hour, at the option of the owner or
operator)):
5649
5650
7)
Hourly gross unit load (rounded
to nearest
MWge)
5651
5652
4)
Steam load
in
1000
lbs/hr at stated temperatures
and pressures, rounded
to
5653
the nearest 1000
lbs/hr.
5654
5655
Operating load range corresponding
to hourly gross load of 1 to
10, except
5656
for
units using a common stack, which
may use up to 20 load ranges
for
5657
stack or fuel flow,
as specified in the monitoring plan:
5658
5659
)
Hourly heat input
rate
(mmBtulhr,
rounded
to the nearest
tenth):
5660
5661
7)
Identification
code for formula used for heat
input as provided in Section
5662
1.10 of this Appendix: and
5663
5664
For Mercury CEMS units only, F-factor
for heat input calculation and
5665
indication of whether
the diluent cap was used for heat input
calculations
5666
for
the hour.
5667
5668
c)
Diluent Record Provisions. The
owner or operator of a unit using
a flow monitor
5669
and an
02
diluent monitor to determine heat
input, in accordance with Equation
F
5670
17 or
F-18
of
Exhibit
C to this Appendix,
or a unit that accounts for heat input
5671
using a flow monitor and
a CO
2diluent monitor
(which
is used only for heat input
5672
determination and is not used
as a CO
2pollutant concentration monitor)
must
5673
keep the following records for the
02
or
CO2
diluent monitor:
5674
JCAR350225-081 8507r01
5675
1)
Component-system identification
code as provided in Section 1.10
of this
5676
Appendix;
5677
5678
Date and hour;
5679
5680
)
Hourly
average diluent gas
(Q2
or
C0
2)
concentration
(in
percent, rounded
5681
to the nearest tenth);
5682
5683
4).
Percent monitor data availability for the diluent monitor
(recorded
to the
5684
nearest tenth
of a percent) calculated pursuant to Section 1.8 of this
5685
Appendix;
and
5686
5687
Method of determination code for diluent gas
(02
or
C0
2)
concentration
5688
data using Codes 1-55 in Table 4a
of this Section.
5689
5690
).
Missing Data Records. The owner
or
operator
must record the causes of any
5691
missing data
periods
and the actions taken by the owner or operator to correct
5692
such causes.
5693
5694
Mercury Emission
Record
Provisions
(CEMS’).
The owner or operator must
5695
record for each hour the
information required by this subsection for each affected
5696
unit using mercury CEMS in combination
with
flow rate, and (in certain cases)
5697
moisture, and diluent gas monitors, to determine mercury
concentration and (if
5698
applicable)
unit
heat input under Subpart B of this Part.
5699
5700
1)
For mercury concentration
during unit operation, as measured and
5701
reported from each certified primary monitor, certified
back-up monitor or
5702
other approved
method of emissions determination:
5703
5704
).
Component-system identification code as provided in Section
1.10
5705
of this Appendix;
5706
5707
).
Date and
hour;
5708
5709
c)
Hourly mercury concentration
(jig/scm,
rounded to the
nearest
5710
tenth).
For
a particular pair of sorbent traps, this will be the flow-
5711
proportional average concentration for
the data collection period;
5712
5713
j).
Method
of determination for hourly mercury concentration
using
5714
Codes
1-55 in Table
4a
of this Section; and
5715
5716
1).
The percent monitor data availability
(to
the nearest tenth of a
5717
percent) calculated pursuant to Section 1.8 of this Appendix.
JCAR350225-081
8507r01
5718
5719
For flue
gas
moisture
content during
unit
operation
(if
required),
as
5720
measured
and reported
from
each
certified
primary
monitor,
certified
5721
back-up
monitor
or other
approved method
of
emissions
determination
5722
(except
where
a default
moisture
value
is
approved
under 40
CFR 75.66,
5723
incorporated
by
reference
in Section
225.140):
5724
5725
)
Component-system
identification
code
as
provided
in Section
1.10
5726
of
this Appendix;
5727
5728
Date
and hour;
5729
5730
J
Hourly
average
moisture content
of flue
gas (percent,
rounded
to
5731
the
nearest
tenth).
If
the continuous
moisture
monitoring
system
5732
consists
of
wet-and
dry-basis
oxygen analyzers,
also
record
both
5733
the
wet- and
dry-basis
oxygen
hourly
averages
(in
percent
O
5734
rounded
to the
nearest
tenth);
5735
5736
Percent
monitor
data availability
(recorded
to the
nearest tenth
of a
5737
percent)
for the
moisture
monitoring
system
calculated
pursuant
to
5738
Section
1.8
of this
Appendix;
and
5739
5740
)
Method
of
determination
for hourly
average
moisture percentage
5741
using
Codes 1-55
in
Table 4a of
this Section.
5742
5743
For
diluent gas
(Q2
or
2
C0)
concentration
during
unit
operation
(if
5744
required),
as
measured
and
reported
from
each
certified
primary
monitor,
5745
certified
back-up
monitor
or other
approved
method
of emissions
5746
determination:
5747
5748
Component-system identification
code
as
provided
in Section
1.10
5749
of this
Appendix;
5750
5751
)
Date
and hour;
5752
5753
Hourly
average
diluent
gas
(02
or
C0
2)
concentration
(in
percent,
5754
rounded
to the
nearest
tenth);
5755
5756
Method
of determination
code for diluent
gas
(02
or
CO
5757
concentration
data
using
Codes 1-55
in
Table 4a
of this
Section;
5758
5759
5760
The
percent
monitor
data availability
(to
the
nearest tenth
of a
JCAR350225-08
1 8507r01
5761
percent)
for the
Q2
or
2
CO
monitoring
system (if
a
separate
O2or
5762
cQ2
monitoring system
is used
for heat input detennination)
5763
calculated
pursuant
to Section
1.8
of
this Appendix.
5764
5765
4,)
For stack gas volumetric
flow
rate
during unit operation,
as measured and
5766
reported from each
certified primary
monitor,
certified
back-up monitor
or
5767
other approved
method of emissions
determination, record
the information
5768
required under 40
CFR
75.5
7(c)(2)(i)
through
(vi),
incorporated by
5769
reference in
Section 225.140.
5770
5771
For mercury
mass emissions
during
unit
operation,
as measured and
5772
reported
from the certified primary
monitoring systems,
certified
5773
redundant or
non-redundant
back-up monitoring
systems, or other
5774
approved methods
of
emissions
determination:
5775
5776
)
Date and
hour;
5777
5778
,)
Hourly mercury
mass
emissions
(ounces, rounded
to three decimal
5779
places);
5780
5781
c)
Identification
code
for emissions formula
used to derive hourly
5782
mercury
mass
emissions
from mercury
concentration, flow
rate
5783
and moisture data,
as provided
in Section
1.10
of this
Appendix.
5784
5785
fi
Mercury
Emission
Record
Provisions
(Sorbent
Trap
Systems).
The
owner
or
5786
operator
must record
for
each
hour the information
required
by
this subsection,
5787
for
each affected unit using
sorbent
trap monitoring
systems in
combination with
5788
flow rate,
moisture,
and
(in
certain
cases)
diluent gas monitors,
to determine
5789
mercury
mass emissions
and (if required) unit
heat input under
this Part.
5790
5791
1)
For mercury concentration
during unit
operation, as measured
and
5792
reported from each
certified primary
monitor, certified back-up
monitor
or
5793
other approved method
of emissions determination:
5794
5795
)
Component-system
identification
code as provided in
Section 1.10
5796
of this
Appendix;
5797
5798
,)
Date
and hour;
5799
5800
Hourly
mercury
concentration
(ig/dscm,
rounded to the nearest
5801
tenth).
For
a particular
pair of sorbent
traps, this will be the
flow-
5802
proportional average
concentration
for the data collection
period;
5803
JCAR350225-081
8507r01
5804
)
Method
of
determination
for
hourly average
mercury
concentration
5805
using
Codes 1-55
in Table
4a of this Section;
and
5806
5807
j)
Percent
monitor
data availability
(recorded
to the
nearest tenth
of a
5808
percent)
calculated
pursuant
to Section
1.8 of this
Appendix;
5809
5810
7)
For flue
gas moisture
content
during unit
operation,
as
measured
and
5811
reported
from each
certified primary
monitor,
certified
back-up
monitor or
5812
other approved
method
of emissions
determination
(except
where
a default
5813
moisture
value
is
approved
under
40
CFR 75.66,
incorporated
by
reference
5814
in Section
225.140),
record the
information
required under
subsections
5815
(e)(2)(A)
through
(E)
of
this Section;
5816
5817
For
diluent gas
(02
or
2
C0)
concentration
during unit
operation
(if
5818
required
for heat
input
determination),
record
the
information
required
5819
under
subsections
(e)(3)(A)
through
(E) of
this Section.
5820
5821
4)
For
stack
gas volumetric
flow
rate during
unit operation,
as measured
and
5822
reported
from each
certified
primary monitor,
certified
back-up
monitor
or
5823
other
approved
method
of emissions
determination,
record
the information
5824
required
under
40
CFR
75.57(c)(2)(i)
through
(vi),
incorporated
by
5825
reference
in
Section
225.140.
5826
5827
For mercury
mass emissions
during
unit operation,
as measured
and
5828
reported
from the
certified
primary
monitoring
systems,
certified
5829
redundant
or
non-redundant
back-up
monitoring
systems
or other
5830
approved
methods
of
emissions
determination,
record the
information
5831
required
under
subsection
(e)(5)
of this
Section.
5832
5833
Record
the average
flow
rate of stack
gas
through
each
sorbent trap
(in
5834
appropriate
units, e.g.,
liters/mm,
cc/mi
dscmlmin).
5835
5836
7)
Record the
gas flow
meter
reading
(in
dscm,
rounded
to
the nearest
5837
hundredth)
at
the beginning
and
end of the collection
period
and at
least
5838
once in each
unit operating
hour
during the
collection
period.
5839
5840
)
Calculate
and record
the ratio
of the bias-adjusted
stack
gas flow
rate to
5841
the sample
flow rate,
as
described
in Section
11.2
of Exhibit
D to
this
5842
Appendix.
5843
5844
Table
4a. — Codes
for
Method
of Emissions
and
Flow Determination
Code
5845
Hourly
emissions/flow
measurement
or estimation
method
5846
JCAR350225-0818507r01
1
Certified primary
emission/flow
monitoring
system.
2
Certified backup
emission/flow
monitoring
system.
3
Approved alternative
monitoring
system.
4
Reference
method.
17
Like-kind replacement
non-redundant
backup
analyzer.
32
Hourly Hg
concentration
determined from analysis
of a
single
trap multiplied
by a factor of 1.111
when one of the
paired
traps is invalidated
or
damaged
(See
Appendix K,
Section
8).
33
Hourly
Hg concentration
determined
from the trap resulting
in the
higher
Hg concentration
when
the
relative
deviation
criterion
for the
paired traps is not met
(See Appendix K,
Section
8).
40
Fuel
specific default value
(or
prorated
default value) used
for the
hour.
54
Other
quality assured methodologies
approved
through
petition.
These
hours
are included in missing
data lookback
and
are treated as unavailable
hours
for percent monitor
availability
calculations.
55
Other
substitute
data approved through
petition. These
hours are not included
in missing
data lookback and are
treated as unavailable
hours
for percent monitor
availability
calculations.
5847
5848
5849
Section
1.12
General Recordkeeping
Provisions
for Specific
Situations
5850
5851
The owner or
operator must meet all
of the applicable
recordkeeping requirements
of this
5852
Section.
Tn
accordance
with 40 CFR
75.34,
incorporated
by reference in
Section
225.140,
the
5853
owner or operator
of an affected unit
with
add-on
emission controls must
record the applicable
5854
information
in this
Section for each hour
of missing
mercury
concentration
data. Except
as
5855
otherwise
provided
in
40
CFR 75.34(d),
incorporated
by
reference
in
Section 225.140, for
units
5856
with
add-on mercury
emission controls,
the
owner or
operator must record:
5857
5858
Parametric
data that demonstrate,
for
each
hour of missing
mercury
emission
data,
5859
the proper operation
of the add-on
emission controls, as
described in the
quality
5860
assurance/quality
control
program for
the unit. The
parametric data must
be
5861
maintained on site and
must
be submitted,
upon request,
to
the Agency.
5862
Alternatively, for
units equipped
with flue gas desulfurization
(FGD)
systems,
the
5863
owner or operator
may use quality-assured
data
from a certified
SO
2
monitor
to
5864
demonstrate proper
operation
of the emission controls
during periods
of missing
5865
mercury data;
5866
JCAR350225-081
8507r01
5867
)
A
flag indicating, for each
hour of missing
mercury emission
data,
either
that the
5868
add-on
emission
controls
are operating
properly,
as evidenced
by all
parameters
5869
jffig
within the ranges
specified in the
quality assurance/quality
control
program,
5870
or that the add-on emission
controls
are not operating properly.
5871
5872
Section
1.13
Certification,
Quality
Assurance
and Quality
Control
Record
Provisions
5873
5874
The owner or
operator must
meet all of the applicable
recordkeeping
requirements
of
this
5875
Section.
5876
5877
Continuous Emission
Monitoring
Systems.
The owner or operator
must record
the
5878
applicable
information in
this Section for each
certified monitor
or certified
5879
monitoring system
(including
certified backup
monitors)
measuring
and recording
5880
emissions
or
flow from an affected
unit.
5881
5882
1).
For
each flow monitor, mercury
monitor
or diluent gas monitor
(including
5883
wet- and
dry-basis
02
monitors used to determine
percent
moisture),
the
5884
owner
or operator must record
the following
for all daily and
7-day
5885
calibration
error
tests,
all daily system
integrity checks and
all off-line
5886
calibration
demonstrations,
including any
follow-up
tests after corrective
5887
action:
5888
5889
Component-system
identification
code
(on and after January
1,
5890
2009,
only the component
identification
code is
required);
5891
5892
i)
Instrument
span and
span
scale;
5893
5894
Date
and hour;
5895
5896
L)
Reference
value
(i.e.,
calibration gas
concentration
or reference
5897
signal
value,
in ppm
or other appropriate
units);
5898
5899
)
Observed
value
(monitor
response
during
calibration,
in ppm
or
5900
other
appropriate units);
5901
5902
Percent
calibration
error
(rounded
to
the nearest tenth
of a percent)
5903
(flag
if using alternative
performance
specification for
low
emitters
5904
or
differential
pressure
flow monitors);
5905
5906
Reference signal
or
calibration
gas
level:
5907
5908
For
7-day
calibration error
tests, a test number
and reason for
test;
5909
JCAR350225-081 8507r01
5910
II
For 7-day calibration
tests for certification or
recertification,
a
5911
certification from the cylinder gas vendor or CEMS vendor that
5912
calibration
gas, as defined in 40 CFR 72.2, incorporated by
5913
reference in Section 225.140,
and Exhibit A to this
Appendix, was
5914
used to conduct calibration error testing;
5915
5916
j)
Description
of any
adjustments,
corrective actions or maintenance
5917
prior to a passed test or following
a
failed test; and
5918
5919
)
Indication
of
whether
the unit is off-line or on-line.
5920
5921
For each flow monitor, the
owner or operator must record
the following
5922
for all daily interference checks, including any follow-up tests after
5923
corrective action.
5924
5925
A)
Component-system identification code
(after January
1, 2009,
only
5926
the
component identification code is required);
5927
5928
)
Date and hour;
5929
5930
)
Code indicating whether
monitor
passes or
fails the interference
5931
check; and
5932
5933
)
Description of any
adjustments,
corrective actions or maintenance
5934
prior
to a passed test or following a failed test.
5935
5936
For each mercury concentration monitor or diluent gas monitor (including
5937
wet- and
dry-basis
monitors
2
Q
used to
determine percent moisture),
the
5938
owner or operator must record the following for the initial and all
5939
subsequent linearity checks
and
3-level
system integrity
checks
(mercury
5940
monitors with converters only), including any follow-up tests after
5941
corrective
action:
5942
5943
A)
Component-system identification code
(on
and after July
1, 2009,
5944
only the
component identification code is required);
5945
5946
)
Instrument span and span scale
(only
span scale is
required
on and
5947
after
July 1, 2009);
5948
5949
)
Calibration gas level;
5950
5951
j)
Date and time
(hour
and
minute)
of each gas injection at each
5952
calibration
gas level;
JCAR350225-08
1
8507r01
5953
5954
)
Reference
value
(i.e.,
reference
gas concentration
for
each gas
5955
injection
at each calibration
gas
level, in
ppm
or other
appropriate
5956
units);
5957
5958
f)
Observed
value
(monitor
response
to each
reference
gas injection
5959
at each
calibration
gas level,
in ppm
or other appropriate
units);
5960
5961
)
Mean of
reference
values
and
mean
of
measured
values at
each
5962
calibration
gas
level;
5963
5964
I)
Linearity
error
at
each
of the reference
gas
concentrations
(rounded
5965
to
nearest
tenth
of a percent)
(flag
if using
alternative
perfoance
5966
specification);
5967
5968
Test
number
and
reason
for test (flag
if
aborted test);
and
5969
5970
j)
Description
of any
adjustments,
corrective
action
or maintenance
5971
prior to a
passed
test or following
a
failed test.
5972
5973
4)
For each
differential
pressure
type
flow
monitor,
the owner
or operator
5974
must
record items
in
subsections
(a)(4)(A)
through
(E)
of this Section,
for
5975
all quarterly
leak
checks,
including
any
follow-up
tests after corrective
5976
action.
For
each
flow
monitor,
the owner
or operator
must
record items
in
5977
subsections
(a)(4)(F)
and (G)
of this
Section for
all
flow-to-load
ratio
and
5978
gross heat
rate tests:
5979
5980
)
Component-system
identification
code
(on
and after
July
1, 2009,
5981
only
the system
identification
code
is
required).
5982
5983
)
Date
and hour.
5984
5985
c)
Reason
for
test.
5986
5987
I)
Code
indicating
whether monitor
passes
or fails the
quarterly
leak
5988
check.
5989
5990
Description
of any
adjustments,
corrective
actions
or maintenance
5991
prior
to a
passed
test or
following
a failed test.
5992
5993
)
Test data
from the
flow-to-load
ratio
or
gross
heat rate (GHR)
5994
evaluation,
including:
5995
JCAR350225-081
8507r01
5996
Monitoring
system identification
cocj
5997
5998
Calendar
year
and quarter;
5999
6000
jjj)
Indication
of
whether
the test
is a
flow-to-load
ratio
or
6001
gross
heat
rate evaluation;
6002
6003
jy)
Indication
of whether
bias
adjusted
flow rates
were
used:
6004
6005
y)
Average
absolute
percent difference
between
reference
6006
ratio
(or GHR)
and
hourly
ratios
(or
GHR
values):
6007
6008
yj)
Test
result;
6009
6010
yj)
Number
of hours
used in final
quarterly
average;
6011
6012
yjji
Number
of hours
exempted
for
use of a
different fuel
type;
6013
6014
j)
Number
of hours
exempted
for
load ramping
up or
down;
6015
6016
y)
Number
of hours
exempted
for
scrubber
bypass;
6017
6018
çj)
Number
of hours
exempted
for
hours
preceding
a normal-
6019
load flow
RATA;
6020
6021
jj
Number
of
hours
exempted for
hours
preceding
a
6022
successful
diagnostic
test,
following
a documented
monitor
6023
repair
or
major
component
replacement;
6024
6025
çjji
Number
of hours
excluded for
flue
gases discharging
6026
simultaneously
thorough
a
main
stack and
a bypass stack;
6027
and
6028
6029
4y)
Test
number.
6030
6031
)
Reference
data
for
the
flow-to-load
ratio
or
gross heat
rate
6032
evaluation,
including
(as
applicable):
6033
6034
1)
Reference
flow
RATA end
date and
time;
6035
6036
jj)
Test
number of
the reference
RATA;
6037
6038
jjj
Reference
RATA
load
and load
level;
JCAR350225-081
8507r01
6039
6040
jy
Average reference
method flow
rate during reference
flow
6041
RATA;
6042
6043
y)
Reference
flow/load ratio;
6044
6045
yj
Average
reference
method diluent gas concentration
during
6046
flow
RATA and diluent
gas units of
measure;
6047
6048
yjj
Fuel
specific
Fd-or
Fe-factor
during flow
RATA and F
6049
factor
units
of measure;
6050
6051
yjji
Reference
gross heat
rate
value;
6052
6053
j)
Monitoring
system
identification code;
6054
6055
Average
hourly
heat
input rate during RATA;
6056
6057
çj)
Average
gross unit
load;
6058
6059
jj
Operating load level;
and
6060
6061
jji
An indicator
(flag) if separate reference
ratios are
6062
calculated
for each multiple
stack.
6063
6064
)
For each flow monitor,
each
diluent gas
(02
or
C0
2)
monitor
used to
6065
determine
heat
input,
each moisture monitoring
system, mercury
6066
concentration monitoring
system, each sorbent
trap
monitoring
system
and
6067
each
approved alternative
monitoring
system, the owner or operator
must
6068
record the following
information for the initial
and
all subsequent
relative
6069
accuracy
test audits:
6070
6071
)
Reference methods
used.
6072
6073
Individual test run
data
from the
relative
accuracy test
audit for
the
6074
flow
monitor,
CO
2
emissions concentration
monitor-diluent
6075
continuous
emission
monitoring
system, diluent gas
(02
or
CO
6076
monitor used
to determine
heat
input, moisture monitoring
system,
6077
mercury
concentration monitoring
system, sorbent
trap monitoring
6078
system
or approved alternative
monitoring
system, including:
6079
6080
Date,
hour
and minute of beginning
of test run;
6081
JCAR350225-08
1 8507r01
6082
j)
Date,
hour and minute of end of test
run;
6083
6084
lii)
Monitoring system identification code;
6085
6086
jy)
Test number
and
reason
for test;
6087
6088
yl
Operating level
(low,
mid, high or
normal, as appropriate)
6089
and number
of operating levels comprising test;
6090
6091
y
Normal
load
(or
operating
level)
indicator
for flow RATAs
6092
(except
for peaking units);
6093
6094
yjj)
Units
of measure;
6095
6096
yjji
Run number;
6097
6098
Run value from CEMS being tested,
in the appropriate
6099
units of measure;
6100
6101
Run value
from reference method, in
the appropriate units
6102
of measure;
6103
6104
j)
Flag value
(0,
1 or
9, as appropriate) indicating whether
run
6105
has been used in calculating relative
accuracy and bias
6106
values
or whether the test was aborted
prior to completion;
6107
6108
çjj)
Average gross unit load, expressed
as a total gross unit
6109
load,
rounded
to the nearest MWe, or as steam
load,
6110
rounded to the nearest
1000 lb/hr. except for units that
do
6111
not produce
electrical or thermal output; and
6112
6113
jji
Flag to indicate
whether an alternative performance
6114
specification has been used.
6115
6116
Calculations
and tabulated results, as follows:
6117
6118
j)
Arithmetic mean
of
the
monitoring system measurement
6119
values
of the reference method
values, and of their
6120
differences,
as
specified
in
Equation
A—7 in Exhibit A to
6121
this Appendix;
6122
6123
Ii.1
Standard deviation, as
specified in Equation A—8 in Exhibit
6124
A to
this Appendix;
JCAR350225-08
1 8507r01
6125
6126
jjj)
Confidence coefficient,
as specified in Equation
A—9 in
6127
Exhibit
A to this Appendix;
6128
6129
jy
Statistical t value
used in
calculations;
6130
6131
)
Relative
accuracy test results,
as specified
in Equation
A—
6132
10 in Exhibit
A to this Appendix. For multi-level
flow
6133
monitor tests the relative
accuracy
test results must
be
6134
recorded
at each load
(or
operating) level
tested.
Each
load
6135
(or
operating) level
must be expressed as a total gross
unit
6136
load, rounded
to the nearest MWe, or
as steam load,
6137
rounded to the nearest
1000 lb/hr. or as otherwise specified
6138
by the Agency,
for units that do not produce electrical
or
6139
thermal output;
6140
6141
yj
Bias
test results as specified in Section 7.4.4
in
Exhibit
A to
6142
this Appendix;
and
6143
6144
Description
of any
adjustment,
corrective action or
maintenance
6145
prior to a passed
test or following a failed or aborted
test.
6146
6147
j)
For
flow monitors, the equation
used to linearize the flow
monitor
6148
and the
numerical values of the
polynomial coefficients or K
6149
factors of that
equation.
6150
6151
For
moisture monitoring systems, the
coefficient or K factor
or
6152
other mathematical
algorithm used to adjust the monitoring
system
6153
with respect
to the reference method.
6154
6155
j
For each mercury
concentration monitor, and
each CO2or
02
monitor
6156
used to determine heat input, the
owner or operator must record
the
6157
following information
for the cycle time test:
6158
6159
Component-system
identification code
(on
and after July 1, 2009,
6160
only the component
identification code is required);
6161
6162
Date:
6163
6164
)
Start and end times;
6165
6166
Upscale
and downscale cycle
times for each component;
6167
JCAR350225-08 1 8507r01
6168
Stable start monitor
value:
6169
6170
Stable end monitor
value:
6171
6172
Reference
value
of
calibration
gases:
6173
6174
ll
Calibration gas
level:
6175
6176
Total cycle
time:
6177
6178
Reason for
test:
and
6179
6180
j
Test number.
6181
6182
D
In addition to the information in subsection (a)(5) of this Section, the
6183
owner or operator
must record, for each
relative
accuracy test audit,
6184
supporting information sufficient to substantiate compliance with all
6185
applicable
Sections and Appendices in this Part. Unless otherwise
6186
specified
in this Part or in an applicable test method,
the
information
in
6187
subsections (a)(7)(A) through (H) of this Section may be recorded either
6188
in hard copy format, electronic format or a combination of the two, and
6189
the
owner or
operator must maintain this information in a format suitable
6190
for inspection and audit purposes. This RATA
supporting
information
6191
must include, but must not be limited
to,
the following data elements:
6192
6193
For each
RATA using Reference Method 2 (or its allowable
6194
alternatives)
in appendix A to 40 CFR
60,
incorporated
by
6195
reference in Section 225.140, to determine volumetric flow rate:
6196
6197
j)
Information indicating whether or not the location meets
6198
requirements of Method 1 in appendix
A
to 40
CFR 60,
6199
incorporated
by reference in Section
225.140:
and
6200
6201
jj
Information
indicating whether
or not the equipment passed
6202
the
required
leak checks.
6203
6204
For each run of each RATA
using Reference Method 2
(or
its
6205
allowable alternatives in appendix A
to
40 CFR
60,
incorporated
6206
by reference in Section
225.140)
to determine volumetric flow
6207
rate, record
the following data elements
(as
applicable to the
6208
measurement
method
used):
6209
6210
j)
Operating
level
(low,
mid, high or normal, as
appropriate):
JCAR350225-08
1
8507r01
6211
6212
jj)
Number
of reference
method
traverse
points;
6213
6214
Average
stack
gas temperature
(°F);
6215
6216
jyj
Barometric
pressure
at test
port
(inches
of
mercury);
6217
6218
Stack
static
pressure
(inches
of H
7
Q)j
6219
6220
yj)
Absolute
stack
gas
pressure
(inches
of
mercury);
6221
6222
jj)
Percent
CO
2
and
O7in
the
stack
gas,
dry basis;
6223
6224
yjji
çQ2
and
02
reference
method
used;
6225
6226
jç)
Moisture
content
of
stack
gas
(percent
H
7
Q)
6227
6228
)
Molecular
weight
of
stack
gas,
dry-basis
(lb/lb-mole);
6229
6230
çj)
Molecular
weight
of
stack
gas, wet-basis
(lb/lb-mole);
6231
6232
jj)
Stack
diameter
(or
equivalent
diameter)
at the test
port
(fi);
6233
6234
jji
Average
square
root
of
velocity
head
of stack
gas (inches
of
6235
jO)fortherun;
6236
6237
çjy)
Stack
or duct
cross-sectional
area at
test port
(fl
2
);
6238
6239
çy)
Average
velocity
(ft/sec);
6240
6241
çyj)
Average
stack
flow rate,
adjusted,
if
applicable,
for
wall
6242
effects
(scfh,
wet-basis);
6243
6244
çyjjJ
Flow
rate reference
method
used;
6245
6246
xviii)
Average
velocity,
adjusted
for
wall
effects;
6247
6248
çj)
Calculated
(site-specific)
wall
effects
adjustment
factor
6249
determined
during
the run,
and,
if
different,
the
wall
effects
6250
adjustment
factor
used in
the
calculations;
and
6251
6252
p)
Default
wall
effects
adjustment
factor
used.
6253
JCAR350225-08 1 8507r01
6254
)
For each traverse point of each run of each RATA using Reference
6255
Method 2 (or its allowable alternatives
in
appendix A
to
40
CFR
6256
60, incorporated by reference in Section 225.140) to determine
6257
volumetric
flow rate, record the following data elements (as
6258
applicable
to the measurement method
used):
6259
6260
j)
Reference method probe type;
6261
6262
Ij
Pressure measurement device
type;
6263
6264
IJj
Traverse point ID;
6265
6266
jy
Probe or pitot tube calibration coefficient;
6267
6268
y)
Date of latest probe or pitot tube calibration;
6269
6270
il
Average velocity differential pressure at traverse point
6271
(inches
of
H
2
0)
or the average of the square roots of the
6272
velocity differential pressures
at
the traverse
point
((inches
6273
of
H,O)”
2
);
6274
6275
yjj
T,
stack temperature at the traverse point (°F);
6276
6277
yjji
Composite (wall
effects) traverse point identifier;
6278
6279
ç)
Number of
points
included in composite traverse point;
6280
6281
Yaw angle of flow at traverse point (degrees);
6282
6283
j)
Pitch angle of flow at traverse point (degrees);
6284
6285
2c1i1
Calculated
velocity
at
traverse
point both accounting and
6286
not accounting for wall effects
(ft/see):
and
6287
6288
jji
Probe identification number.
6289
6290
For each RATA using Method
3A in appendix A to
40
CFR 60,
6291
incorporated by reference in Section 225.140, to determine
CO
2
6292
Q
2
concentration:
6293
6294
j)
Pollutant
or diluent gas being measured;
6295
6296
jjj
Span of reference method analyzer;
JCAR350225-081 8507r01
6297
6298
jj)
Type of reference method system (e.g.,
extractive or
6299
dilution
type);
6300
6301
jy)
Reference method dilution factor (dilution
type systems
6302
only);
6303
6304
y
Reference
gas
concentrations (zero,
mid and high gas
6305
levels)
used for
the 3-point
pre-test
analyzer
calibration
6306
error test
(or,
for dilution type reference method
systems,
6307
for the 3-point pre-test system calibration
error test) and
for
6308
any subsequent
recalibrations;
6309
6310
yj)
Analyzer
responses to the zero-,
mid-
and high-level
6311
calibration
gases during the 3-point pre-test analyzer
(or
6312
system) calibration error test
and during any subsequent
6313
recalibrations;
6314
6315
yjfl
Analyzer
calibration
error at each gas level
(zero,
mid
and
6316
high) for the
3-point
pre-test analyzer
(or
system)
6317
calibration error
test
and for any subsequent
recalibrations
6318
(percent of span value);
6319
6320
yjji
Upscale gas concentration
(mid
or high gas
level)
used
for
6321
each pre-run
or
post-run system bias check or
(for
dilution
6322
type reference method
systems)
for each pre-run or
post-
6323
run
system calibration error check;
6324
6325
j
Analyzer
response
to the calibration
gas for each pre-run
or
6326
post-run system bias
(or
system calibration error) check;
6327
6328
The arithmetic average
of the analyzer responses
to
the
6329
zero-level
gas, for each pair of pre- and
post-run system
6330
bias
(or
system calibration error)
checks;
6331
6332
çj)
The arithmetic average
of the analyzer responses
to the
6333
upscale calibration gas for each pair
of pre- and post-run
6334
system
bias
(or
system calibration error) checks;
6335
6336
li)
The results of each
pre-run and each post-run
system
bias
6337
(or
system calibration
error)
check using the zero-level
gas
6338
(percentage
of span value);
6339
JCAR350225-08
1 8507r01
6340
jji
The results
of each pre-run and
each post-run system
bias
6341
(or
system
calibration
error) check using
the upscale
6342
calibration
gas (percentage of span
value);
6343
6344
Calibration
drift and zero drift of
analyzer during
each
6345
RATA
run (percentage of span
value);
6346
6347
çy)
Moisture
basis
of
the
reference
method analysis:
6348
6349
çyj
Moisture content of
stack gas, in percent,
during each test
6350
run
(if
needed to convert
to moisture basis
of CEMS being
6351
tested);
6352
6353
yjj)
Unadjusted
(raw) average pollutant
or diluent
gas
6354
concentration
for each run:
6355
6356
xviii)
Average
pollutant or diluent
gas concentration
for each
run,
6357
corrected
for calibration
bias
(or
calibration
error)
and, if
6358
applicable,
corrected for
moisture:
6359
6360
The
F-factor used
to convert reference
method
data to
units
6361
of lb/mmBtu
(if
applicable);
6362
6363
ç)
Dates of the
latest analyzer interference
tests;
6364
6365
pçj)
Results
of
the
latest
analyzer
interference
tests:
and
6366
6367
çjj)
For
each calibration gas
cylinder used during
each RATA,
6368
record
the cylinder gas vendor,
cylinder number,
expiration
6369
date,
pollutants in the cylinder
and certified gas
6370
concentrations.
6371
6372
)
For each test run
of each moisture determination
using
Method 4 in
6373
appendix A to 40
CFR 60, incorporated
by reference
in Section
6374
225.140,
(or
its
allowable
alternatives),
whether the determination
6375
is made to
support a gas RATA,
to support a flow RATA
or
to
6376
quality assure
the
data from
a
continuous
moisture
monitoring
6377
system, record
the following data
elements
(as
applicable
to the
6378
moisture
measurement method
used):
6379
6380
Test number;
6381
6382
jj
Run number:
JCAR350225-08
1 8507r01
6383
6384
The beginning
date, hour and minute of the run;
6385
6386
jy
The ending date, hour and minute
of
the
run;
6387
6388
y
Unit operating
level
(low,
mid,
high or normal, as
6389
appropriate);
6390
6391
yj)
Moisture
measurement method;
6392
6393
yjfl
Volume
of 02
H collected in the impingers (ml);
6394
6395
yjji
Mass
of 02
H collected in the silica gel (g);
6396
6397
jç)
Dry gas meter
calibration
factor;
6398
6399
)
Average dry
gas meter temperature
(°F);
6400
6401
çj
Barometric
pressure (inches of
mercury);
6402
6403
jj)
Differential pressure across the orifice
meter
(inches
of
6404
6405
6406
jji
Initial
and final dry gas meter readings
(ft
3
);
6407
6408
çjy)
Total
sample gas volume, corrected to standard
conditions
6409
(dscf);
and
6410
6411
çy)
Percentage
of moisture in the stack gas
(percent
H
2
Q)
6412
6413
The raw data and
calculated results for any stratification tests
6414
performed
in accordance with Sections 6.5.5.1 through
6.5.5.3 of
6415
Exhibit A to this Appendix.
6416
6417
For each RATA run
using the Ontario Hydro Method to determine
6418
mercury concentration:
6419
6420
Percent
CO
2and
O2in
the stack gas, dry-basis;
6421
6422
jj
Moisture content of the stack gas
(percent
H2
Q)j
6423
6424
jjjj.
Average
stack temperature
(°F);
6425
JCAR350225-081 8507r01
6426
jy
Dry
gas volume metered
(dscm):
6427
6428
y)
Percent
isokinetic;
6429
6430
yj
Particle-bound
mercury
collected
by
the filter,
blank and
6431
probe rinse
(igm);
6432
6433
yiIl
Oxidized
mercury collected by the
KC1 impingers
(igm);
6434
6435
yjji
Elemental
mercury collected
in
the IINO
3
LH
2
O
2
impinger
6436
and
in
the
KMnO
4
/H
2
SO
4
impingers
(igm);
6437
6438
jç)
Total
mercury,
including particle-bound
mercury (igm);
6439
and
6440
6441
)
Total mercury,
excluding
particle-bound
mercury
()
6442
6443
All appropriate data
elements
for Methods
30A
and
30B.
6444
6445
For a unit with a flow
monitor installed
on a rectangular stack
or
6446
duct, if a site-specific
default
or measured
wall effects
adjustment
6447
factor (WAF)
is used to correct
the stack
gas volumetric
flow rate
6448
data
to account for
velocity
decay
near
the stack or duct wall,
the
6449
owner
or operator
must keep records
of the following
for each
flow
6450
RATA
performed with EPA
Method 2 in appendices
A—i and A—2
6451
to 40 CFR 60, incorporated
by reference in
Section 225.140,
6452
subsequent to the
WAF determination:
6453
6454
Monitoring
system
ID;
6455
6456
fl
Test
number:
6457
6458
jJj)
Operating
level:
6459
6460
jy
RATA end date and
time:
6461
6462
y
Number of
Method 1
traverse
points;
and
6463
6464
yj)
Wall effects
adjustment factor
(WAF),
to the nearest
6465
0.0001.
6466
JCAR350225-08
1
8507r01
6467
j)
For
each
RATA run
using Method
29 in
appendix
A—8
to
40
CFR
6468
60, incorporated
by reference
in Section
225.140,
to determine
6469
mercury
concentration:
6470
6471
Percent
CQ
2and 2
O
in
the stack
gas,
dry-basis;
6472
6473
jj)
Moisture
content
of the
stack
gas (percent
H
2
Q)
6474
6475
jjj)
Average
stack
gas temperature
(°F);
6476
6477
j
Dry
gas
volume
metered
(dscm);
6478
6479
y
Percent
isokinetic;
6480
6481
yj)
Particulate
mercury
collected
in the front
half of the
6482
sampling
train,
corrected for
the
front-half
blank value
6483
Qigm);
and
6484
6485
yji)
Total
vapor phase
mercury
collected
in
the back half
of
the
6486
sampling
train,
corrected for
the back-half
blank
value
6487
fllgm).
6488
6489
)
For
each certified
continuous
emission
monitoring
system, excepted
6490
monitoring
system or
alternative
monitoring
system,
the date
and
6491
description
of each
event
that requires
certification,
recertification
or
6492
certain diagnostic
testing
of the system
and
the date
and type
of each
test
6493
performed.
If the conditional
data
validation
procedures
of Section
6494
1
.4(b)(3)
of this
Appendix
are to
be used to
validate
and
report data
prior
6495
to the completion
of
the
required
certification,
recertification
or diagnostic
6496
testing,
the
date and
hour
of the probationary
calibration
error
test
must
be
6497
reported
to mark the
beginning
of conditional
data
validation.
6498
6499
2)
Hardcopy
relative
accuracy
test
reports,
certification
reports,
6500
recertification
reports
or
semiannual
or animal
reports
for gas
or flow
rate
6501
CEMS, mercury
CEMS
or sorbent
trap monitoring
systems
are required
or
6502
requested
under
40
CFR
75.60(b)(6)
or 75.63,
incorporated
by reference
in
6503
Section 225.140,
the
reports must
include,
at a
minimum,
the following
6504
elements
as applicable
to
the
types of tests
performed:
6505
6506
l
Summarized
test
results.
6507
6508
)
DAHS
printouts
of the CEMS
data
generated
during the
calibration
6509
error,
linearity,
cycle
time
and
relative accuracy
tests.
JCAR350225-081
8507r01
6510
6511
)
For pollutant
concentration
monitor or diluent
monitor relative
6512
accuracy
tests at normal operating
load:
6513
6514
The raw reference
method
data
from each run, i.e., the
data
6515
under subsection
(a)(7)(D)(xvii)
of this Section (usually
in
6516
the
form of
a
computerized
printout,
showing
a series
of
6517
one-minute
readings
and the
run average);
6518
6519
i1
The
raw
data and results for
all
required
pre-test,
post-test,
6520
pre-run and
post-run
quality
assurance checks
(i.e.,
6521
calibration
gas
injections)
of
the reference method
6522
analyzers,
i.e., the data under subsections
(a)(7)(D)(v)
6523
through (xiv)
of this Section;
6524
6525
jjj)
The raw data
and results for
any moisture measurements
6526
made during
the relative accuracy
testing, i.e.,
the data
6527
under subsections
(a)(7)(E)(i)
through
(xv)
of this
Section;
6528
and
6529
6530
Tabulated,
final, corrected
reference method
run
data
(i.e.,
6531
the actual
values
used
in the relative accuracy
calculations),
6532
along
with the equations
used
to
convert
the raw data to
the
6533
final values and example
calculations
to demonstrate how
6534
the
test data were
reduced.
6535
6536
For
relative accuracy
tests
for flow monitors:
6537
6538
j)
The raw flow rate
reference method
data, from Reference
6539
Method 2
(or
its allowable
alternatives)
under appendix
A
6540
to 40 CFR 60,
incorporated
by
reference
in Section
6541
225.140, including
auxiliary moisture
data
(often
in the
6542
form of handwritten
data
sheets),
i.e.,
the
data under
6543
subsections (a)(7)(B)(i)
through
(xx),
subsections
6544
(a)(7)(C)(i)
through
(xiii),
and, if applicable,
subsections
6545
(a)(7)(E)(i)
through (xv) of this
Section;
and
6546
6547
jI
The tabulated,
final volumetric flow
rate values
used in the
6548
relative
accuracy calculations
(determined
from the flow
6549
rate reference
method data
and other necessary
6550
measurements,
such
as moisture, stack temperature
and
6551
pressure),
along with the
equations used
to convert the raw
JCAR350225-081
8507r01
6552
data to the
final
values
and example
calculations
to
6553
demonstrate
how the test
data
were reduced.
6554
6555
Calibration
gas
certificates
for
the gases
used in the
linearity,
6556
calibration
error
and cycle time
tests
and
for
the calibration
gases
6557
used to
quality
assure the
gas monitor
reference
method
data
6558
during
the relative
accuracy
test audit.
6559
6560
)
Laboratory
calibrations
of the source
sampling
equipment.
For
6561
sorbent trap
monitoring
systems,
the
laboratory
analyses of
all
6562
sorbent
traps and
information
documenting
the results
of
all leak
6563
checks and
other
applicable
quality
control
procedures.
6564
6565
)
A copy of
the
test protocol
used
for
the
CEMS
certifications
or
6566
recertifications,
including
narrative
that
explains
any testing
6567
abnormalities,
problematic
sampling,
and
analytical
conditions
that
6568
required
a change
to the
test protocol,
andlor solutions
to technical
6569
problems
encountered
during
the testing
program.
6570
6571
)
Diagrams
illustrating
test locations
and
sample
point
locations
(to
6572
verify that
locations
are
consistent
with information
in the
6573
monitoring
plan).
Include
a discussion
of any
special
traversing
or
6574
measurement
scheme.
The discussion
must
also
confirm
that
6575
sample
points satisfy
applicable
acceptance
criteria.
6576
6577
Names
of key
personnel
involved
in the
test
program,
including
6578
test team
members,
plant
contacts, agency
representatives
and test
6579
observers
on
site.
6580
6581
IQ)
Whenever
reference
methods
are
used as
backup
monitoring
systems
6582
pursuant to
Section
1.4(d)(3)
of this
Appendix,
the
owner or
operator
must
6583
record the
following
information:
6584
6585
)
For
each test
run
using Reference
Method
2 (or its
allowable
6586
alternatives
in
appendix A
to 40 CFR
60,
incorporated
by
reference
6587
in
Section
225.140)
to
determine
volumetric
flow
rate,
record
the
6588
following
data
elements
(as
applicable
to
the measurement
method
6589
used):
6590
6591
Unit
or
stack identification
number;
6592
6593
iii
Reference
method
system
and component
identification
6594
numbers;
JCAR350225-0818507r01
6595
6596
jjj)
Run
date and hour;
6597
6598
iI
The
data in
subsection
(a)(7)(B)
of this
Section,
except
for
6599
subsections
(a)(7)(B)(i),
(vi), (viii),
(xii) and
(xvii)
through
6600
(xx);
and
6601
6602
y)
The data in
subsection
(a)(7)(C),
except on a run
basis.
6603
6604
)
For each reference
method test run
using Method 6C,
7E or 3A in
6605
appendix
A
to 40
CFR
60,
incorporated
by reference
in Section
6606
225.140,
to determine
,2
SO
N0,
CO2
or
02
concentration:
6607
6608
Unit or stack identification
number;
6609
6610
li)
The reference
method
system
and component identification
6611
numbers;
6612
6613
jjj
Run number;
6614
6615
jy)
Run start
date and hour;
6616
6617
y)
Run
end date and hour;
6618
6619
yj)
The
data in subsections
(a)(7)(D)(ii)
through
(ix)
and (xii)
6620
through (xv);
and
(vii)
Stack gas
density adjustment
factor
6621
(if
applicable).
6622
6623
)
For
each hour of each
reference method
test run using Method
6C,
6624
7E or
3A in appendix
A to 40 CFR 60,
incorporated
by reference
6625
in
Section 225.140, to
determine
2
SO,
N0,
CO
2.or
0
6626
concentration:
6627
6628
j)
Unit or stack
identification number;
6629
6630
jj)
The reference
method
system and
component
identification
6631
numbers;
6632
6633
jjj)
Run
number;
6634
6635
jy)
Run date
and hour;
6636
6637
y)
Pollutant
or diluent
gas being measured;
JCAR350225-081 8507r01
6638
6639
yj
Unadjusted (raw) average pollutant
or
diluent
gas
6640
concentration
for the hour; and
6641
6642
XIi)
Average pollutant
or diluent gas
concentration
for the hour,
6643
adjusted
as appropriate for moisture, calibration
bias (or
6644
calibration
error)
and stack gas density.
6645
6646
II)
For each other quality-assurance test or other quality assurance
activity,
6647
the
owner or operator
must record the following
(as
applicable):
6648
6649
)
Component/system
identification
code;
6650
6651
Parameter;
6652
6653
Test or activity completion date
and hour;
6654
6655
Test or activity
description;
6656
6657
j)
Test result;
6658
6659
Reason for test; and
6660
6661
Test code.
6662
6663
j
For each
request
for a quality assurance
test
extension
or exemption,
for
6664
any loss of exempt status, and for each single-load flow RATA claim
6665
pursuant to Section 2.3.1.3(c)(3)
of Exhibit B to this Appendix, the
owner
6666
or
operator must record the following (as applicable):
6667
6668
For a RATA deadline extension or exemption request:
6669
6670
Monitoring system identification code;
6671
6672
jj)
Date
of last RATA;
6673
6674
jjj
RATA
expiration
date without extension;
6675
6676
i1
RATA
expiration date with extension;
6677
6678
y
Type of RATA extension
of exemption claimed or lost;
6679
JCAR350225-08 1 8507r01
6680
yj
Year
to date hours of usage of fuel other than very
low
6681
sulfur fuel;
6682
6683
yj
Year to date
hours of non-redundant back-up CEMS usage
6684
at the unit/stack;
and
6685
6686
yjji
Quarter
and year.
6687
6688
)
For a linearity test or
flow-to-load ratio test quarterly exemption:
6689
6690
Component-system
identification
code;
6691
6692
jj)
Type of
test:
6693
6694
jj)
Basis for
exemption:
6695
6696
jy
Quarter
and year; and
6697
6698
Span scale.
6699
6700
)
For a fuel flowmeter accuracy test extension:
6701
6702
Component-system identification
code;
6703
6704
jj
Date of last accuracy test;
6705
6706
Iji)
Accuracy
test
expiration
date
without extension;
6707
6708
jy)
Accuracy test expiration
date
with
extension;
6709
6710
y
Type of
extension:
and
6711
6712
yj)
Quarter
and year.
6713
6714
)
For a single-load
(or
single-level) flow RATA claim:
6715
6716
j)
Monitoring
system identification code;
6717
6718
ji)
Ending date of last annual flow RATA;
6719
6720
jjj
The relative frequency (percentage) of unit or stack
6721
operation
at each load
(or operating)
level
(low,
mid
and
JCAR350225-0818507r01
6722
high) since the
previous annual flow RATA, to the nearest
6723
0.1 percent;
6724
6725
jy
End date of the historical
load
(or
operating
level)
data
6726
collection
period; and
6727
6728
y)
Indication
of
the
load
(or
operating) level
(low,
mid or
6729
high) claimed for the single-load
flow RATA.
6730
6731
j
For the sorbent
traps
used in sorbent
trap monitoring systems to quantify
6732
mercury concentration
under Sections 1.14 through 1.18 of this Appendix
6733
(including sorbent traps used for relative
accuracy
testing), the owner or
6734
operator
must keep
records of the following:
6735
6736
The ID number
of the monitoring system in which each sorbent
6737
trap
was
used to collect mercury;
6738
6739
The unique identification number of
each sorbent trap;
6740
6741
)
The beginning and ending
dates and hours of the data collection
6742
period for each sorbent trap;
6743
6744
I)
The average
mercury concentration
(in
igm1dscm) for the
data
6745
collection
period;
6746
6747
)
Information
documenting the results of the required
leak checks;
6748
6749
)
The analysis of the mercury collected
by each sorbent trap; and
6750
6751
Information documenting the results
of the other applicable quality
6752
control procedures
in Section 1.3 of this Appendix and in Exhibits
6753
B and D to this Appendix.
6754
6755
Except as
otherwise provided
in Section
1.12(a)
of this Appendix,
for units with
6756
add-on mercury emission controls,
the owner or operator must keep the following
6757
records on-site in the quality assurance/quality
control plan required by Section
1
6758
of Exhibit B to
this Appendix:
6759
6760
fl
A list of operating parameters
for the add-on emission controls, including
6761
parameters
in Section 1.12 of this Appendix,
appropriate
to the particular
6762
installation
of add-on emission controls; and
6763
JCAR350225-08 1 8507r01
6764
The range of each operating parameter
in the list that indicates the add-on
6765
emission
controls are properly operating.
6766
6767
ç).
Excepted Monitoring for Mercury Low
Mass Emission Units under Section
6768
1.15(b)
of this Appendix. For qualifng coal-fired units using
the
alternative
low
6769
mass emission methodology under Section
1.15(b),
the owner or operator
must
6770
record
the data elements
described
in Section 1.13
(a)(7)(G),
Section 1.1 3(a)(7)(H)
6771
or Section 1.1 3(a)(7)(J) of this Appendix,
as
applicable, for
each run
of each
6772
mercury emission test and re-test required under Section 1.15(c)(1) or Section
6773
1.15(d)(4)(C)
of this
Appendix.
6774
6775
ç
DM15
Verification. For
each
DAHS
(missing data and
formula)
verification that
6776
is required for initial certification, recertification or for certain diagnostic testing
6777
of a
monitoring system, record the date and
hour that the DAHS verification is
6778
successfully completed.
(This
requirement only applies to units that report
6779
monitoring plan data in accordance with Section
1.10(d)
of this
Appendix.)
6780
6781
Section
1.14 General Provisions
6782
6783
Applicability.
The
owner or operator of a unit must comply with the requirements
6784
of
this Appendix
to
the extent
that compliance is required by this Part. For
6785
purposes of this Appendix, the term “affected
unit” means any coal-fired unit
(as
6786
defined in 40 CFR 72.2,
incorporated
by
reference) that is subject to this
Part. The
6787
term “non-affected unit” means any unit that is not subject to such a program,
the
6788
term “permitting authority” means the Agency, and the term “designated
6789
representative” means
the
responsible
party under
this Part.
6790
6791
Compliance
Dates.
The owner or operator of an affected unit must meet the
6792
compliance
deadlines
established
by
Subpart B of this Part.
6793
6794
Prohibitions.
6795
6796
fl
No owner or operator of an affected unit or a non-affected unit under
6797
Section 1.16(b)(2)(B)
of
this Appendix
will
use
any alternative monitoring
6798
system,
alternative reference method or any other alternative for the
6799
required
continuous
emission monitoring system without having obtained
6800
prior written approval in accordance with subsection
(f)
of this
Section.
6801
6802
)
No owner or operator of an affected unit or a non-affected unit under
6803
Section 1.16(b)(2)(B)
of this Appendix will operate the unit so as to
6804
discharge, or allow to be discharged, emissions
of mercury to the
6805
atmosphere without accounting for all such emissions in accordance
with
6806
the applicable provisions of this Appendix.
JCAR350225-081
8507r01
6807
6808
)
No
owner
or operator of an affected unit
or a non-affected unit under
6809
Section 1.16(b)(2)(B)
of this Appendix will disrupt
the continuous
6810
emission monitoring system,
any
portion of the system, or any other
6811
approved
emission monitoring method,
and thereby
avoid
monitoring and
6812
recording
mercury mass emissions discharged
into the atmosphere, except
6813
for periods
of
recertification
or periods when calibration,
quality assurance
6814
testing or maintenance is performed
in accordance with the provisions
of
6815
this
Appendix applicable to monitoring
systems under Section 1.15 of this
6816
Appendix.
6817
6818
4
No owner or operator
of an affected unit or a non-affected unit
under
6819
Section 1.1
6(b)(2)(B)
will retire or permanently
discontinue use of the
6820
continuous emission monitoring
system, any component of the system,
or
6821
any other approved
emission monitoring system under
this Appendix,
6822
except under any one of the following
circumstances:
6823
6824
During the period
that the unit is covered by a retired unit
6825
exemption
that
is in effect under
this Part; or
6826
6827
)
The owner
or operator is monitoring mercury mass emissions
from
6828
the affected unit with another
certified monitoring system
6829
approved, in accordance with
the provisions of Section 250 of
this
6830
Part; or
6831
6832
)
The designated representative
submits notification of the date
of
6833
certification testing of a replacement
monitoring
system in
6834
accordance with
Section
240(d)
of this Part.
6835
6836
)
Quality Assurance and Quality Control
Requirements. For units that use
6837
continuous emission monitoring systems to account for
mercury mass emissions,
6838
the owner or operator must meet the
applicable quality assurance and quality
6839
control requirements in
Section 1.5 and Exhibit B to this Appendix
for the flow
6840
monitoring systems, mercury concentration
monitoring systems, moisture
6841
monitoring systems
and diluent monitors
required
under
Section
1.15 of this
6842
Appendix. Units using sorbent trap
monitoring systems must meet the
applicable
6843
quality assurance requirements in Section 1.3
of this Appendix, Exhibit D to
this
6844
Appendix, and Sections
1.3 and 2.3 of Exhibit B to this
Appendix.
6845
6846
Reporting Data Prior to Initial
Certification. If, by the
applicable
compliance
date
6847
under this Part, the owner or
operator
of
an affected unit has not successfully
6848
completed
all
required certification tests for
any monitoring systems, he or she
6849
must
determine, record,
and report data prior to initial certification
in accordance
JCAR350225-081 8507r01
6850
with Section 239 of this Part.
6851
6852
fi
Petitions.
6853
6854
jJ
The
designated
representative
of an affected unit that is also subject
to the
6855
Acid Rain Program may
submit a petition to the Agency requesting an
6856
alternative to any requirement
of Sections 1.14 through 1.18 of this
6857
Appendix. Such a petition must meet the requirements
of
40
CFR 75.66,
6858
incorporated
by
reference
in Section 225.140, and any additional
6859
requirements established
by
Subpart B of this Part. Use of an alternative to
6860
any requirement
of
Sections
1.14 through 1.18 of this Appendix is in
6861
accordance with Sections 1.14 through
1.18 of this Appendix and with
6862
Subpart B
of this
Part
only
to the extent that the petition is approved
in
6863
writing by the Agency.
6864
6865
Notwithstanding subsection
(f)(1)
of this Section, petitions
requesting an
6866
alternative to
a
requirement
concerning any additional CEMS required
6867
solely to meet the common stack provisions of Section
1.16 of this
6868
Appendix must
be submitted to the Agency and will be governed
by
6869
subsection (f)(3) of this
Section. Such a petition must meet the
6870
requirements of 40 CFR 75.66, incorporated
by reference in Section
6871
225.140, and any additional requirements established
by Subpart B of this
6872
Part.
6873
6874
)
The designated representative
of an affected unit that is not
subject
to
the
6875
Acid Rain Program may submit a petition to the Agency
requesting an
6876
alternative
to any requirement of Sections 1.14 through 1.18 of this
6877
Appendix. Such a petition must
meet
the requirements
of 40 CFR 75.66,
6878
incorporated
by reference in Section 225.140, and any additional
6879
requirements established
by Subpart
B of this
Part.
Use of an alternative
to
6880
any
requirement
of Sections 1.14 through 1.18 of this Appendix is in
6881
accordance with Sections 1.14 through 1.18 of this Appendix
only to the
6882
extent that it is approved
in writing by the Agency.
6883
6884
Section
1.15
Monitoring of Mercury
Mass Emissions and Heat
Input
at the Unit Level
6885
6886
The owner or
operator of the
affected
coal-fired unit must:
6887
6888
Meet
the general operating requirements
in Section
1.2
of this Appendix for the
6889
following continuous emission monitors (except
as
provided
in accordance with
6890
subpart E of 40 CFR 75, incorporated
by
reference in Section 225.140):
6891
6892
j)
A mercury concentration
monitoring
system
(consisting
of a mercury
JCAR350225-08
1 8507r01
6893
pollutant concentration
monitor
and an automated DAHS,
which provides
6894
a permanent,
continuous record of
mercury emissions
in units of
6895
micrograms
per standard cubic
meter
(jig/scm))
or
a sorbent trap
6896
monitoring
system to measure
the mass concentration
of total vapor phase
6897
mercury
in the flue gas, including
the elemental
and oxidized forms
of
6898
mercury,
in micrograms per
standard cubic meter
(pg/scm);
6899
6900
)
A flow
monitoring system;
6901
6902
A continuous
moisture
monitoring system
(if
correction of mercury
6903
concentration for moisture
is required),
as
described
in
40
CFR
75.11(b),
6904
incorporated
by
reference
in Section
225.140.
Alternatively,
the owner
or
6905
operator may use the
appropriate fuel-specific
default moisture
value
6906
provided
in 40 CFR 75.11,
incorporated
by reference in Section
225.140,
6907
or a site-specific moisture
value approved
by petition under 40
CFR 75.66,
6908
incorporated
by reference
in Section 225.140;
and
6909
6910
4)
If heat
input is
required
to be reported
under
this Part, the owner
or
6911
operator must meet the
general operating requirements
for
a
flow
6912
monitoring
system
and an
02
or
CO2
monitoring
system
to measure
heat
6913
input rate.
6914
6915
j)
For an affected unit
that
emits 464 ounces
(29 lb) of
mercury
per
year or less,
use
6916
the following excepted
monitoring methodology.
To implement
this methodology
6917
for a qualifying
unit,
the
owner
or
operator must meet
the general operating
6918
requirements in
Section
1.2 of this
Appendix
for the
continuous emission
6919
monitors described
in subsections
(a)(2)
and (a)(4) of this
Section,
and
perform
6920
mercury
emission
testing
for
initial certification and
on-going quality-assurance,
6921
as described
in subsections (c) through
(e) of this Section.
6922
6923
c)
To determine
whether an affected
unit is eligible to use
the monitoring provisions
6924
in
subsections
(b)
of this Section:
6925
6926
1)
The owner
or operator must
perform mercury
emission testing within
18
6927
months
before the compliance
date in Section 1.14(b)
of this
Appendix to
6928
determine
the mercury
concentration
(i.e.,
total vapor phase mercury)
in
6929
the
effluent.
6930
6931
)
The testing
must
be performed
using one of the mercury
reference
6932
methods listed
in Section
1.6(a)(5)
of this Appendix,
and must
6933
consist of
a minimum
of 3 runs at the normal
unit operating load,
6934
while
combusting
coal. The
coal combusted during
the testing
6935
must
be representative
of the coal that will be
combusted
at the
JCAR350225-081 8507r01
6936
start
of the mercury
mass emissions
reduction program
(preferably
6937
from the same sources
of supply).
6938
6939
)
The minimum
time per run must be
1
hour if
Method 30A is used.
6940
If either Method 29
in appendix A-8 to 40 CFR
60,
incorporated
6941
by reference, ASTM D6784-02
(the
Ontario
Hydro
method)
6942
(incorporated
by reference under
Section
225.140)
or Method
30B
6943
is used, paired
samples are required for each test run
and the runs
6944
must be long enough
to ensure that sufficient mercury is collected
6945
to analyze.
When Method 29 in
appendix A-8 to 40 CFR 60,
6946
incorporated
by
reference,
or the Ontario Hydro method is
used,
6947
the test
results
must be based on the vapor
phase mercury collected
6948
in the back-half
of
the
sampling trains (i.e., the non-filterable
6949
impinger
catches).
For each Method 29 in appendix
A-8 to 40 CFR
6950
60, incorporated
by
reference,
Method 30B or Ontario Hydro
6951
method test
run, the paired trains must meet the relative
deviation
6952
(RD)
requirement specified
in Section
1.6(a)(5)
of this Appendix
6953
or Method
30B, as applicable. If the RD specification
is met, the
6954
results of the two
samples must be averaged arithmetically.
6955
6956
)
If
the
unit is equipped with flue gas desulfurization
or add-on
6957
mercury
emission controls, the controls must be operating
6958
normally
during the testing, and, for the purpose of establishing
6959
proper operation
of the controls, the owner or operator must record
6960
parametric data or
7
SO
concentration
data in accordance with
6961
Section
1.12(a)
of this Appendix.
6962
6963
If two or more of units of the same type qualify
as a group of
6964
identical units in
accordance with 40 CFR 75.19(c)(1)(iv)(B),
6965
incorporated by reference in Section 225.140, the owner
or
6966
operator may test
a subset of these units in lieu of testing each
unit
6967
individually.
If this option is selected, the number of
units required
6968
to be tested must
be
determined
from Table LM-4 in 40 CFR
6969
75.19,
incorporated by reference in Section 225.140.
For the
6970
purposes of the required
retests under subsection (d)(4) of this
6971
Section, it is strongly recommended that
(to
the
extent
practicable)
6972
the same subset
of the units not be tested in two successive
retests,
6973
and that every
effort be made to ensure that each unit in the group
6974
of identical units is tested in
a
timely
manner.
6975
6976
6977
6978
Based on the results
of the
emission
testing, Equation 1 of this
1CAR350225-08
1
8507r01
6979
Section must be used
to provide a conservative estimate of the
6980
annual
mercury mass emissions from
the unit:
6981
6982
E=NXKXCHgXQmax
(Equation
1)
6983
6984
Where:
6985
B
= Estimated annual mercury
mass emissions from the
affected unit,
(ounces/year)
K
= Units conversion constant,
9.978 x
100
oz-scm/Iig
scf
N
= Either 8,760
(the
number
of hours in a year) or the
maximum
number of operating hours per year
(if
less
than 8,760) allowed by the unit’s Federally-
enforceable operating
permit.
The highest mercury concentration (
1
ug/scm)
from
any
of
the test
runs or 0.50 ,ug/scm, whichever
is
greater
Maximum potential flow rate, determined according
—
to Section 2.1.2.1
of Exhibit A to this Appendix,
(scfh)
6986
6987
Equation
1 of this Section assumes that the unit operates
at its
6988
maximum
potential flow rate, either year-round or for the
6989
maximum number
of hours
allowed
by the operating permit (if
unit
6990
operation
is restricted to less than
8,760 hours per
year).
If the
6991
permit restricts
the annual unit heat input but not the number
of
6992
annual unit operating hours, the owner
or operator may divide the
6993
allowable annual
heat input
(mmBtu)
by the design rated heat
input
6994
capacity
of the unit (mmBtu/hr) to determine
the value of “N” in
6995
Equation 1. Also, note
that if the highest mercury concentration
6996
measured
in any test run is less than 0.50 ftg/scm, a default
value
6997
of 0.50 pg/scm must be
used
in
the calculations.
6998
6999
If the estimated annual
mercury mass emissions from subsection (c)(2)
of
7000
this Section
are
464 ounces per year or less,
then the unit is eligible to
use
7001
the monitoring provisions
in subsection
(b)
of this Section, and
continuous
7002
monitoring of the mercury
concentration
is not required
(except
as
7003
otherwise provided in subsections
(e)
and
(f)
of this Section).
7004
7005
If the
owner
or
operator
of an eligible unit under subsection
(c)(3)
of this Section
7006
elects
not to continuously monitor
mercury concentration, then the following
7007
requirements must be met:
JCAR350225-081
8507r01
7008
7009
j)
The results
of the mercury emission
testing
performed under subsection
7010
(c) of this
Section must be submitted as
a
certification
application to the
7011
permitting authority,
no later than 45
days
after the testing
is completed.
7012
The calculations demonstrating
that the unit emits 464 ounces (or less)
per
7013
year
of mercury must also be provided,
and the default mercury
7014
concentration
that will be used for reporting
under
Section
1.18 of this
7015
Appendix must be specified
in both the electronic and hard copy
portions
7016
of the monitoring plan for the unit.
The methodology is considered to
be
7017
provisionally
certified as of the date and hour
of
completion
of the
7018
mercury emission testing.
7019
7020
Following initial certification, the
same default mercury concentration
7021
value
that was used
to estimate the unit’s annual mercury mass
emissions
7022
under
subsection (c) of this Section must
be reported for each unit
7023
operating hour, except as
otherwise provided in subsection (d)(4)(D)
or
7024
(d)(6)
of this Section. The default mercury concentration
value must
be
7025
updated
as appropriate
according to subsection
(d)(5)
of this Section.
7026
7027
)
The hourly
mercury mass emissions must be calculated according
to
7028
Section 4.1.3 in Exhibit
C
to this Appendix.
7029
7030
4)
The mercury emission testing
described in subsection
(c)
of this Section
7031
must be repeated periodically, for the
purposes of quality-assurance,
as
7032
follows:
7033
7034
If the results of the certification
testing under subsection
(c)
of this
7035
Section show
that the unit emits 144 ounces
(9
lb)
of mercury
per
7036
year or less, the first retest
is required by the end of the fourth
QA
7037
operating
quarter
(as
defined in 40 CFR 72.2, incorporated
by
7038
reference) following the calendar
quarter
of the certification
7039
testing; or
7040
7041
)
If the results
of the certification testing under subsection
(c)
of this
7042
Section show that the unit emits
more than 144 ounces of mercury
7043
per year,
but less than or equal to 464 ounces per year,
the first
7044
retest is required
by the end of the second
QA
operating
quarter
(as
7045
defined in 40 CFR 72.2, incorporated
by reference) following
the
7046
calendar
quarter
of the certification testing;
and
7047
7048
)
Thereafter, retesting
must
be
required
either semiannually
or
7049
annually
(i.e.,
by
the
end of the second or fourth
QA
operating
7050
quarter following the quarter
of the
previous
test),
depending
on
JCAR350225-08
1 8507r01
7051
the
results
of the
previous
test.
To
determine
whether
the next
7052
retest
is due
within two
or four
QA
operating
quarters,
substitute
7053
the
highest mercury
concentration
from the
current
test or
0.50
7054
jig/scm
(whichever
is greater)
into
the
equation
in subsection
(c)(2)
7055
of this Section.
If
the
estimated
annual
mercury
mass
emissions
7056
exceeds
144
ounces,
the next
test is due
within
two
QA
operating
7057
quarters.
If the
estimated
annual
mercury
mass
emissions
is 144
7058
ounces
or less,
the
next test is
due within
four
OA
operating
7059
quarters.
7060
7061
An additional
retest
is required
when there
is a
change
in the
coal
7062
rank
of the primary
fuel
(e.g.,
when
the
primary
fuel
is switched
7063
from bituminous
coal to
lignite).
Use ASTM
D388-99
7064
(incorporated
by
reference
under
Section
225.140) to
determine
the
7065
coal
rank.
The four
principal
coal ranks
are
anthracitic,
bituminous,
7066
subbituminous
and
lignitic. The
ranks of
anthracite
coal refuse
7067
(cuim)
and
bituminous
coal refuse
(gob)
must
be anthracitic
and
7068
bituminous,
respectively.
The
retest must
be performed
within
720
7069
unit operating
hours
of the change.
7070
7071
)
The
default mercury
concentration
used for reporting
under
Section
1.18
7072
of this Appendix
must
be
updated
after
each
required retest.
This
includes
7073
retests that
are required
prior
to
the compliance
date in Section
1.14(b) of
7074
this Appendix.
The
updated
value
must
either be
the highest
mercury
7075
concentration
measured
in any
of the
test runs or
0.50
jig/scm, whichever
7076
is greater.
The
updated
value
must be applied
beginning
with
the first
unit
7077
operating
hour
in which mercury
emissions
data
are
required
to be
7078
reported
after
completion
of
the retest,
except
as
provided
in
subsection
7079
(d)(4)(D)
of this
Section, where
the need
to retest
is
triggered
by a change
7080
in
the
coal
rank
of the
primary
fuel. In that
case,
apply
the updated
default
7081
mercury
concentration
beginning
with
the first unit
operating
hour
in
7082
which
mercury
emissions
are
required
to
be reported
after the
date
and
7083
hour
of the fuel
switch.
7084
7085
If the
unit is equipped
with
a flue gas
desulfurization
system or
add-on
7086
mercury
controls,
the
owner
or operator
must
record
the information
7087
required
under
Section 1.12
of this Appendix
for
each unit
operating hour,
7088
to
document proper
operation
of the
emission
controls.
7089
7090
For
units with
common
stack
and
multiple
stack exhaust
configurations,
the
use
of
7091
the
monitoring
methodology
described
in
subsections
(b)
through
(d)
of this
7092
Section
is restricted
as follows:
7093
JCAR350225-08 1 8507r01
7094
jJ
The methodology may not
be used for reporting mercury mass emissions
7095
at a
common stack unless all of the units using the common
stack are
7096
affected
units
and
the
units’ combined potential to emit does not exceed
7097
464
ounces of mercury per year
times
the number of units sharing the
7098
stack, in accordance with subsections (c) and
(d)
of this Section. If the test
7099
results
demonstrate that the units sharing the common stack
qualify as low
7100
mass emitters, the default
mercury concentration used for reporting
7101
mercury mass emissions at the common
stack must either be the highest
7102
value obtained in any test run or 0.50 hg/scm, whichever
is greater.
7103
7104
)
The initial emission testing required under subsection
(c)
of this
7105
Section maybe performed
at the common stack if the following
7106
conditions are met. Otherwise, testing of the individual
units (or a
7107
subset of the units, if identical,
as described in subsection (c)(l)(D)
7108
of this
Section)
is required:
7109
7110
j)
The testing must be done at a combined load corresponding
7111
to the designated
normal load level
(low,
mid or
high)
for
7112
the units sharing the common stack in accordance
with
7113
Section
6.5.2.1
of Exhibit Ato this Appendix;
7114
7115
jj
All of the units that
share the stack must be operating in
a
7116
normal, stable manner and
at
typical load levels
during
the
7117
emission testing. The coal combusted in each
unit during
7118
the testing
must be representative of the coal that will
be
7119
combusted in that unit
at the start of the mercury mass
7120
emission reduction program (preferably from
the
same
7121
sources
of supply);
7122
7123
jjj
If flue gas
desulfurization andlor add-on mercury emission
7124
controls are used to reduce the level of the emissions
7125
exiting from the
common stack, these emission controls
7126
must be operating normally during the emission
testing
7127
and, for the purpose
of establishing proper operation
of the
7128
controls, the owner or
operator
must record parametric
data
7129
or
SO
2
concentration
data
in accordance with Section
7130
1.12(a) of this Appendix;
7131
7132
jy
When
calculating E, the estimated maximum
potential
7133
annual mercury
mass emissions
from the stack, substitute
7134
the maximum potential
flow rate through the common
stack
7135
(as
defined in the monitoring plan)
and the highest
7136
concentration
from any test run
(or
0.50
pig/scm,
if greater)
JCAR350225-081
8507r01
7137
into Equation
1;
7138
7139
y)
The calculated
value
of E
must
be
divided
by the number
of
7140
units
sharing the stack.
If the result, when
rounded
to the
7141
nearest
ounce, does
not exceed 464 ounces,
the
units
7142
qualify
to use the
low
mass
emission
methodology;
and
7143
7144
yj
If the units qualify
to use the methodology,
the
default
7145
mercury
concentration
used for reporting
at the common
7146
stack must be the
highest value
obtained in any test
run or
7147
0.50 pg/scm,
whichever
is greater;
or
7148
7149
The retests
required
under
subsection
(d)(4)
of this Section may
7150
also
be done at the common
stack. If this testing
option
is
chosen,
7151
the testing
must
be
done
at a combined
load corresponding to
the
7152
designated
normal load
level
(low,
mid or
high)
for the
units
7153
sharing
the common stack,
in accordance
with Section 6.5.2.1
of
7154
Exhibit
A to this Appendix.
Provided
that the
required
load
level is
7155
attained
and that
all
of the units sharing
the stack are fed from
the
7156
same
on-site coal supply
during normal
operation, it is not
7157
necessary for all of
the units sharing the
stack
to be in
operation
7158
during
a retest.
However, if two or more
of the units that
share the
7159
stack are fed
from
different on-site
coal supplies (e.g.,
one
unit
7160
bums low-sulfur
coal for compliance
and the other
combusts
7161
higher-sulfur
coal),
then either:
7162
7163
Perform
the
retest
with all units in normal
operation;
or
7164
7165
jj
If
this is not
possible,
due to circumstances
beyond
the
7166
control of the owner
or operator (e.g.,
a forced unit outage),
7167
perform
the retest
with the available
units operating and
7168
assess the test results
as follows. Use the
mercury
7169
concentration
obtained
in
the retest for
reporting purposes
7170
under this Part if the
concentration is greater
than or equal
7171
to
the value
obtained
in
the
most recent
test. If the retested
7172
value is lower than
the mercury concentration
from the
7173
previous
test, continue
using the higher
value from
the
7174
previous test for reporting
purposes
and use that same
7175
higher mercury
concentration value
in Equation 1
to
7176
determine
the due date for the next
retest,
as described
in
7177
subsection
(e)(1)(C)
of this Section.
7178
7179
If testing is done
at the
common
stack, the due date
for
the next
JCAR350225-08
1 8507r01
7180
scheduled retest must be determined
as
follows:
7181
7182
Substitute the
maximum potential flow rate for the common
7183
stack
(as defined in the monitoring plan)
and the highest
7184
mercury
concentration from any test run (or 0.50
,ug/scm, if
7185
greater) into
Equation 1 and
7186
7187
jj)
If the value of E obtained from Equation
1, rounded to the
7188
nearest
ounce,
is greater than 144 times the number
of units
7189
sharing the common stack,
but less than or equal to 464
7190
times the
number of units sharing the stack, the next
retest
7191
is due in two
QA
operating quarters
or
7192
7193
jjj)
If the value of E obtained from Equation
1,
rounded
to the
7194
nearest ounce, is
less than or equal to
144
times the number
7195
of
units sharing the common stack, the next retest
is due in
7196
four
QA
operating
quarters.
7197
7198
)
For units with multiple
stack or duct configurations, mercury emission
7199
testing must be performed separately
on each stack or duct, and the
sum of
7200
the estimated annual mercury mass emissions from
the
stacks or ducts
7201
must not exceed 464
ounces of mercury per year. For reporting
purposes,
7202
the default mercury
concentration used for each stack or duct must
either
7203
be the highest value obtained
in any test run for that stack or 0.50
jig/scm,
7204
whichever
is greater.
7205
7206
For units with a main
stack and bypass stack configuration, mercury
7207
emission
testing
must be performed only
on the main stack. For reporting
7208
purposes, the default mercury
concentration used for the main stack
must
7209
either be
the
highest value obtained in any
test run for that stack or 0.50
7210
jig/scm,
whichever is greater.
Whenever the main stack is bypassed,
the
7211
maximum potential
mercury concentration,
as defined in Section
2.1.3
of
7212
Exhibit A to this Appendix, must
be reported.
7213
7214
At the end of each calendar year,
if the cumulative annual mercury mass
7215
emissions from
an
affected unit have exceeded 464
ounces, then the owner must
7216
install, certify, operate and
maintain a mercury concentration monitoring
system
7217
or a sorbent trap monitoring system
no later than 180
days
after the end of
the
7218
calendar year in which the annual mercury
mass emissions exceeded 464
ounces.
7219
For common
stack
and multiple stack configurations,
installation
and certification
7220
of
a mercury concentration
or sorbent trap monitoring system on each
stack
7221
(except
for
bypass
stacks)
is likewise
required within 180 days after the
end of the
7222
calendar year, if:
JCAR350225-081 8507r01
7223
7224
jJ
The
annual mercury mass emissions at the common stack have
exceeded
7225
464
ounces times
the number of affected units using the common stack;
or
7226
7227
The
sum of the annual mercury
mass
emissions from
all of the multiple
7228
stacks or
ducts has exceeded 464 ounces; or
7229
7230
)
The sum of the annual
mercury mass
emissions
from the main and bypass
7231
stacks has exceeded 464 ounces.
7232
7233
g
For an affected unit that is using a mercury concentration
CEMS
or
a sorbent trap
7234
system under Section 1.15(a)
of this Appendix to continuously monitor the
7235
mercury mass emissions, the owner or operator may switch to the
methodology in
7236
Section
1.15(b)
of this Appendix,
provided that the applicable conditions in
7237
subsections
(c)
through
(f)
of this Section are met.
7238
7239
Section 1.16
Monitorin2
of
Mercury
Mass Emissions and Heat Input at Common and
7240
Multiple Stacks
7241
7242
Unit
Utilizing
Common Stack with Other Affected Units. When an affected
unit
7243
utilizes a common stack with
one or more affected units, but no non-affected
7244
units, the owner or operator must
either:
7245
7246
1)
Install, certify, operate and maintain the monitoring
systems described in
7247
Section 1.15(a)
of this Appendix at the common stack record the
7248
combined mercury mass emissions
for the units exhausting to the common
7249
stack. Alternatively, if, in accordance with Section 1.15(e)
of this
7250
Appendix,
each of
the units using the common stack is demonstrated
to
7251
emit less than
464
ounces of mercury per year, the owner
or operator may
7252
install, certify, operate
and maintain the monitoring systems and perform
7253
the mercury emission testing described under Section
1.15(b)
of this
7254
Appendix. If reporting
of
the
unit
heat input rate is required, determine
the
7255
hourly
unit
heat input rates either by:
7256
7257
Apportioning
the common stack heat input rate
to the
individual
7258
units according
to the procedures in 40 CFR
75.16(e)(3),
7259
incorporated by reference in
Section
225.140;
or
7260
7261
Installing,
certifying, operating
and maintaining
a
flow
monitoring
7262
system
and diluent
monitor in the duct to the common stack
from
7263
each unit; or
7264
7265
Install,
certify,
operate and maintain the monitoring systems
and
(if
JCAR350225-081
8507r01
7266
applicable) perform the
mercury
emission
testing
described
in Section
7267
1.15(a)
or
Section
1.15(b) of this Appendix
in the duct
to
the
common
7268
stack from each unit.
7269
7270
J2)
Unit Utilizing Common
Stack
with Nonaffected Units.
When
one
or
more
7271
affected
units
utilizes a common
stack with one or more
nonaffected
units,
the
7272
owner or operator
must either:
7273
7274
D
Install, certify,
operate and maintain
the monitoring
systems and
(if
7275
applicable) perform
the mercury emission
testing
described in Section
7276
1.15(a)
or
Section
1.15(b)
of
this
Appendix in the duct
to
the
common
7277
stack from each
affected unit; or
7278
7279
Install,
certify,
operate and
maintain the monitoring
systems described
in
7280
Section
1.15(a)
of this Appendix
in the common
stack; and
7281
7282
Install,
certify,
operate
and maintain the
monitoring systems
and
(if
7283
applicable)
perform the
mercury emission
testing described in
7284
Section
1.15(a)
or
(b)
of this Appendix in the
duct to the
common
7285
stack
from each non-affected
unit. The
designated representative
7286
must submit
a petition to the Agency
to
allow
a method of
7287
calculating and
reporting
the
mercury mass emissions
from the
7288
affected units as
the difference
between mercury mass
emissions
7289
measured
in the
common stack and
mercury mass
emissions
7290
measured in the ducts
of the non-affected
units, not to
be
reported
7291
as
an hourly value less
than
zero. The
Agency may approve
such
a
7292
method
whenever
the designated representative
demonstrates,
to
7293
the
satisfaction of the
Agency, that
the method ensures that
the
7294
mercury
mass emissions
from the affected
units
are not
7295
underestimated;
or
7296
7297
Count
the
combined emissions
measured
at the common
stack
as
7298
the mercury mass
emissions for the affected
units,
for
7299
recordkeeping
and
compliance purposes,
in accordance with
7300
subsection
(a)
of this
Section; or
7301
7302
Submit
a
petition
to the Agency to allow
use of a method for
7303
apportioning
mercury
mass emissions measured
in the
common
7304
stack
to each of the units using
the common
stack
and for reporting
7305
the mercury
mass emissions.
The Agency may
approve such a
7306
method
whenever
the designated
representative
demonstrates, to
7307
the satisfaction
of the Agency,
that
the method ensures
that the
7308
mercury mass
emissions from the affected
units
are not
JCAR350225-081
8507r01
7309
underestimated.
7310
7311
If the monitoring
option in
subsection
(b)(2)
of this Section is selected,
7312
and
if heat input
is required
to be reported under
this
Part, the
owner or
7313
operator
must
either:
7314
7315
Apportion the
common
stack
heat input rate to the
individual units
7316
according
to the procedures in
40 CFR 75.16(e)(3),
incorporated
7317
by reference
in Section 225.140;
or
7318
7319
Install a
flow monitoring system
and a diluent gas
(02
or
C0
7320
monitoring
system in the
duct
leading from
each affected unit
to
7321
the common
stack, and measure
the heat input rate
in each duct,
7322
according
to Section 2.2 of Exhibit
C
to this
Appendix.
7323
7324
ç
Unit With
a Main
Stack
and a Bypass Stack. Whenever
any portion
of the flue
7325
gases from
an affected unit can
be
routed
through
a bypass stack
to avoid the
7326
mercury monitoring
systems
installed on the main
stack, the
owner and operator
7327
must either:
7328
7329
jj
Install,
certify,
operate and maintain
the monitoring
systems described
in
7330
Section 1.15(a)
of this Appendix
on both the main
stack and the
bypass
7331
stack and calculate
mercury
mass emissions for
the unit
as
the
sum of the
7332
mercury
mass emissions
measured at the two
stacks;
7333
7334
Install,
certify,
operate
and maintain the monitoring
systems
described
in
7335
Section
1.15(a)
of this
Appendix at the
main stack and measure
mercury
7336
mass
emissions at the
bypass stack using the
appropriate
reference
7337
methods
in Section
1.6(b)
of this Appendix.
Calculate mercury
mass
7338
emissions
for the unit
as the sum of the emissions
recorded
by the installed
7339
monitoring
systems on
the main stack
and the emissions measured
by
the
7340
reference
method
monitoring
systems:
7341
7342
Install, certify,
operate
and maintain the monitoring
systems
and
(if
7343
applicable)
perform the mercury
emission
testing
described
in Section
7344
1.15(a)
or
(b)
of this
Appendix only on
the main stack. If
this option is
7345
chosen,
it is not necessary
to designate
the
exhaust configuration
as a
7346
multiple stack configuration
in
the
monitoring plan required
under
Section
7347
1.10 of
this
Appendix,
since only
the main stack is
monitored; or
7348
7349
4)
If the monitoring
option
in subsection
(c)(1) or (2)
of this Section
is
7350
selected, and
if heat input
is required to be reported
under
this
Part, the
7351
owner or
operator
must:
JCAR350225-08
1 8507r01
7352
7353
Use the
installed flow
and
diluent
monitors to
determine
the hourly
7354
heat input
rate at
each
stack (mmBtu/hr),
according
to
Section
2.2
7355
of Exhibit
C
to this
Appendix;
and
7356
7357
)
Calculate
the
hourly
heat input
at each
stack
(in mmBtu)
by
7358
multiplying
the
measured
stack
heat input
rate
by
the
7359
corresponding
stack operating
time;
and
7360
7361
Determine
the
hourly unit
heat input
by
summing
the
hourly
stack
7362
heat
input
values.
7363
7364
cD
Unit
With
Multiple
Stack or
Duct
Configuration.
When
the flue
gases
from
an
7365
affected
unit
discharge
to
the
atmosphere
through more
than
one stack,
or when
7366
the
flue
gases from
an affected
unit
utilize
two or more
ducts
feeding
into
a
single
7367
stack
and
the owner
or operator
chooses
to monitor
in the
ducts rather
than
in
the
7368
stack,
the owner
or operator
must
either:
7369
7370
1)
Install,
certify,
operate
and
maintain the
monitoring
systems
and
(if
7371
applicable)
perform
the mercury
emission
testing described
in
7372
Section
1.15(a)
or
(b)
of
this Appendix
in
each of
the multiple
7373
stacks and
determine
mercury mass
emissions from
the affected
7374
unit
as the
sum of
the
mercury
mass
emissions
recorded
for each
7375
stack.
If another
unit
also
exhausts
flue gases
into one
of the
7376
monitored
stacks,
the
owner or
operator
must
comply
with the
7377
applicable
requirements
of
subsections
(a)
and
(b)
of this
Section,
7378
in order
to
properly
determine
the mercury
mass
emissions
from
7379
the
units
using
that
stack;
7380
7381
)
Install,
certify, operate
and
maintain the
monitoring
systems
and (if
7382
applicable)
perform
the
mercury
emission
testing described
in
7383
Section
1.15(a) or
(b) of this
Appendix
in
each
of the
ducts
that
7384
feed
into the stack,
and determine
mercury
mass emissions
from
7385
the affected
unit
using
the sum
of the
mercury
mass emissions
7386
measured
at each
duct,
except
that where
another unit
also
7387
exhausts
flue
gases
to one or
more of the
stacks,
the owner
or
7388
operator
must
also comply
with
the
applicable
requirements
of
7389
subsections
(a)
and
(b)
of this
Section
to
determine
and record
7390
mercury mass
emissions
from
the units
using that
stack;
or
7391
7392
If the monitoring
option
in subsection
(d)(1)
or
(2) of this
Section
7393
is selected,
and if
heat
input is
required to
be
reported under
this
7394
Part, the
owner
or
operator
must:
JCAR350225-08 1 8507r01
7395
7396
M
Use the installed
flow and
diluent monitors
to determine
7397
the
hourly heat input rate at each stack or duct (mmBtu/hr),
7398
according to
Section 2.2 of Exhibit C to this Appendix;
and
7399
7400
])
Calculate the hourly heat input at each stack or
duct (in
7401
mmBtu)
by multiplying the measured stack
(or
duct)
heat
7402
input rate
by
the
corresponding stack (or duct) operating
7403
time;
and
7404
7405
c)
Determine the hourly unit heat input
by
summing
the
7406
hourly stack
(or
duct) heat input values.
7407
7408
Section 1.17
Calculation of mercury mass emissions
and heat input rate
7409
7410
The
owner or operator must calculate mercury
mass emissions and heat input rate in accordance
7411
with the procedures in Sections
4.1
through
4.3
of Exhibit F to this Appendix.
7412
7413
Section 1.18 Recordkeepiug and reporting
7414
7415
General recordkeeping
provisions.
The owner or operator of any affected unit
7416
must maintain for each affected
unit
and each non-affected unit under Section
7417
1.1
6(b)(2)(B)
of this Appendix a file of all measurements,
data, reports, and other
7418
information required by this part at the source in a form suitable
for
inspection
for
7419
at least 3 years from the date of each record. Except for the certification
data
7420
required in Section 1.1 1(a)(4)
of this Appendix and the initial submission of
the
7421
monitoring plan required in Section
1.11(a)(5)
of this Appendix,
the data must
be
7422
collected beginning
with
the earlier of the date of provisional certification
or the
7423
compliance deadline in Section
1.14(b)
of this Appendix.
The certification data
7424
required
in Section
1.1 1(a)(4) of this Appendix must be collected beginning
with
7425
the date of the first certification test performed. The file must contain
the
7426
following information:
7427
7428
D
The information required
in
Sections
1.11 (a)(2),
(a)(4), (a)(5), (a)(6),
(b),
7429
(c) (if
applicable), (d), and
(e)
or
(f)
of this Appendix (as applicable);
7430
7431
The information
required
in Section 1.12
of this Appendix, for units with
7432
flue gas
desulfurization
systems or add-on mercury emission
controls;
7433
7434
For affected
units
using
mercury CEMS or sorbent
trap
monitoring
7435
systems, for each hour when the unit is
operating, record the mercury
mass
7436
emissions, calculated in accordance with Section 4
of Exhibit
C
to this
7437
Appendix.
JCAR350225-081 8507r01
7438
7439
4)
Heat
input and
mercury
methodologies for the hour; and
7440
7441
)
Formulas from the monitoring
plan for total mercury mass emissions and
7442
heat input
rate
(if
applicable);
7443
7444
j)
Certification, quality assurance
and quality control record provisions. The owner
7445
or operator of any affected unit must record
the
applicable
information
in Section
7446
1.13 of this Appendix
for each affected unit or group of units monitored
at a
7447
common stack and each non-affected
unit under Section
1.16(b)(2)(B)
of this
7448
Appendix.
7449
7450
c)
Monitoring plan recordkeeping
provisions.
7451
7452
jJ
General provisions.
The owner or operator of an affected unit must
7453
prepare and maintain a monitoring plan
for each
affected
unit or group of
7454
units monitored at
a common stack and each non-affected unit under
7455
Section
1.16(b)(2)(B)
of this Appendix.
The monitoring plan must contain
7456
sufficient
information on the continuous monitoring systems and
the use
7457
of data derived from these
systems
to demonstrate that all the unit’s
7458
mercury emissions are monitored
and reported.
7459
7460
)
Updates. Whenever the owner or operator makes
a
replacement,
7461
modification, or
change in a certified continuous monitoring
system or
7462
alternative monitoring
system under 40 CFR 75, subpart E, incorporated
7463
by reference in Section 225.140, including
a change in the automated
data
7464
acquisition and handling system or in the flue gas handling
system, that
7465
affects information reported
in the monitoring plan (e.g., a change to
a
7466
serial number for a component of a monitoring system), then the
owner or
7467
operator must
update
the monitoring
plan.
7468
7469
.)
Contents of the monitoring plan.
Each monitoring plan must contain the
7470
information in Section
1.10(d)(1)
of this Appendix in electronic format
7471
and the information in Section 1.1 0(d)(2)
in hardcopy format.
7472
7473
ç
General reporting provisions.
7474
7475
II
The designated representative
for an affected unit must comply
with all
7476
reporting
reciuirements
in
this Section and with any additional
7477
requirements set forth in 35 Ill.
Adm. Code 225.
7478
7479
)
The
designated
representative for an affected unit
must
submit the
7480
following for each
affected unit or group of units monitored
at a common
JCAR350225-081
8507r01
7481
stack
and each
non-affected
unit under
Section
1.1
6(b)(2)(B)
of
this
7482
Appendix:
7483
7484
Monitoring
plans
in accordance
with subsection
(e)
of this
Section;
7485
and
7486
7487
)
Quarterly
reports
in accordance
with
subsection
(f)
of this
Section.
7488
7489
Other
petitions
and communications.
The
designated
representative
for
an
7490
affected
unit
must
submit petitions,
correspondence,
application
fonns,
7491
and
petition-related
test results
in accordance
with
the
provisions
in
7492
Section
1.14(f)
of this
Appendix.
7493
7494
41
Quality
assurance
RATA
reports.
If requested
by
the Agency,
the
7495
designated
representative
of an affected
unit
must submit
the quality
7496
assurance
RATA
report
for each
affected
unit or
group
of units monitored
7497
at a
common stack
and
each non-affected
unit under
Section 1.1
6(b)(2)(B)
7498
of this
Appendix
by the
later
of 45 days
after
completing
a quality
7499
assurance
RATA
according
to Section
2.3
of
Exhibit
B to this Appendix
7500
or
15 days after
receiving
the
request.
The
designated
representative
must
7501
report
the hardcopy
information
required
by Section
1.1
3(a)(9)
of this
7502
Appendix
to
the
Agency.
7503
7504
)
Notifications.
The designated
representative
for
an
affected
unit must
7505
submit
written notice
to
the Agency
according
to the
provisions
in
40
CFR
7506
75.61,
incorporated
by
reference
in Section
225.140,
for
each
affected
unit
7507
or group
of units
monitored
at a common
stack and
each
non-affected
unit
7508
under
Section
1.16(b)(2)(B)
of
this Appendix.
7509
7510
Monitoring
plan
reporting.
7511
7512
II
Electronic
submission.
The designated
representative
for
an
affected
unit
7513
must submit
to the
Agency
and USEPA,
or
an alternate
Agency designee
7514
if one
is
specified,
a
complete,
electronic,
up-to-date
monitoring
plan file
7515
in a format
specified
by
the
Agency
for each
affected unit
or group
of
7516
units
monitored
at a
common stack
and each
non-affected
unit under
7517
Section
1.16(b)(2)(B)
of
this
Appendix,
as
follows:
No
later than
21 days
7518
prior
to the
commencement
of
initial certification
testing;
at the
time
of
a
7519
certification
or
recertification
application
submission;
and whenever
an
7520
update of
the electronic
monitoring
plan
is required,
either
under Section
7521
1.10
of
this Appendix
or
elsewhere
in this
Appendix.
7522
7523
1
Hardcopy
submission.
The
designated
representative
of an
affected
unit
JCAR350225-0818507r01
7524
must submit all of the hardcopy information required
under Section
1.10
7525
of
this Appendix,
for each
affected
unit or group
of units monitored at a
7526
common stack and each non-affected unit under Section
1.1 6(b)(2)(B)
of
7527
this Appendix, to the Agency prior to initial
certification. Thereafter,
the
7528
designated representative
must
submit hardcopy
information only if that
7529
portion
of the monitoring
plan is
revised. The
designated representative
7530
must submit the
required
hardcopy information as
follows: no later
than
7531
21 days prior to the commencement of initial
certification
testing; with
7532
any certification or
recertification application, if a hardcopy monitoring
7533
plan change is associated with the recertification event;
and within
30 days
7534
after any other
event
with
which
a hardcopy
monitoring plan change is
7535
associated, pursuant to Section
1.10(b)
of this
Appendix. Electronic
7536
submittal
of all monitoring
plan information, including hardcopy portions,
7537
is permissible provided that a paper copy of the
hardcopy portions can
be
7538
furnished
upon
request.
7539
7540
fi
Quarterly
reports.
7541
7542
j)
Electronic submission. Electronic
quarterly reports must be submitted,
7543
beginning with the calendar quarter containing the
compliance
date
in
7544
Section
1.14(b)
of this Appendix, unless otherwise
specified in
35
Ill.
7545
Adm.
Code 225. The designated
representative
for
an affected unit
must
7546
report the data and information in this
subsection (f)(1) and the applicable
7547
compliance certification
information in subsection
(f)(2)
of this Section
to
7548
the
Agency and USEPA, or an alternate Agency designee if one is
7549
specified, quarterly in a format specified by the
Agency, except
as
7550
otherwise provided in
40
CFR 75.64(a),
incorporated by reference in
7551
Section 225.140, for units in long-term cold storage. Each
electronic
7552
report must be submitted to the
Agency within 45 days following the end
7553
of
each calendar
quarter.
Except as otherwise provided
in 40
CFR
7554
75.64(a)(4) and
(a)(5),
incorporated
by
reference in Section 225.140, each
7555
electronic report must include the date of report
generation and the
7556
following
information for each affected unit or group of units monitored
at
7557
a common stack:
7558
7559
j
The
facility
information in 40 CFR 75.64(a)(3), incorporated by
7560
reference in Section 225.140; and
7561
7562
The information and
hourly
data
required
in subections (a) and
(b)
7563
of this Section, except for:
7564
7565
j)
Descriptions of
adjustments,
corrective action, and
7566
maintenance;
JCAR350225-081 8507r01
7567
7568
jj)
Information which
is
incompatible
with
electronic
reporting
7569
(e.g., field
data
sheets,
lab
analyses,
quality
control
plan);
7570
7571
jj)
For units
with
flue gas
desulfurization systems
or
with
add-
7572
on mercury
emission
controls,
the parametric
information
7573
in Section
1.12
of this
Appendix;
7574
7575
jy)
Information
required
by Section
1.11(d)
of
this
Appendix
7576
concerning
the
causes
of any
missing
data
periods
and
the
7577
actions
taken
to cure
those
causes;
7578
7579
y)
Hardcopy
monitoring
plan
information
required
by
Section
7580
1.10
of this
Appendix
and hardcopy
test data
and results
7581
required
by
Section
1.13 of
this
Appendix;
7582
7583
yj)
Records
of
flow
polynomial
equations
and
numerical
7584
values
required
by Section
1.13(a)(5)(E)
of
this
Appendix;
7585
7586
yjj)
Stratification
test results
required
as
part of
the
RATA
7587
supplementary records
under
Section
1.13(a)(7)
of
this
7588
Appendix;
7589
7590
yjji
Data and
results
of RATAs
that
are aborted
or
invalidated
7591
due to
problems
with
the
reference
method
or
operational
7592
problems
with
the unit
and data
and
results
of
liney
7593
checks
that
are
aborted
or
invalidated
due to
operational
7594
problems
with
the
unit;
7595
7596
jy)
Supplementary RATA
information
required
under
Section
7597
1.1 3(a)(7)
of
this Appendix,
except
that:
the
applicable
data
7598
elements
under
Section
1.13(a)(7)(B)(i)
through
(xx)
of this
7599
Appendix
and
under
Section
1.13
(a)(7)(C)(i)
through
(xiii)
7600
of this
Appendix
must
be
reported
for
flow
RATAs
at
7601
circular
or rectangular stacks
(or
ducts)
in which
angular
7602
compensation for yaw
and/or
pitch
angles
is
used
(i.e.,
7603
Method
2F
or
2G in
appendices
A-i and
A-2
to
40 CFR
60,
7604
incorporated
by
reference
in Section
225.140),
with
or
7605
without
wall
effects
adjustments;
the
applicable
data
7606
elements
under
Section
1.13(a)(7)(B)(i)
through
(xx)
of
this
7607
Appendix
and
under
Section
1.1
3(a)(7)(C)(i)
through
(xiii)
7608
of
this Appendix
must
be
reported
for any
flow
RATA
run
7609
at a circular
stack
in which
Method
2 in
appendices
A-i
JCAR350225-08
1
8507r01
7610
and A-2 to 40 CFR
60,
incorporated
by
reference in
Section
7611
225.140, is
used and a wall effects
adjustment
factor
is
7612
determined by direct measurement;
the data
under
Section
7613
1.13(a)(7)(B)(xx)
of this Appendix must be reported
for all
7614
flow RATAs
at circular stacks in which Method 2 in
7615
appendices
A-i and A-2 to 40 CFR 60, incorporated by
7616
reference in Section 225.140,
is used and a default wall
7617
effects
adjustment
factor is applied; and the data under
7618
Section 1.1
3(a)(7)(I)(i)
through (vi) must be reported for
all
7619
flow RATAs at rectangular
stacks or
ducts in which
7620
Method 2
in appendices A-i and A-2 to 40 CFR 60,
7621
incorporated
by
reference in
Section
225.140,
is
used and a
7622
wall effects
adjustment
factor
is applied.
7623
7624
)
For units using
sorbent trap monitoring systems, the hourly
7625
gas flow meter readings taken between the initial and
final
7626
meter readings
for the data collection period; and
7627
7628
j
Ounces
of
mercury
emitted during quarter and cumulative ounces
7629
of mercury emitted in the year-to-date (rounded
to
the
nearest
7630
thousandth);
and
7631
7632
j)
Unit or
stack operating hours for quarter, cumulative unit or
stack
7633
operating hours
for year-to-date;
and
7634
7635
)
Reporting period heat input (if applicable) and cumulative,
year-to-
7636
date heat input.
7637
7638
)
Compliance certification.
7639
7640
The designated
representative must certify that the monitoring
plan
7641
information in each quarterly electronic report (i.e., component
and
7642
system identification
codes, formulas,
etc.)
represent current
7643
operating conditions for the affected units.
7644
7645
The designated
representative
must submit and
sign
a compliance
7646
certification in support of each quarterly emissions monitoring
7647
report
based on
reasonable
inquiry of those persons with primary
7648
responsibility for ensuring
that all of the unit’s emissions are
7649
correctly and
fully
monitored.
The certification
must state that:
7650
7651
The monitoring data submitted were recorded in
7652
accordance with
the applicable requirements of this
JCAR350225-08
1 8507r01
7653
Appendix,
including
the
quality assurance
procedures
and
7654
specifications;
and
7655
7656
j.fl
With regard
to a unit with an
FGD
system
or
with
add-on
7657
mercury emission
controls,
that for all hours where
7658
mercury data
is missing
in accordance with Section
1.13(b)
7659
of this
Appendix,
the
add-on emission controls
were
7660
operating
within the range
of parameters listed
in
the
7661
quality-assurance
plan
for the unit
(or
that
quality-assured
7662
Q2
CEMS data were available
to
document
proper
7663
operation
of the emission
controls).
7664
7665
)
Additional reporting
requirements.
The designated representative
must
7666
also
comply with
all of the quarterly reporting
requirements
in 40
CFR
7667
75.64(d),
(f),
and
(g),
incorporated
by reference in Section
225.140.
7668
JCAR350225-081
8507r01
7669
Exhibit A to
Appendix
B — Specifications and Test Procedures
7670
7671
1. Installation and Measurement Location
7672
7673
1.1 Gas and Mercury Monitors
7674
7675
Following the procedures in Section 8.1.1 of Performance Specification 2
in Appendix B to
40
7676
CFR 60, incorporated by reference in Section 225.140, install the pollutant concentration
7677
monitor or
monitoring
system
at
a
location
where the pollutant concentration and emission rate
7678
measurements are directly representative of the total emissions from
the affected
unit. Select
a
7679
representative
measurement
point or path for the monitor probes (or for the path from the
7680
transmitter to the
receiver)
such that the
CO
2
Q
2,
concentration monitoring system, mercury
7681
concentration
monitoring
system,
or
sorbent
trap monitoring system will pass the relative
7682
accuracy test (see Section 6 of this Exhibit).
7683
7684
It is
recommended that monitor measurements be made at locations where the exhaust gas
7685
temperature is above
the dew-point temperature.
If the cause of
failure
to meet the relative
7686
accuracy tests
is determined to be the measurement location, relocate the monitor probes.
7687
7688
1.1.1 Point Monitors
7689
7690
Locate the
measurement point (1) within the centroidal area of the stack or duct cross section,
or
7691
(2)
no less
than 1.0 meter from the stack or duct wall.
7692
7693
1.2 Flow
Monitors
7694
7695
Install
the flow monitor in a location that provides representative volumetric flow over all
7696
operating
conditions. Such a location is one that provides an average velocity of the
flue gas flow
7697
over the
stack
or duct cross section and is representative of the pollutant concentration monitor
7698
location. Where
the moisture content of the flue gas affects volumetric flow measurements,
use
7699
the
procedures in both Reference Methods 1 and
4
of appendix A to 40 CFR 60, incorporated
by
7700
reference in
Section 225.140, to establish a proper location for the flow monitor. The Illinois
7701
EPA
recommends
(but
does
not
require) performing
a flow profile study following the
7702
procedures in
40 CFR 60, appendix A, Method 1, Sections 11.5 or 11.4, incorporated
by
7703
reference
in Section
225.140,
for
each
of the three operating or load levels indicated in Section
7704
6.5.2.1 of this
Exhibit to determine the acceptability of the potential flow monitor location
and to
7705
determine
the number and location of flow sampling points required to obtain a
representative
7706
flow
value. The procedure in
40 CFR
60, appendix A, Test Method 1, Section 11.5, incorporated
7707
by
reference in Section
225.140, may be used even
if the flow measurement location is greater
7708
than
or equal to
2 equivalent stack or duct diameters downstream or greater than
or equal to
V
2
7709
duct
diameter upstream from a flow disturbance. If a flow profile study shows that cyclonic
(or
7710
swirling)
or stratified flow conditions exist at the potential flow monitor location that are likely
7711
to
prevent the
monitor from meeting the
performance specifications of this part, then the Agency
JCAR350225-08
1 8507r01
7712
recommends
either (1) selecting
another
location where there is
no cyclonic
(or
swirling) or
7713
stratified flow condition, or (2) eliminating the
cyclonic
(or
swirling) or stratified flow condition
7714
by straightening the flow, e.g., by installing straightening vanes.
The Agency also recommends
7715
selecting
flow
monitor locations
to minimize
the effects of condensation, coating, erosion,
or
7716
other
conditions that
could adversely affect
flow
monitor performance.
7717
7718
1.2.1 Acceptability of Monitor
Location
7719
7720
The installation
of a
flow monitor is acceptable
if either (1) the location satisfies the minimum
7721
siting criteria of Method 1 in appendix A to 40 CFR 60, incorporated
by
reference
in Section
7722
225.140
(i.e.,
the
location is greater than or equal
to eight stack or duct diameters downstream
7723
and two diameters upstream from a flow
disturbance;
or, if necessary,
two stack
or
duct
7724
diameters downstream and one-half stack or
duct diameter upstream from a flow disturbance),
or
7725
(2) the results of a flow profile study, if performed, are acceptable (i.e., there are no cyclonic
(or
7726
swirling) or stratified flow
conditions),
and the
flow
monitor
also satisfies the performance
7727
specifications of this part. If
the flow
monitor is installed in a location that does not satisfy
these
7728
physical criteria, but nevertheless the monitor achieves
the performance specifications of this
7729
part, then the location is acceptable, notwithstanding the requirements of this Section.
7730
7731
1.2.2 Alternative Monitoring
Location
7732
7733
Whenever the owner or operator successfully demonstrates that modifications to the exhaust
duct
7734
or stack (such as
installation of straightening
vanes, modifications of ductwork, and the like)
are
7735
necessary for the
flow monitor to meet the
performance specifications, the Agency may approve
7736
an interim
alternative flow monitoring methodology and an
extension to the required certification
7737
date
for the flow monitor.
7738
7739
Where no
location exists that satisfies the physical siting criteria in Section 1.2.1,
where the
7740
results of flow
profile studies performed
at two or more
alternative
flow monitor locations
are
7741
unacceptable, or where installation of a flow monitor in either the stack or the
ducts is
7742
demonstrated to
be technically infeasible, the
owner or operator may petition the Agency
for an
7743
alternative method for monitoring flow.
7744
7745
2.
Equipment Specifications
7746
7747
2.1
Instrument Span and Range
7748
7749
In
implementing
Sections 2.1.1 through 2.1.2
of this Exhibit, set the measurement range for
each
7750 parameter (COQ
2,
or flow
rate)
high enough
to prevent
full-scale
exceedances
from occurring,
7751
yet low
enough to ensure good measurement accuracy and to maintain a
high signal-to-noise
7752
ratio. To
meet these
objectives,
select the range such that the majority of the readings
obtained
7753
during typical
unit operation are kept,
to the extent practicable, between 20.0 and
80.0
percent
of
7754
the
full-scale
range of the instrument.
JCAR350225-081 8507r01
7755
7756
2.1.1
CO2
and
02
Monitors
7757
7758
For an
02
monitor (including
02
monitors
used to measure CO2 emissions or percentage
7759
moisture), select a span value between 15.0 and 25.0 percent
02.
For a CO2monitor installed on
7760
a boiler, select a span value between 14.0 and 20.0 percent
CO
2.For a CO2
monitor installed
on a
7761
combustion turbine, an
alternative
span value between 6.0 and 14.0 percent
CO1
may be used.
7762
An
alternative
CQ2
span value below
6.0 percent may be used if an appropriate technical
7763
justification is included in the
hardcopy
monitoring plan. An alternative
02
span
value below
7764
15.0 percent
02
may be
used
if
an appropriate technical justification is included in the
7765
monitoring plan (e.gQ
2concentrations above a certain level create
an unsafe
operating
7766
condition).
Select
the
full-scale
range of the instrument to be consistent with Section 2.1 of this
7767
Exhibit and to be greater than or equal to the span value. Select the calibration
gas
concentrations
7768
for the
daily calibration error tests
and
linearity
checks in accordance with Section 5.1 of this
7769
Exhibit, as percentages of the span value. For
02
monitors with span values
21.0 percent
O
7770
purified
instrument
air containing 20.9 percent
02
may
be used
as the high-level calibration
7771
material. If a dual-range or autoranging diluent analyzer is installed, the analyzer may
be
7772
represented in the
monitoring plan as a single
component, using a special component type code
7773
specified
by
the USEPA to satisfy the requirements of 40 CFR 75.53(e)(1)(iv)(D), incorporated
7774
by
reference in Section
225.140.
7775
7776
2.1.2
Flow Monitors
7777
7778
Select the
full-scale range of the flow monitor so that it is consistent with Section 2.1
of this
7779
Exhibit and can accurately measure all potential volumetric flow rates at the flow monitor
7780
installation site.
7781
7782
2.1.2.1 Maximum
Potential Velocity and Flow Rate
7783
7784
For
this purpose,
determine
the
span value
of the flow monitor using the following procedure.
7785
Calculate
the maximum potential velocity
(MPV)
using Equation A-3a or A-3b
or
determine
the
7786
MPV
(wet basis)
from
velocity traverse testing
using Reference Method 2
(or
its allowable
7787
alternatives)
in appendix A to
40
CFR 60,
incorporated
by
reference in Section 225.140. If
using
7788
test
values, use
the
highest average velocity
(determined
from the Method 2 traverses) measured
7789
at or near
the maximum unit operating load
(or,
for units that
do
not produce electrical
or thermal
7790
output,
at the normal process
operating
conditions corresponding to the maximum stack gas
flow
7791
rate).
Express
the MPV in units of wet standard
feet
per minute
(fm).
For the purpose of
7792
providing
substitute data during periods of missing flow rate data in accordance with 40
CFR
7793
75.31
and 75.33 and as required elsewhere in this part, calculate the maximum potential stack
7794
gas
flow rate
(MPF) in
units
of standard
cubic feet per hour
(scfh),
as the product of the MPV
(in
7795
units
of wet,
standard fpm) times 60, times the cross-sectional
area of the stack or duct (in
ft
2)
at
7796
the
flow
monitor location.
7797
JCAR350225-081 8507r01
7798
(‘FdH
Y
209
Y
100
7799
MPV
= I
II
II
I
(Equation
A-3a)
A
A
20•9
— %02d
,A\100
— %H2
O)
7800
7801
or
7802
MPV
=
100
100
(Equation A-3b)
A
J%CO
2
d,A\l00—%H2
OJ
7803
7804
Where:
7805
MPV
maximum potential velocity
(fpm, standard wet
basis).
= dry-basis
F factor
(dscf/mmBtu)
from Table 1, Section 3.3.5 of
Appendix F, 40 CFR 75.
F
= carbon-based
F factor
2
(scfCO
/mmBtu)
from Table 1, Section
3.3.5
of Appendix F, 40 CFR 75.
Hf
maximum heat
input
(mmBtu/minute)
for all units, combined,
exhausting to the stack or duct where the flow monitor is located.
A
= inside cross sectional area
)
2
(ft
of the flue at the flow monitor
location.
= maximum oxygen concentration, percent dry basis, under
normal
operating conditions.
%CO
= minimum
carbon dioxide concentration, percent dry basis, under
normal operating
conditions.
= maximum percent
flue gas
moisture
content
under normal operating
conditions.
7806
7807
2.1.2.2
Span
Values and Range
7808
7809
Determine the span and
range of the
flow monitor as follows. Convert the MPV, as determined
7810
in
Section 2.1
.2.1 of this Exhibit, to the same measurement units
of
flow rate
that are used for
7811
daily
calibration
error tests
(e.g.,
scth,
kscfh, kacfm, or differential pressure
(inches
of water)).
7812
Next, determine the
“calibration span value”
by multiplying the MPV
(converted
to equivalent
7813
daily
calibration
error
units)
by a factor no less than 1.00 and no greater than 1.25, and
rounding
7814
up the
result
to
at least tvo
significant
figures. For calibration span values in inches of water,
7815
retain
at least two
decimal places. Select
appropriate reference signals for the daily calibration
7816
error tests as
percentages of the calibration
span
value,
as specified in Section
2.2.2.1
of this
7817
Exhibit. Finally,
calculate the “flow rate span value” (in scth) as
the product of
the
MPF, as
7818
determined in
Section 2.1.2.1 of
this
Exhibit, times the same factor
(between
1.00
and 1.25)
that
7819
was used
to calculate the
calibration
span value. Round off the flow rate span value to the
nearest
JCAR350225-081 8507r01
7820
1000 scth. Select the full-scale
range
of the flow monitor so that
it is greater
than
or equal to the
7821
span value and is consistent with Section 2.1
of this
Exhibit.
Include in the monitoring plan for
7822
the
unit: calculations
of the MPV, MPF, calibration span value,
flow
rate span
value,
and full-
7823
scale range
(expressed
both in scth
and, if different, in the measurement
units of
calibration).
7824
7825
2.1.2.3
Adjustment
of
Span
and Range
7826
7827
For
each affected unit or common
stack, the owner or operator must make
a
periodic
evaluation
7828
of the MPV, span, and range values for each flow
rate monitor (at a minimum, an annual
7829
evaluation
is
required)
and must make any necessary span and range
adjustments with
7830
corresponding monitoring
plan
updates,
as described in subsections
(a)
through (c) of this
7831
Section
2.1.2.3.
Span and range
adjustments
may be
required,
for example,
as a result of changes
7832
in the fuel supply, changes in the stack or ductwork
configuration, changes in the manner
of
7833
operation of the
unit, or installation
or removal of emission controls. In implementing
the
7834
provisions in subsections (a) and
(b)
of this Section 2.1.2.3,
note that flow rate data recorded
7835
during short-term,
non-representative
operating conditions (e.g., a trial burn of a different
type of
7836
fuel) must be excluded from consideration. The owner
or operator must keep the results of the
7837
most recent span and range
evaluation
on-site, in a format suitable for inspection. Make
each
7838
required span or range adjustment no later
than
45
days after the end of the quarter in which
the
7839
need to adjust the span or range is identified.
7840
7841
If
the fuel
supply,
stack or ductwork configuration, operating parameters,
or other
7842
conditions change
such that the maximum potential flow rate changes
7843
significantly, adjust the
span and range to assure the continued accuracy of
the
7844
flow
monitor. A
flsignificantH
change in the
MPV means that the guidelines
of
7845
Section
2.1
of this Exhibit can no longer bernet, as determined
by
either
a
7846
periodic evaluation
by
the owner
or operator or from the results of an audit
by the
7847
Agency. The owner or operator should evaluate
whether any planned changes
in
7848
operation of the unit may
affect the flow of the unit or stack and should plan
any
7849
necessary span and range changes needed to
account for these
changes,
so that
7850
they are made in as timely
a manner as practicable to coordinate with the
7851
operational
changes. Calculate the adjusted calibration span and flow rate
span
7852
values using the procedures in Section 2.1.2.2
of this Exhibit.
7853
7854
!
Whenever the full-scale range
is
exceeded
during
a quarter, provided that the
7855
exceedance is not caused by a monitor out-of-control
period, report
200.0
percent
7856
of
the current full-scale
range as the hourly flow rate for each hour of the
full
7857
scale exceedance. If the range is exceeded,
make appropriate adjustments to
the
7858
flow rate span and range to prevent future
full-scale exceedances. Calculate
the
7859
new calibration span value by converting the new flow
rate span value from units
7860
of
scth to
units
of daily
calibration.
A calibration error test
must be
performed
and
7861
passed to validate data
on the new range.
7862
JCAR350225-08
1 8507r01
7863
Whenever
changes are made
to the
MPV,
full-scale range,
or span value
of the
7864
flow monitor, as described
in subsections
(a) and
(b) of
this
Section, record and
7865
report
(as applicable)
the new full-scale
range setting, calculations
of the
flow rate
7866
span value, calibration
span value,
and MPV in an updated
monitoring
plan
for
7867
the unit. The monitoring
plan
update
must
be made
in the quarter in which
the
7868
changes become
effective. Record
and
report
the
adjusted
calibration
span and
7869
reference values
as parts of the
records for the calibration
error test required
by
7870
Exhibit B to
this Appendix.
Whenever
the calibration
span value is
adjusted,
use
7871
reference
values for the calibration
error test
that meet the
requirements
of Section
7872
2.2.2.1 of this
Exhibit,
based
on the most recent
adjusted calibration
span
value.
7873
Perform
a calibration error test
according to
Section
2.1
.1 of Exhibit
B to this
7874
Appendix whenever
making
a change to the flow
monitor span or range,
unless
7875
the range
change also triggers
a recertification under
Section
1.4
of this Appendix.
7876
7877
2.1.3 Mercury
Monitors
7878
7879
Determine the appropriate
span and range values
for each mercury
pollutant concentration
7880
monitor, so that
all expected
mercury concentrations
can be determined
accurately.
7881
7882
2.1.3.1
Maximum
Potential Concentration
7883
7884
The maximum
potential
concentration
depends
upon
the
type of coal combusted
in the unit.
For
7885
the
initial
MPC
determination, there
are three options:
7886
7887
]j
Use
one
of the following
default values:
9
igJscm
for bituminous
coal; 10
7888
1g/scm
for sub-bituminous
coal; 16 jig/scm
for lignite, and 1 pig/scm
for
7889
waste
coal, i.e., anthracite
cuim or bituminous
gob. If different
coals are
7890
blended,
use the highest
MPC for any fuel
in the blend; or
7891
7892
)
You may
base the
MPC
on the results of site-specific
emission testing
7893
using
one of the mercury
reference methods in
Section
1.6 of
this
7894
Appendix,
if the unit
does not
have
add-on
mercury emission controls
or a
7895
flue
gas desulfurization system,
or if
you
test upstream
of
these
control
7896
devices.
A minimum
of 3 test runs are required
at the normal operating
7897
load.
Use
the
highest total
mercury concentration
obtained
in
any of the
7898
tests as the
MPC:
or
7899
7900
You may base the MPC
on 720 or more hours
of
historical
CEMS data
or
7901
data
from a
sorbent
trap monitoring system,
if the unit
does
not
have
add
7902
on
mercury emission
controls or a
flue gas desulfurization
system
(or
if
7903
the CEMS or sorbent
trap
system
is located
upstream
of these control
7904
devices)
and
if the mercury
CEMS or sorbent trap
system has been tested
7905
for relative
accuracy
against one
of the
mercury
reference
methods
in
JCAR350225-081 8507r01
7906
Section 1.6 of this Appendix and
has met a
relative
accuracy specification
7907
of
20.0%
or
less.
7908
7909
2.1.3.2
Maximum Expected Concentration
7910
7911
For units with FGD
systems
that
significantly
reduce
mercury emissions (including fluidized
bed
7912
units that use limestone
injection)
and for units equipped
with add-on mercury emission controls
7913
(e.g., carbon
injection),
determine the maximum expected mercury concentration
(MEC)
during
7914
normal, stable operation of the unit
and emission controls. To calculate the MEC, substitute
the
7915
MPC value from Section 2.1.3.1 of this Exhibit into Equation A-2
in Section 2.1.1.2 of appendix
7916
A
to
40 CFR
75,
incorporated
by reference in Section 225.140. For units with add-on
mercury
7917
emission controls, base the percent removal efficiency on
design engineering calculations. For
7918
units
with FGD systems, use the
best available estimate of the mercury removal efficiency
of the
7919
FGD system.
7920
7921
2.1.3.3 Span and Range Values
7922
7923
For each mercury monitor, determine a high
span
value,
by rounding the MPC
7924
value from Section 2.1.3.1
of this Exhibit upward to the next highest
multiple
of
7925
10 jig/scm.
7926
7927
]
For an affected unit equipped with an FGD system
or a
unit
with add-on mercury
7928
emission controls, if the MEC value from Section 2.1.3.2 of this Exhibit
is less
7929
than
20 percent
of the high span value from subsection
(a)
of this Section,
and if
7930
the high span value is 20
jig/scm or greater, define a second, low span value
of 10
7931
jig/scm.
7932
7933
If
only a high span value is
required,
set the
full-scale range of the mercury
7934
analyzer
to be greater than or equal to the span value.
7935
7936
ç)
If two
span values
are required, you may either:
7937
7938
fl
Use
two
separate
(high and
low)
measurement scales, setting the range
of
7939
each scale to be greater than or equal
to the high or low span value, as
7940
appropriate;
or
7941
7942
)
Quality-assure two segments of a single measurement scale.
7943
7944
2.1.3.4 Adjustment
of Span and Range
7945
7946
For each
affected unit
or common stack, the owner or operator
must make a periodic evaluation
7947
of the MPC,
MEC, span, and range values for each mercury monitor (at
a
minimum,
an annual
7948
evaluation is
required) and
must
make any
necessary span and range adjustments, with
JCAR350225-081 8507r01
7949
corresponding monitoring
plan
updates.
Span and range
adjustments
may be required, for
7950
example, as a result of changes in the fuel supply, changes
in
the manner
of operation of the unit,
7951
or
installation or removal
of
emission
controls. In implementing the provisions in subsections
(a)
7952
and
(b)
of this Section, data recorded
during
short-term,
non-representative process operating
7953
conditions (e.g., a trial burn of a different type of fuel)
must be
excluded
from consideration.
The
7954
owner or operator must keep the results of the most recent span and range evaluation
on-site, in
a
7955
format
suitable
for inspection.
Make each required span or range
adjustment
no later than 45
7956
days
after the end of the quarter in which
the need to
adjust
the span or range is identified, except
7957
that up to 90 days after the end of that quarter may
be
taken
to
implement
a span
adjustment
if
7958
the calibration gas
concentrations
currently being
used for calibration error tests,
system
integrity
7959
checks, and linearity checks are unsuitable for use with the
new
span
value and new calibration
7960
materials must be
ordered.
7961
7962
The guidelines of Section 2.1
of this Exhibit do not apply to mercury monitoring
7963
systems.
7964
7965
)
Whenever a full-scale range exceedance occurs during a quarter and is not
caused
7966
by a
monitor out-of-control
period, proceed as follows:
7967
7968
L
For monitors with a single measurement scale, report that the
system was
7969
out
of
range and
invalid data was obtained until the readings come
back
7970
on-scale and, if appropriate,
make
adjustments
to the MPC, span, and
7971
range to prevent future full-scale exceedances;
or
7972
7973
For units with two separate measurement scales, if the low range
is
7974
exceeded, no further
action
is required, provided that the high range
is
7975
available and is not out-of-control or out-of-service
for any reason.
7976
However, if the
high range is not able to provide quality assured data
at
7977
the time of the low range exceedance or
at any
time
during
the
7978
continuation of
the exceedance, report that the system was out-of-control
7979
until the readings return to the low range or until the high range
is able
to
7980
provide quality assured
data
(unless
the
reason that the high-scale range
is
7981
not able to provide quality assured data is because the high-scale
range
has
7982
been exceeded; if the
high-scale range is exceeded follow the procedures
7983
in subsection
(b)(1)
of this
Section).
7984
7985
Whenever changes are made to the
MPC,
MEC, full-scale range, or span value
of
7986
the mercury monitor, record and report (as applicable)
the
new full-scale
range
7987
setting,
the
new MPC
or MEC and calculations of the adjusted span value
in an
7988
updated
monitoring plan. The
monitoring plan update must be made in the
quarter
7989
in
which the changes become effective.
In addition, record and report the adjusted
7990
span as part of the records for the
daily
calibration
error test and linearity check
7991
specified by
Exhibit
B to this Appendix. Whenever the span value is adjusted,
use
JCAR350225-081 8507r01
7992
calibration gas concentrations that meet the requirements of Section 5.1 of this
7993
Exhibit, based on the adjusted span value.
When a span adjustment is
so
7994
significant
that the
calibration
gas
concentrations
currently
being used for
7995
calibration error tests, system integrity checks and linearity checks are unsuitable
7996
for use with the new span value, then a
diagnostic linearity
or
3-level
system
7997
integrity check using the new calibration gas
concentrations
must
be performed
7998
and passed. Use the data validation
procedures in Section 1
.4(b)(3)
of this
7999
Appendix,
beginning with
the hour in which the span is changed.
8000
8001
2.2
Design for Quality
Control Testing
8002
8003
2.2.1 Pollutant Concentration
andQ
2
or
02
Monitors
8004
8005
Design and equip
each pollutant concentration and
CO2
or
02
monitor
with a
8006
calibration gas injection port that allows a
check of the entire measurement
8007
system when
calibration
gases are introduced. For extractive and
dilution
type
8008
monitors, all monitoring components exposed
to the sample gas, (e.g., sample
8009
lines,
filters, scrubbers,
conditioners, and as much of the probe as practicable) are
8010
included in
the measurement system. For in-situ type
monitors, the calibration
8011
must
check against the injected gas for the
performance of all active electronic
8012
and
optical components (e.g.,
transmitter, receiver,
analyzer).
8013
8014
])
Design and
equip
each
pollutant concentration or
CO
2
or
02
monitor to allow
8015
daily
determinations of calibration error (positive or
negative) at the zero- and
8016
mid-
or high-level concentrations
specified
in
Section 5.2 of this Exhibit.
8017
8018
2.2.2 Flow Monitors
8019
8020
Design all
flow monitors to
meet the applicable performance
specifications.
8021
8022
2.2.2.1 Calibration Error Test
8023
8024
Design and
equip each
flow monitor to allow for a daily calibration
error
test consisting of at
8025
least
two reference
values: Zero to
20 percent of span or an equivalent reference
value
(e.g.,
8026
pressure
pulse or electronic
signal) and 50 to 70 percent of span.
Flow monitor response, both
8027
before
and afler any
adjustment, must be capable of
being recorded
by
the data acquisition and
8028
handling system.
Design each
flow monitor to allow a daily calibration error test
of the entire
8029
flow
monitoring system, from
and including the probe tip
(or
equivalent)
through
and including
8030
the
data
acquisition
and handling system, or the flow
monitoring system from and including the
8031
transducer
through
and including
the
data
acquisition and handling system.
8032
8033
2.2.2.2 Interference Check
8034
JCAR350225-08 1 8507r01
8035
Design and equip each
flow
monitor with a means to ensure that the moisture
8036
expected to occur at
the
monitoring location
does not
interfere with
the proper
8037
functioning of the flow monitoring system. Design and equip each
flow
monitor
8038
with
a
means to detect,
on at least a daily basis, pluggage of each sample line
and
8039
sensing port, and malfunction
of each resistance temperature
detector
(RTD),
8040
transceiver or equivalent.
8041
8042
])
Design
and
equip
each differential pressure flow monitor to provide an automatic,
8043
periodic back purging (simultaneously
on both
sides
of the
probe)
or equivalent
8044
method of sufficient force and frequency to keep the probe and lines sufficiently
8045
free of obstructions on at least
a
daily
basis to
prevent velocity sensing
8046
interference, and a means for detecting leaks in the system on at least a quarterly
8047
basis
(manual
check is acceptable).
8048
8049
c
Design and equip each thermal flow monitor with a means to ensure on
at
least
a
8050
daily
basis
that the
probe remains sufficiently clean to
prevent velocity
sensing
8051
interference.
8052
8053
ci)
Design
and equip each ultrasonic flow monitor
with a means to
ensure
on at least
8054
a daily basis that the transceivers remain sufficiently clean (e.g., back purging
8055
system) to prevent velocity sensing interference.
8056
8057
2.2.3
Mercury Monitors
8058
8059
Design and
equip each mercury monitor to
permit
the introduction of known concentrations
of
8060
elemental mercury and HgC1
2separately, at a point
immediately
preceding the sample extraction
8061
filtration system, such
that the entire measurement system
can be
checked.
If
the mercury
8062
monitor does
not have a
converter,
the
HgCl2
injection
capability
is not required.
8063
8064
3. Performance Specifications
8065
8066
3.1 Calibration Error
8067
8068
The
calibration error
performance specifications in this Section apply only to
7-
8069
day
calibration error tests under Sections 6.3.1
and
6.3.2 of this Exhibit
and to the
8070
offline calibration demonstration described in Section 2.1 .1.2 of Exhibit B to
this
8071
Appendix. The calibration
error limits for daily operation of the continuous
8072
monitoring
systems
required under this part are
found
in Section 2.1.4(a)
of
8073
Exhibit B to this Appendix.
8074
8075
j)
The
calibration error
of a mercury concentration monitor must not deviate from
8076
the
reference value of either the zero
or upscale calibration gas by more than
5.0
8077
percent of the span value, as calculated using Equation A-S
of
this Exhibit.
JCAR350225-08 1 8507r01
8078
Alternatively,
if the span value is
10
fig/scm,
the
calibration
error test results
are
8079
also acceptable if the absolute
value of the difference between the monitor
8080
response value and the reference
value, R-A in
Equation
A-5 of this Exhibit,
is
8081
1.0
rig/scm.
8082
8083
CE
=
x
100
(Equation A-5)
8084
8085
Where:
8086
CE =
Calibration error as
a percentage of
the
span of the instrument.
R
=
Reference
value of zero or upscale (high-level or mid-level,
as
applicable) calibration
gas
introduced into
the monitoring system.
A =
Actual monitoring system response to the calibration
gas.
S
Span of the instrument, as specified in Section 2
of
this
Exhibit.
8087
8088
8089
3.2
Linearity
Check
8090
8091
For
CO2
or
02
monitors (including
02
monitors
used to measure CO2 emissions or
percent
8092
moisture):
8093
8094
The error in linearity for each calibration gas concentration (low-, mid-,
and high-
8095
levels)
must not exceed
or deviate from the reference value
by
more than 5.0
8096
percent as calculated using Equation A-4
of this
Exhibit
or
8097
8098
The absolute
value
of the difference between the average of the monitor
response
8099
values and the average of the reference values,
R-A in Equation A-4 of this
8100
Exhibit, must
be less
than or equal to 0.5 percent
CO2
or
02,
whichever is less
8101
restrictive.
8102
8103
ç)
For
the linearity check and the 3-level system integrity
check of a mercury
8104
monitor, which are required,
respectively,
under Section 1
.4(c)(
1
)(B)
and
8105
(c)(1)(E) of this Appendix, the measurement
error must not exceed 10.0 percent
8106
of the reference
value
at any of the three gas levels. To calculate the measurement
8107
error at
each level, take
the absolute value of the difference between the reference
8108
value and mean CEM response,
divide the result by the reference value, and
then
8109
multiply by 100. Alternatively, the results at any
gas level are acceptable if the
8110
absolute value of the difference between the average
monitor response and the
8111
average reference
value,
i.e., R-A in Equation A-4 of this Exhibit, does
not exceed
8112
0.8
.igJm
3.
The principal
and alternative performance specifications in this
8113
Section also apply to the single-level
system
integrity
check described in Section
JCAR350225-08 1 8507r01
8114
2.6 of Exhibit
B to this Appendix.
8115
8116
LE=
R
xlOO
(EguationA-4)
8117
8118
Where:
8119
LE = Percentage linearity error, based upon the reference
value.
R
= Reference value of low-, mid-, or high-level calibration
gas
introduced
into the monitoring system.
A
Average of the monitoring
system
responses.
8120
8121
3.3 Relative Accuracy
8122
8123
3.3.1
Relative
Accuracy for
CO2
and
02
Monitors
8124
8125
The
relative accuracy for CO
2and
02
monitors must not exceed 10.0 percent. The relative
8126
accuracy test results
are also acceptable
if the difference between the mean value of the
CO
2or
8127
Q2
monitor
measurements and the corresponding reference
method measurement mean value,
8128
calculated using
equation
A-7 of this Exhibit, does not exceed
±
1.0
percent
CO2or
02.
8129
8130
d
=
(Equation A-7)
8131
8132
Where:
8133
n
= Number
of data points.
The difference between a reference method value
and the
corresponding
continuous
emission monitoring system value
CEM
1)
at a given point in time i.
8134
8135
3.3.2
Relative Accuracy for Flow Monitors
8136
8137
The relative accuracy of flow monitors must not exceed
10.0 percent at any load
8138
(or operating)
level
at which a RATA is performed
(i.e.,
the low-, mid-,
or high-
8139
level,
as
defined in Section 6.5.2.1
of this Exhibit).
8140
8141
i)
For affected units where the average of the flow reference
method measurements
8142
of gas velocity
at
a particular load (or operating) level of the relative accuracy
test
8143
audit is less
than or equal
to 10.0 fps, the difference between the mean value
of
8144
the
flow monitor velocity measurements
and the reference method mean value
in
8145
fps at that
level
must not exceed
±
2.0
fps,
wherever
the 10.0 percent
relative
JCAR350225-08 1 8507r01
8146
accuracy specification is not achieved.
8147
8148
3.3.3 Relative Accuracy for
Moisture Monitoring Systems
8149
8150
The relative accuracy
of
a
moisture monitoring
system
must
not exceed 10.0 percent.
The
8151
relative accuracy test results are also acceptable
if the difference between the mean
value of the
8152
reference method measurements
(in
percent 0)2
H
and the corresponding mean value of the
8153
moisture monitoring system measurements (in percent
H
2
0),
calculated
using Equation A-7
of
8154
this Exhibit does not
exceed ± 1.5
percent H
2
0.
8155
8156
3.3.4 Relative
Accuracy for Mercury Monitoring Systems
8157
8158
The relative accuracy
of a mercury
concentration monitoring
system
or a sorbent trap
monitoring
8159
system must not exceed 20.0 percent. Alternatively,
for affected units
where
the average of
the
8160
reference method
measurements
of
mercury concentration during the relative accuracy
test audit
8161
is less than 5.0 jig/scm, the test results are
acceptable
if the difference between
the mean value
of
8162
the monitor
measurements and the
reference method mean value does not exceed 1.0
jig/scm, in
8163
cases
where the relative accuracy specification
of
20.0
percent is not achieved.
8164
8165
3.4 Bias
8166
8167
3.4.1 Flow Monitors
8168
8169
Flow monitors must not be biased low as determined by the test procedure in
Section 7.4 of this
8170
Exhibit. The bias
specification
applies to all flow monitors including those measuring
an average
8171
gas velocity of 10.0
fps or less.
8172
8173
3.4.2
Mercury Monitoring Systems
8174
8175
Mercury
concentration monitoring
systems and sorbent trap monitoring systems must not
be
8176
biased
low as determined by the test procedure in Section 7.4 of this Exhibit.
8177
8178
3.5 Cycle Time
8179
8180
The
cycle time for mercury concentration monitors, oxygen monitors used to determine
percent
8181
moisture, and any
other monitoring
component
of a continuous emission monitoring
system that
8182
is required to
perform
a cycle time test must not exceed 15 minutes.
8183
8184
4. Data Acquisition and Handling Systems
8185
8186
Automated
data
acquisition and handling systems must read
and record the full range ofpollutant
8187
concentrations and volumetric flow from zero through span and
provide a continuous, permanent
8188
record
of all measurements and required information as an ASCII flat file capable of
JCAR350225-08
1
8507r01
8189
transmission both
by
direct computer-to-computer
electronic transfer via modem and EPA-
8190
provided software and by an IBM-compatible personal computer
diskette. These systems also
8191
must
have the capability of interpreting
and converting the individual output signals from
a flow
8192
monitor, a
CO2
monitor, an
02
monitor,
a moisture monitoring system, a mercury concentration
8193
monitoring system, and a sorbent trap monitoring system,
to
produce
a continuous readout of
8194
pollutant emission rates or pollutant mass emissions (as applicable)
in
the appropriate
units
(çg
8195
lb/hr.
lb/mmBtu, ounces/hr,
tons/hr).
These
systems also must have the capability of interpreting
8196
and converting the individual output
signals from a flow monitor to produce a continuous
8197
readout of pollutant mass emission rates in the units of
the
standard.
Where CO2emissions are
8198
measured
with
a
continuous
emission monitoring system, the data acquisition and handling
8199
system must also
produce
a readout of
CO2
mass emissions
in tons.
8200
8201
Data acquisition and handling systems must also compute
and
record
monitor
calibration error,
8202 any bias
adjustments to mercury pollutant
concentration data, flow rate data, or mercury emission
8203
rate data.
8204
8205
5. Calibration Gas
8206
8207
5.1 Reference Gases
8208
8209
For the purposes of
this Appendix,
calibration gases include the following:
8210
8211
5.1.1 Standard Reference
Materials
(SRM)
8212
8213
These calibration gases may be obtained from the National Institute of Standards and
8214
Technology (NIST)
at the following
address:
Quince
Orchard
and Cloppers Road, Gaithersburg,
8215
MD
20899-0001.
8216
8217
5.1.2 SRM-Equivalent Compressed
Gas
Primary Reference
Material
(PRM)
8218
8219
Contact the
Gas Metrology Team, Analytical
Chemistry
Division, Chemical
Science and
8220
Technology
Laboratory
of NIST, at
the address in Section 5.1.1, for a list of vendors and
8221
cylinder
gases.
8222
8223
5.1.3
NIST Traceable Reference Materials
8224
8225
Contact the Gas
Metrology Team, Analytical
Chemistry
Division,
Chemical Science and
8226
Technology
Laboratory of NIST, at the address in Section 5.1.1,
for
a list of vendors and
8227
cylinder gases that meet the definition for a NIST Traceable Reference Material (NTRM)
8228
provided in 40 CFR
72.2, incorporated
by reference in Section 225.140.
8229
8230
5.1.4
EPA Protocol
Gases
8231
JCAR350225-08 1 8507r01
8232
An EPA
Protocol
Gas is a calibration
gas
mixture prepared and analyzed
8233
according to Section 2 of the “EPA Traceability
Protocol
for Assay and
8234
Certification
of
Gaseous
Calibration
Standards”,
September 1997, EPA-600/R-
8235
97/121
or
such revised procedure
as
approved
by
the Administrator
(EPA
8236
Traceability Protocol).
8237
8238
An EPA Protocol Gas must have a specialty gas
producer-certified uncertainty
8239
(95
percent
confidence interval) that must not be greater than 2.0 percent of the
8240
certified concentration
(tag value)
of the gas mixture. The uncertainty must be
8241
calculated using the
statistical
procedures
(or
equivalent statistical techniques)
8242
that
are listed in Section 2.1.8 of the EPA Traceability Protocol.
8243
8244
ci
A
copy ofEPA-600/R-97/121 is available from the
National Technical
8245
Information
Service, 5285 Port
Royal
Road, Springfield VA, 703-605-6585 or
8246
http ://www.ntis. gov, and from http ://www. epa.
gov/ttnlemc/news.html or http
://
8247
www.epa.
gov/appcdwww/tsb/index.html.
8248
8249
5.1.5
Research
Gas
Mixtures
8250
8251
Research gas
mixtures must be vendor-certified to be within 2.0
percent of the concentration
8252
specified on
the
cylinder
label (tag
value),
using the
uncertainty calculation procedure in Section
8253
2.1.8 of the
“EPA Traceability
Protocol
for
Assay and Certification of Gaseous Calibration
8254
Standards”,
September 1997,
EPA-600/R-97/121. Inquiries about the RGM program should
be
8255
directed
to: National
Institute
of Standards and Technology, Analytical
Chemistry Division,
8256
Chemical Science
and
Technology Laboratory, B-324 Chemistry,
Gaithersburg MD 20899.
8257
8258
5.1.6 Zero Air Material
8259
8260
Zero air
material is defined
in 40 CFR 72.2, incorporated by reference in Section
225.140.
8261
8262
5.1.7
NIST/EPA-Approved Certified Reference Materials
8263
8264
Existing
certified reference
materials
(CRMs)
that
are still within
their certification
period may
8265
be
used as
calibration gas.
8266
8267
5.1.8 Gas Manufacturer’s
Intermediate Standards
8268
8269
Gas
manufacturer’s
intermediate standards is defined in 40 CFR
72.2, incorporated
by reference
8270
in Section
225.140.
8271
8272
5.1.9 Mercury Standards
8273
8274
For 7-day
calibration
error
tests
of mercury concentration monitors
and
for daily calibration error
JCAR350225-08 1 8507r01
8275
tests of mercury monitors, either NIST-traceable elemental
mercury
standards (as defined in
8276
Section
225.130)
or a NIST-traceable
source of oxidized mercury (as
defined
in Section
8277
225.130)
maybe used. For linearity checks, NIST-traceable
elemental mercury standards must
8278
be used. For 3-level and single-point system integrity checks under
Section
l.4(c)(l)(E)
of this
8279
Appendix,
Sections 6.2(g) and
6.3.1 of this Exhibit, and Sections 2.1.1, 2.2.1
and
2.6
of Exhibit
8280
B
to this
Appendix, a NIST-traceable
source of oxidized mercury must
be used.
Alternatively,
8281
other NIST-traceable standards may be used
for the required checks, subject to the approval
of
8282
the Agency.
Notwithstanding
these requirements, mercury calibration
standards that are not
8283
NIST-traceable may
be used for
the tests described in this Section until December 31, 2009.
8284
However, on and after January 1, 2010, only
NIST-traceable calibration standards must be
used
8285
for these tests.
8286
8287
5.2 Concentrations
8288
8289
Four
concentration levels
are required
as follows.
8290
8291
5.2.1 Zero-level
Concentration
8292
8293
0.0 to 20.0 percent of span, including span for high-scale or both low- and high-scale
for
CO2
8294
and
02
monitors, as
appropriate.
8295
8296
5.2.2 Low-level Concentration
8297
8298
20.0 to 30.0 percent of span,
including
span for high-scale or both low- and high-scale
for
CO2
8299
and
02
monitors, as
appropriate.
8300
8301
5.2.3
Mid-level Concentration
8302
8303
50.0
to
60.0
percent of span, including span for high-scale or both low-
and
high-scale for
CO2
8304
and
02
monitors, as
appropriate.
8305
8306
5.2.4 High-level Concentration
8307
8308
80.0 to 100.0
percent of span, including span for high-scale
or both low-and high-scale for
CO2
8309
andQ2
monitors, as appropriate.
8310
8311
6. Certification Tests and Procedures
8312
8313
6.1
General Requirements
8314
8315
6.1.1 Pretest Preparation
8316
8317
Install the components of the
continuous
emission monitoring system (i.e., pollutant
JCAR350225-08 1 8507r01
8318
concentration monitors,
2
CO
or
02
monitor, and
flow monitor) as specified in Sections 1, 2,
and
8319
3 of this
Exhibit,
and prepare each system component and the combined system
for operation in
8320
accordance
with
the manufacturer’s written instructions.
Operate
the units during each period
8321
when measurements are made. Units may be tested
on non-consecutive days. To the extent
8322
practicable, test the DAHS software prior to testing the monitoring
hardware.
8323
8324
6.1.2
Requirements for Air Emission Testing Bodies
8325
8326
On and after January 1, 2009, any Air Emission Testing
Body
(AETB)
conducting
8327
relative accuracy test
audits
of CEMS and sorbent trap monitoring systems
under
8328
Part 225, Subpart B, must conform to the requirements
of
ASTM
D7036-04
8329
(incorporated
by
reference
in Section 225.140). This Section is not applicable
to
8330
daily operation, daily calibration error checks,
daily
flow
interference
checks,
8331
quarterly linearity checks
or
routine
maintenance
of CEMS.
8332
8333
j
2)
The AETB must provide to the
affected sources certification that the AETB
8334
operates in conformance with, and that data submitted to the Agency has
been
8335
collected in accordance
with, the requirements of ASTM D7036-04
(incorporated
8336
by reference in Section
225.140).
This certification may be provided
in the form
8337
ofi
8338
8339
jj
A certificate
of
accreditation
of relevant scope issued by a recognized,
8340
national accreditation
body;
or
8341
8342
A letter of certification signed
by
a member of the senior management
8343
staff
of
the
AETB.
8344
8345
c
The AETB must either provide a Qualified Individual on-site to conduct
or must
8346
oversee all relative accuracy testing carried out
by
the AETB
as required in
8347
ASTM
D7036-04
(incorporated by reference in Section
225.140).
The
Oualified
8348
Individual must
provide
the
affected sources with copies
of the qualification
8349
credentials relevant
to the scope of the testing conducted.
8350
8351
6.2 Linearity
Check (General Procedures)
8352
8353
Check
the linearity of each CO
2.Hg, and
02
monitor while the unit, or group of units
for a
8354
common stack, is
combusting fuel at conditions
of typical stack temperature and pressure;
it is
8355
not necessary
for the unit to be generating electricity during this test. For
units with two
8356
measurement
ranges
(high
and
low)
for a particular parameter, perform a linearity
check on
both
8357
the
low scale and the high scale. For on-going quality assurance of the CEMS,
perform
linearity
8358
checks, using the
procedures in this Section,
on the
ranges
and at the frequency specified in
8359
Section
2.2.1
of Exhibit B to this Appendix. Challenge each monitor
with calibration gas, as
8360
defined in
Section 5.1 of this Exhibit, at the low-, mid-, and high-range
concentrations specified
JCAR350225-08 1 8507r01
8361
in
Section
5.2 of this
Exhibit. Introduce the
calibration gas at the gas injection port, as specified
8362
in Section 2.2.1
of
this Exhibit. Operate each monitor at its normal operating temperature
and
8363
conditions. For
extractive
and dilution
te monitors, pass the calibration gas through all filters,
8364
scrubbers, conditioners, and other monitor components
used
during normal sampling and
8365
through as much
of
the sampling probe as is practical. For in-situ
te
monitors, perform
8366
calibration checking all active electronic and optical components, including the transmitter,
8367
receiver, and analyzer.
Challenge
the monitor three times with each reference gas (see example
8368
data sheet in Figure
1). Do not use the same
gas
twice in
succession. To the extent
practicable,
8369
the
duration of each linearity test, from the hour of the first injection
to
the hour of the
last
8370
injection,
must not
exceed
24 unit
operating hours. Record the monitor response from the data
8371
acquisition and handling system. For each concentration, use the average of the responses
to
8372
determine the error in
linearity using
Equation A-4 in this Exhibit. Linearity checks are
8373
acceptable
for monitor or monitoring system certification, recertification, or quality assurance
if
8374
none of the test
results
exceed the applicable
performance
specifications
in Section
3.2
of this
8375
Exhibit. The status of emission data from a CEMS prior to and during a
linearity
test
period
must
8376
be determined as
follows:
8377
8378
For the
initial certification
of a CEMS, data from the monitoring system are
8379
considered invalid until all certification tests, including the linearity test,
have
8380
been
successfully
completed, unless the conditional data validation procedures
in
8381
Section 1.4(b)(3) of this Appendix are used. When the procedures in Section
8382
1 .4(b)(3)
of this Appendix
are
followed, the words
‘initia1 certification’ apply
8383
instead of 11
recertification”, and complete all of the initial certification
tests by
8384
January 1, 2009, rather than within the time periods specified in Section
8385
1.4(b)(3)(D)
of this Appendix for the individual tests.
8386
8387
For the routine quality assurance linearity checks required
by
Section 2.2.1
of
8388
Exhibit B to this Appendix, use the data validation procedures in Section 2.2.3
of
8389
Exhibit B to this Appendix.
8390
8391
When a linearity test is required as a diagnostic test or for recertification,
use the
8392
data
validation procedures
in Section
1.4
(b)(3)
of this Appendix.
8393
8394
For
linearity tests of non-redundant backup monitoring
systems, use the data
8395
validation procedures in Section 1
.4(d)(2)(C)
of this Appendix.
8396
8397
For
linearity tests performed during a grace period
and after the
expiration
of a
8398
grace period, use the data validation procedures in Sections 2.2.3 and 2.2.4,
8399
respectively,
of Exhibit B to this Appendix.
8400
8401
For
all other linearity checks,
use
the data validation
procedures in Section 2.2.3
8402
of Exhibit B to this Appendix.
8403
JCAR350225-08 1 8507r01
8404
g)
For mercury monitors,
follow
the
guidelines
in Section 2.2.3 of this Exhibit in
8405
addition
to the applicable procedures in
Section 6.2 when performing the
system
8406
integrity checks
described in Section 1.4(c)(1)(E)
and in Sections 2.1.1, 2.2.1,
and
8407
2.6 of Exhibit B to this Appendix.
8408
8409
For
mercury
concentration monitors,
if
moisture
is added to the calibration
gas
8410
during the required
linearity checks or system
integrity checks, the moisture
8411
content of the calibration
gas must be accounted for. Under
these circumstances,
8412
the
dry
basis concentration of the calibration
gas must be used to calculate
the
8413
linearity error or
measurement error
(as
applicable).
8414
8415
6.3 7-Day Calibration Error
Test
8416
8417
6.3.1 Gas Monitor
7-day Calibration Error Test
8418
8419
Measure the calibration error of each mercury
concentration monitor
and each
CO2or
02
8420
monitor while the unit
is
combusting fuel
(but
not necessarily
generating
electricity)
once
each
8421
day for
7
consecutive operating days
according to the following procedures.
For mercury
8422
monitors, you may perform this test using either
elemental mercury standards or a
NIST
8423
traceable source of
oxidized
mercury. Also for mercury monitors,
if moisture is added to the
8424
calibration gas,
the added moisture
must
be accounted for and the dry-basis
concentration
of the
8425
calibration gas must be used to calculate
the calibration error.
(In
the event
that unit outages
8426
occur after the commencement of the test,
the 7 consecutive unit operating
days need not be
7
8427
consecutive calendar days.) Units using dual
span monitors must perform the calibration
error
8428
test on both high- and low-scales of the pollutant concentration
monitor. The calibration error
8429
test procedures
in this Section and in
Section 6.3.2 of this Exhibit must also
be used to
perform
8430
the
daily
assessments
and additional calibration
error tests required under Sections 2.1.1
and
8431
2.1.3 of Exhibit B to
this Appendix.
Do not make manual or automatic
adjustments
to the
8432
monitor settings until after taking measurements
at both zero and high concentration levels
for
8433
that day during the 7-day test. If automatic adjustments are made following
both
injections,
8434
conduct the calibration error test such that the magnitude
of the
adjustments
can be
determined
8435
and recorded.
Record and report test
results
for each
day
using the unadjusted
concentration
8436
measured in the calibration error test prior to making any
manual or automatic adjustments
(i.e.,
8437
resetting the
calibration).
The calibration
error tests should be approximately
24 hours apart,
8438
(unless the
7-day
test is performed over non-consecutive
days). Perform calibration error
tests
at
8439
both the zero-level
concentration and
high-level concentration,
as specified in Section 5.2
of this
8440
Exhibit.
Alternatively, a mid-level concentration
gas
(50.0
to 60.0
percent
of the span
value)
may
8441
be used
in lieu of the high-level gas, provided that the
mid-level gas is more representative
of
the
8442
actual stack gas concentrations. Use only calibration gas,
as specified in Section 5.1 of this
8443
Exhibit. Introduce
the
calibration
gas at the gas
injection
port,
as
specified
in Section 2.2.1
of this
8444
Exhibit. Operate
each monitor in its normal
sampling mode. For extractive
and dilution type
8445
monitors, pass
the calibration gas through all
filters, scrubbers, conditioners,
and other monitor
8446
components used during normal sampling and through
as much of the sampling probe
as is
JCAR350225-081
8507r01
8447
practical. For
in-situ type monitors,
perform calibration, checking all active electronic
and
8448
optical components, including the transmitter, receiver,
and analyzer. Challenge the pollutant
8449
concentration monitors
and
CO
2or
02
monitors once with
each
calibration
gas. Record the
8450
monitor
response from the data
acquisition and handling
system.
Using Equation A-5
of
this
8451
Exhibit, determine the calibration error
at each concentration once each day
(at
approximately
8452
24-hour
intervals)
for 7 consecutive days according
to the procedures given in this Section. The
8453
results of a 7-day calibration error test are acceptable for monitor or
monitoring system
8454
certification,
recertification or
diagnostic testing if none of these daily calibration error test
8455
results
exceed the applicable performance specifications
in Section 3.1 of this Exhibit. The status
8456
of emission data from a
gas
monitor prior to and during a 7-day calibration
error test period must
8457
be
determined as follows:
8458
8459
For initial certification, data from the
monitor are considered invalid until all
8460
certification tests,
including the 7-day calibration error test, have been
8461
successfully completed, unless the conditional
data
validation procedures in
8462
Section 1.4(b)(3)
of this Appendix are used. When the procedures in Section
8463
1.4(b)(3)
of this Appendix are followed, the words
“initial certification” apply
8464
instead
of “recertification”,
and complete all of the initial certification tests
by
8465
January
1, 2009, rather than within the
time
periods specified in Section
8466
1
.4(b)(3)(D)
of this Appendix for the individual tests.
8467
8468
When a
7-day calibration
error test is required as a diagnostic test or for
8469
recertification, use the
data
validation
procedures in Section 1
.4(b)(3)
of this
8470
Appendix.
8471
8472
6.3.2
Flow Monitor 7-day Calibration Error Test
8473
8474
Flow monitors
installed on peaking units
(as
defined in 40 CFR 72.2, incorporated
by reference
8475
in
Section 225.140)
are exempted from the
7-day calibration error test requirements of this
part.
8476
In all other
cases, perform the 7-day calibration error test of a flow monitor, when required
for
8477
certification,
recertification or
diagnostic
testing, according
to the following procedures.
8478
Introduce
the reference signal
corresponding
to the values specified in Section 2.2.2.1
of this
8479
Exhibit to the
probe tip
(or equivalent),
or to the transducer.
During the 7-day certification test
8480
period,
conduct the calibration error test while the unit is operating once each unit operating
day
8481
(as
close to
24-hour intervals as practicable). In the event
that unit
outages occur after the
8482
commencement
of the test, the 7 consecutive operating days need not be
7 consecutive calendar
8483
days.
Record the
flow monitor responses
by means of the data acquisition and handling
system.
8484
Calculate
the
calibration error using Equation
A-6 of
this Exhibit.
Do not perform any corrective
8485
maintenance,
repair, or replacement upon the flow monitor during
the 7-day test period other
8486
than that
required in the quality assurance/quality control plan required
by
Exhibit B
to this
8487
Appendix.
Do not
make adjustments
between the zero and high reference level measurements
on
8488
any
day
during
the 7-day test. If the flow
monitor operates within the calibration error
8489
performance
specification
(i.e., less than or equal
to
3.0 percent
error each day and requiring no
JCAR350225-081 8507r01
8490
corrective
maintenance, repair, or replacement during the 7-day test period), the flow monitor
8491
passes
the calibration error test.
Record all maintenance activities
and the
magnitude of any
8492
adjustments. Record
output readings from the data acquisition and handling system before and
8493
after all
adjustments. Record and report all
calibration
error test results using
the unadjusted
flow
8494
rate
measured in the calibration
error test
prior to resetting
the
calibration. Record all
8495
adjustments made during the
7-day period at the time the
adjustment
is made, and
report
them
in
8496
the certification or
recertification application. The status of emissions data from a flow monitor
8497
prior to and
during a 7-day calibration error test period must be determined as follows:
8498
8499
For
initial certification, data from the monitor are considered invalid until all
8500
certification tests,
including the
7-day
calibration error test, have been
8501
successfully completed,
unless the conditional data validation procedures in
8502
Section
1.4(b)(3)
of this
Appendix are used. When the procedures in Section
8503
1 .4(b)(3)
of this Appendix are followed, the words “initial
certification”
apply
8504
instead of
“recertification”, and complete all of the initial certification tests by
8505
January 1, 2009, rather than within the time periods specified in
Section
8506
1
.4(b)(3)(D)
of
this Appendix for the individual tests.
8507
8508
When a 7-day calibration error test is
required
as
a diagnostic test or for
8509
recertification,
use the data validation procedures in Section 1 .4(b)(3).
8510
8511
CE=
xlOO
(EquationA-6)
8512
8513
Where:
8514
Calibration error as a percentage
of span.
R
= Low or high level reference value specified in Section
2.2.2.1
of this
Exhibit.
A = Actual flow
monitor response to the reference value.
S
= Flow monitor
calibration span value as determined under Section
2.1.2.2 of this Exhibit.
8515
8516
6.3.3
8517
8518
For gas or
flow
monitors installed on peaking units, the exemption
from performing
the 7-day
8519
calibration error
test
applies as long as the unit
continues
to
meet the definition of a peaking
unit
8520
in
40 CFR
72.2, incorporated by
reference
in
Section 225.140. However, if at the end of a
8521
particular
calendar year or
ozone season, it is determined that peaking unit status has been lost,
8522
the owner
or
operator must perform a diagnostic 7-day calibration error test of
each
monitor
8523
installed on the
unit,
by
no later than December 31 of
the following calendar year.
JCAR350225-08
1 8507r01
8524
8525
6.4 Cycle Time Test
8526
8527
Perform cycle time tests for each pollutant concentration
monitor and continuous emission
8528
monitoring system while the unit is operating, according
to
the
following procedures. Use a zero-
8529
level
and
a
high-level calibration
gas
(as
defined in Section 5.2
of this
Exhibit)
alternately. For
8530
mercury monitors, the calibration gas
used for this test may either be the elemental or
oxidized
8531
form of mercury. To determine the downscale cycle
time,
measure the concentration of the
flue
8532
gas emissions until
the
response stabilizes. Record the stable emissions
value.
Inject
a zero-level
8533
concentration calibration gas into the
probe tip
(or injection
port leading to the calibration
cell,
8534
for in-situ systems with no
probe).
Record the time of the zero
gas
injection,
using the data
8535
acquisition and handling
system
(DAHS).
Next, allow the
monitor to measure the concentration
8536
of the zero gas until the response stabilizes. Record the stable ending
calibration gas reading.
8537
Determine the downscale cycle time as the time it
takes for 95.0 percent of the step change
to be
8538
achieved between
the stable stack
emissions value
and the stable ending zero
gas reading. Then
8539
repeat the procedure, starting with stable stack emissions
and injecting the high-level gas, to
8540
determine the
upscale cycle time,
which is the time it takes for 95.0 percent
of the step change to
8541
be
achieved between the stable stack emissions value
and the stable
ending
high-level
gas
8542
reading. Use the following criteria to assess when a stable reading
of stack emissions or
8543
calibration gas
concentration has
been attained. A stable
value
is equivalent to
a
reading with
a
8544
change of less
than
2.0 percent of the
span
value
for 2 minutes, or a reading with a change
of less
8545
than 6.0
percent from the measured average concentration over
6 minutes. Alternatively, the
8546
reading is considered stable if it changes by no more than
0.5 ppm, 0.5 ig/m
3
(for
mercury) for
8547
two
minutes.
(Owners
or operators of systems that do not record
data in 1-minute or 3-minute
8548
intervals may petition
the Agency
for alternative stabilization criteria). For monitors
or
8549
monitoring
systems that
perform
a series of operations
(such
as purge, sample, and analyze),
8550
time
the
injections of the calibration gases so they will produce the
longest possible cycle time.
8551
Refer to Figures 6a
and 6b in this Exhibit
for example calculations of upscale and downscale
8552
cycle times. Report the slower of the two cycle times (upscale or
downscale)
as the cycle time
8553
for the analyzer.
On and after January
1,
2009,
record the cycle time for each component
8554
analyzer separately. For time-shared systems, perform the cycle time
tests at each of the probe
8555
locations that
will be
polled
within
the same 15-minute
period during monitoring system
8556
operations. To
determine
the cycle time for time-shared systems, at each
monitoring location,
8557
report the sum
of the cycle time observed at
that monitoring location plus the sum of the time
8558
required for all purge
cycles
(as
determined by the continuous emission
monitoring system
8559
manufacturer)
at
each of the probe locations
of the time-shared systems. For monitors with
dual
8560
ranges, report
the test results for each range separately. Cycle
time test results are acceptable
for
8561
monitor or monitoring system certification, recertification or diagnostic
testing
if none of the
8562
cycle
times exceed 15
minutes. The
status of emissions data from a monitor
prior to and during
a
8563
cycle time test
period must be determined
as follows:
8564
8565
For initial certification, data from the monitor
are considered invalid until all
8566
certification
tests, including the cycle time test, have been
successfully completed,
JCAR350225-08
1 8507r01
8567
unless
the conditional
data validation
procedures
in
Section 1
.4(b)(3)
of
this
8568
Appendix are used.
When the procedures
in Section 1.4(b)(3)
of this
Appendix
8569
are
followed,
the
words “initial certification”
apply
instead of “recertification”,
8570
and complete
all of
the
initial certification
tests
by January 1, 2009,
rather than
8571
within the time
periods specified
in Section 1.4(b)(3)(D)
of this
Appendix for the
8572
individual tests.
8573
8574
j)
When a cycle
time test
is
required
as a diagnostic
test or for
recertification, use
8575
the data
validation procedures
in
Section
1
.4(b)(3)
of this Appendix.
8576
8577
6.5
Relative Accuracy and
Bias
Tests
(General
Procedures)
8578
8579
Perform the required relative
accuracy test audits
(RATAs)
as follows for each
flow
monitor,
8580
each
02
or
C0
diluent monitor
used to
calculate heat input,
each
mercury
concentration
8581
monitoring system, each
sorbent trap monitoring
system,
and each moisture monitoring
system.
8582
8583
Except
as otherwise
provided
in this
subsection,
perform each RATA
while
the
8584
unit
(or units,
if more
than
one unit exhausts into
the
flue) is
combusting the
fuel
8585
that is
a
normal primary or backup
fuel for
that unit
(for
some units,
more than
8586
one
type of fuel may be
considered normal,
e.g., a unit that
combusts gas or
oil on
8587
a
seasonal
basis).
For
units that co-fire fuels
as the predominant
mode of
8588
operation,
perform the
RATAs while
co-firing. For mercury
monitoring
systems,
8589
perform the RATAs
while
the
unit
is combusting coal.
When relative
accuracy
8590
test audits are performed
on CEMS
installed on bypass
stacks/ducts,
use the fuel
8591
normally combusted
by the unit (or
units, if more
than
one unit exhausts
into
the
8592
flue)
when emissions
exhaust
through the bypass stack/ducts.
8593
8594
Perform
each RATA at the load
(or
operating)
levels specified in
Section
6.5.1
or
8595
6.5.2
of this
Exhibit or in Section
2.3.1.3
of Exhibit
B to this Appendix,
as
8596
applicable.
8597
8598
ç
For
monitoring
systems
with
dual ranges, perform
the relative
accuracy
test
on
the
8599
range normally
used for measuring
emissions.
For units with add-on
mercury
8600
controls
that operate
continuously
rather
than seasonally,
or for
units that need
a
8601
dual range to
record high concentration
“spikes”
during startup conditions,
the
8602
low
range
is considered normal.
However,
for
some dual span units
(e.g.,
for
units
8603
that use fuel
switching or
for
which the emission
controls
are
operated
8604
seasonally),
provided that
both monitor ranges
are connected to
a
common probe
8605
and
sample interface, either
of the
two
measurement ranges
may be considered
8606
normal; in such
cases,
perform the RATA
on
the range
that is in use at the
time of
8607
the
scheduled test. If the
low
and
high
measurement
ranges
are connected
to
8608
separate sample probes
and
interfaces,
RATA testing
on
both
ranges
is required.
8609
JCAR350225-08 1 8507r01
8610
)
Record monitor or monitoring system
output from the data acquisition and
8611
handling system.
8612
8613
Complete each single-load relative accuracy test
audit within a period of 168
8614
consecutive unit operating hours, as defined in 40
CFR
72.2, incorporated
by
8615
reference
in
Section
225.140
(or,
for CEMS installed on common stacks or
bypass
8616
stacks,
168 consecutive stack
operating hours, as defined in 40 CFR 72.2,
8617
incorporated by reference in Section 225.140).
Notwithstanding this requirement,
8618
up
to 336
consecutive
unit
or stack operating hours may
be
taken
to
complete
the
8619
RATA of a mercury monitoring
system, when ASTM 6784-02 (incorporated
by
8620
reference in Section
225.140)
or Method 29 in appendix A-8
to
40 CFR
60,
8621
incorporated
by
reference in Section 225.140,
is used as the reference method. For
8622
2-level and 3-level flow monitor RATAs, complete all of the RATAs at all
levels,
8623
to the extent practicable, within a period
of
168 consecutive
unit
(or
stack)
8624
operating hours; however, if this is not possible, up to 720 consecutive unit
(or
8625
stack)
operating hours may be taken to complete
a multiple-load flow RATA.
8626
8627
fi
The status of emission data from the CEMS prior
to and during the RATA test
8628
period must be determined as follows:
8629
8630
For the initial certification
of a CEMS, data from the monitoring system
8631
are considered invalid until all certification
tests, including the RATA,
8632
have been successfully
completed,
unless the conditional
data validation
8633
procedures in Section 1
.4(b’)(3)
of this Appendix are used. When
the
8634
procedures
in Section 1 .4(b)(3) of this Appendix are followed, the words
8635
“initial certification”
apply
instead of”recertification”,
and complete all
of
8636
the initial certification tests
by
January
1, 2009, rather than within
the time
8637
periods
specified
in
Section 1.4(b)(3)(D) of this Appendix for the
8638
individual tests.
8639
8640
For the routine quality assurance RATAs required
by
Section 2.3.1
of
8641
Exhibit B to this Appendix, use the data validation
procedures in Section
8642
2.3.2
of
Exhibit
B to this Appendix.
8643
8644
For
recertification
RATAs, use the data validation procedures in
Section
8645
1
.4(b)(3).
8646
8647
For quality assurance RATAs of non-redundant backup monitoring
8648
systems,
use
the data validation procedures in Section 1 .4(d)(2)(D)
and
(B)
8649
of
this Appendix.
8650
8651
For RATAs performed during and afier the expiration
of a
grace
period,
8652
use the
data
validation
procedures in Sections 2.3.2 and 2.3.3,
JCAR350225-08 1 8507r01
8653
respectively,
of Exhibit B
to this
Appendix.
8654
8655
)
For all
other RATAs,
use the data validation procedures in Section 2.3.2
8656
of
Exhibit B to this Appendix.
8657
8658
g
For each flow monitor, each
2
CO
or
02
diluent
monitor used to
determine
heat
8659
input,
each
moisture
monitoring
system, each mercury concentration monitoring
8660
system, and each sorbent trap monitoring
system, calculate the
relative
accuracy,
8661
in accordance with Section 7.3 of this Exhibit,
as applicable.
8662
8663
6.5.1 Gas and Mercury Monitoring System RATAs
(Special Considerations)
8664
8665
Perform the required relative accuracy test audits
for each CO or
02
diluent
8666
monitor used to determine heat input,
each
mercury concentration monitoring
8667
system, and each sorbent trap monitoring system at the normal load level or
8668
normal operating level for the unit (or
combined units, if common stack), as
8669
defined in Section 6.5.2.1 of this Exhibit. If two load levels or operating levels
8670
have
been designated as normal,
the RATAs may be done at either load level.
8671
8672
For the initial certification of a gas or mercury monitoring system and for
8673
recertifications in which,
in
addition to a RATA, one or more other tests are
8674
required
(i.e.,
a
linearity
test, cycle
time test, or 7-day calibration error test), the
8675
Agency recommends that the RATA not
be
commenced until the other required
8676
tests of the CEMS have been passed.
8677
8678
6.5.2 Flow Monitor
RATAs (Special Considerations)
8679
8680
Except as otherwise
provided
in subsection
(b)
or
(e)
of this Section, perform
8681
relative accuracy test audits for the initial certification
of each flow monitor at
8682
three different exhaust gas velocities
(low,
mid, and
high),
corresponding to
three
8683
different load levels or operating levels within the range of operation,
as defined
8684
in Section
6.5.2.1
of
this Exhibit.
For a common stack/duct, the three different
8685
exhaust gas velocities may be obtained from frequently used unit/load
or
8686
operating
level combinations
for the units exhausting to the common stack. Select
8687
the
three exhaust gas velocities such that the audit points at adjacent load
or
8688
operating levels
(i.e.,
low and mid or mid and
high),
in megawatts
(or
in
8689
thousands of lb/hr of steam
production
or in fl/sec. as applicable), are separated
8690
by
no less than 25.0 percent of the range of operation,
as defined
in
Section
8691
6.5.2.1 of this Exhibit.
8692
8693
i
For
flow monitors on bypass
stacks/ducts and peaking units, the flow monitor
8694
relative accuracy test audits for initial certification
and recertification must be
8695
single-load tests, performed at the normal load,
as
defined in Section
6.5.2.1(d)
of
JCAR350225-081
8507r01
8696
this Exhibit.
8697
8698
Flow monitor
recertification
RATAs must be
done
at three
load levels
(or
three
8699
operating
levels), unless
otherwise specified
in subsection
(b)
or (e) of this
8700
Section
or
unless
otherwise
specified
or approved by the Agency.
8701
8702
ç)
The
semiannual
and annual quality assurance
flow
monitor RATAs required
8703
under Exhibit B to this
Appendix
must be done at the load
levels
(or
operating
8704
levels)
specified
in Section
2.3.1.3
of
Exhibit
B to
this Appendix.
8705
8706
For flow monitors
installed on units
that do not produce
electrical or thermal
8707
output, the flow RATAs
for initial
certification
or
recertification
may
be done
at
8708
fewer than
three
operating levels, if:
8709
8710
j)
The owner
or operator provides
a technical
justification
in the hardcopy
8711
portion of the
monitoring
plan for the unit required
under 40
CFR
8712
75.53(e)(2),
incorporated by reference
in
Section
225.140,
demonstrating
8713
that the unit
operates
at only
one level or two levels
during normal
8714
operation
(excluding
unit startup
and shutdown).
Appropriate
8715
documentation
and data must
be provided
to support the claim
of single-
8716
level or
two-level
operation
and
8717
8718
)
The justification provided
in subsection
(e)(l)
of this Section
is
deemed
to
8719
be acceptable by
the permitting
authority.
8720
8721
6.5.2.1
Range of Operation
and Normal
Load
(or
Operating)
Levels
8722
8723
The
owner or operator
must determine
the upper and lower
boundaries of
the
8724
orange of operation”
as follows for
each
unit (or combination
of units,
for
8725
common
stack configurations):
8726
8727
II
For affected units
that produce
electrical output (in
megawatts) or
thermal
8728
output
(in
lb/hr
of steam production
or
mmBtu/hr),
the lower boundary
of
8729
the range of
operation of a unit
must
be the minimum
safe, stable
loads for
8730
any of the units
discharging through
the stack. Alternatively,
for
a
group
8731
of frequently
operated units that
serve a common
stack, the sum
of the
8732
minimum safe,
stable
loads
for
the individual units
may
be used
as the
8733
lower boundary
of the range
of operation. The
upper boundary
of the
8734
range
of operation of a unit
must
be
the
maximum sustainable
load. The
8735
“maximum
sustainable
load” is the higher of
either:
the
nameplate or rated
8736
capacity
of the unit, less
any physical or
regulatory limitations
or other
8737
deratings; or the highest
sustainable
load, based on at least
four
quarters
of
8738
representative
historical
operating
data. For common
stacks, the
maximum
JCAR350225-08 1 8507r01
8739
sustainable load is
the sum of all
of
the maximum sustainable loads of the
8740
individual units discharging through the stack,
unless this load is
8741
unattainable in
practice, in which
case
use the highest sustainable
8742
combined load for
the units that discharge through the stack.
Based
on at
8743
least
four quarters of representative historical
operating
data.
The load
8744
values for the units must be expressed either in
units of megawatts of
8745
thousands of lb/hr of
steam load
or
mmBtu/hr of thermal output; or
8746
8747
)
For affected units that do not produce
electrical or thermal output, the
8748
lower boundary of
the range
of
operation must be the minimum expected
8749
flue
gas
velocity
(in ft/sec) during normal, stable
operation of the unit.
The
8750
upper boundary of
the range of operation must be the maximum potential
8751
flue gas velocity
(in ft/see)
as defined in Section
2.1.2.1 of this Exhibit.
8752
The minimum
expected and maximum potential
velocities
may be derived
8753
from the results of reference method
testing
or
by
using Equation A-3a
or
8754
A-3b
(as
applicable) in Section 2.1.2.1 of this Exhibit. If
Equation A-3a
or
8755
A-3b is used to determine the
minimum expected velocity, replace the
8756
word
“maximum” with the word “minimum” in the definitions of “MPV,”
8757
i,”
“%O”,
and “%H
2
o” and replace the word
“minimum” with the
8758
word “maximum” in the definition of “COj”.
Alternatively, 0.0 ft/sec may
8759
be used as the
lower boundary of the range of operation.
8760
8761
The operating
levels for relative accuracy test audits will,
except
for peaking
8762
units, be
defined as follows: the “low” operating level
will be the first 30.0
8763
percent
of the range of operation; the “mid”
operating level will be the middle
8764
portion
(>30.0
percent,
but
60.0
percent) of the range of
operation;
and the
8765
“high”
operating level will be the upper end
(>
60.0 percent)
of the range of
8766
operation. For example, if the
upper
and
lower boundaries of the range of
8767
operation are
100 and 1100 megawatts, respectively, then
the low, mid, and
high
8768
operating levels would be 100 to
400 megawatts, 400 to 700 megawatts, and 700
8769
to
1100
megawatts, respectively.
8770
8771
ç)
Units
that do
not produce electrical or thermal output
are exempted from the
8772
requirements of
this subsection
(c).
The owner or operator must identify, for each
8773
affected
unit or common stack, the “normal” load
level
or levels
(low,
mid or
8774
high),
based on the operating
history
of the
units. To identify the normal load
8775
levels, the owner
or operator must, at a minimum, determine the
relative number
8776
of
operating hours at each of the three load levels, low,
mid and high over the
past
8777
four
representative operating quarters. The owner
or operator must determine,
to
8778
the
nearest 0.1 percent, the
percentage
of
the time that each load level
(low,
mid,
8779
high) has been used
during that
time period. A summary of the data used for this
8780
determination and
the
calculated results must be kept on-site in a
format suitable
8781
for
inspection. For new units or newly affected units,
the data analysis in this
JCAR350225-08
1 8507r01
8782
subsection may be based
on
fewer
than
four
quarters
of data if fewer than four
8783
representative
quarters of historical load data
are available. Or,
if no historical
8784
load data are available,
the
owner or operator
may designate the normal load
8785
based on the expected or projected
manner
of operating the
unit. However, in
8786
either case, once four quarters of representative
data become available,
the
8787
historical
load analysis must be repeated.
8788
8789
ci)
Determination of normal load
(or
operating level)
8790
8791
j)
Based on the analysis
of the historical load data
described in subsection
(c)
8792
of this Section, the owner
or operator must, for units that produce
8793
electrical or thermal
output, designate the most
frequently used load level
8794
as the normal load level for the
unit
(or
combination of units, for common
8795
stacks).
The owner or
operator may also designate the
second
most
8796
frequently used load level as
an
additional
normal load level for the
unit or
8797
stack. If the manner
of operation of the unit changes significantly,
such
8798
that the designated normal loads or the
two
most frequently used load
8799
levels change, the
owner or
operator
must repeat
the historical
load
8800
analysis and must redesignate
the normal loads and the two most
8801
frequently used load levels, as appropriate.
A minimum of two
8802
representative
quarters of historical load data
are required to document
8803
that a change in the
manner of unit operation has occurred.
Update the
8804
electronic monitoring
plan
whenever
the normal load levels and
the two
8805
most frequently used load levels
are redesignated.
8806
8807
)
For units that
do not produce electrical or thermal
output, the normal
8808
operating levels must
be determined using sound engineering
judgment,
8809
based
on knowledge of the unit and operating
experience with
the
8810
industrial process.
8811
8812
ç)
The owner or operator must report the
upper and lower boundaries of the range
of
8813
operation for each
unit
(or
combination of units, for common
stacks),
in units
of
8814
megawatts or thousands of lb/hr or mniBtu/hr
of steam production or fl/sec
(as
8815
applicable), in the electronic
monitoring plan required under
Section 1.10 of this
8816
Appendix.
8817
8818
6.5.2.2 Multi-Load
(or
Multi-Level) Flow RATA Results
8819
8820
For each
multi-load
(or multi-level)
flow RATA, calculate
the flow monitor relative accuracy
at
8821
each
operating
level.
If a
flow monitor
relative accuracy test is failed
or aborted due to a problem
8822
with
the
monitor on any level of a 2-level
(or
3-level) relative accuracy test
audit, the RATA
8823
must
be
repeated at that load
(or
operating)
level.
However, the entire 2-level (or 3-level)
relative
8824
accuracy
test audit does not
have
to be repeated
unless
the
flow monitor polynomial coefficients
JCAR350225-081
8507r01
8825
or K-factors
are changed,
in
which
case a 3-level RATA is required
(or,
a 2-level RATA,
for
8826
units demonstrated to operate at only two levels, under Section
6.5.2(e)
of this Exhibit).
8827
8828
6.5.3
Calculations
8829
8830
Using the data from the relative accuracy test audits, calculate
relative accuracy and bias in
8831
accordance
with
the procedures and equations specified in Section
7 of this
Exhibit.
8832
8833
6.5.4 Reference Method Measurement
Location
8834
8835
Select
a
location for reference method measurements
that
is
(1)
accessible; (2) in the same
8836
proximity as the monitor or monitoring system location; and
(3)
meets the requirements
of
8837
Performance Specification 3 in appendix B of 40 CFR
60,
incorporated
by reference in Section
8838
225.140, for CO
2or
02
monitors,
or Method 1 (or
1A)
in appendix A of 40 CFR 60, incorporated
8839
by
reference
in Section 225.140, for volumetric flow, except as
otherwise indicated in this
8840
Section or as approved by
the Agency.
8841
8842
6.5.5 Reference Method Traverse Point Selection
8843
8844
Select
traverse points that ensure acquisition of representative samples
of
pollutant
and diluent
8845
concentrations, moisture content, temperature, and flue gas flow rate over the flue cross
Section.
8846
To
achieve this, the reference method
traverse
points must meet the requirements of Section
8847
8.1.3 of Performance
Specification 2 (“PS
No.
2”)
in appendix B to 40 CFR 60, incorporated
by
8848
reference in Section
225.140
(for
moisture monitoring
system
RATAs),
Performance
8849
Specification 3
in appendix B to 40 CFR 60, incorporated
by
reference
in
Section 225.140
(for
8850
Q
and C0
monitor
RATAs),
Method 1
(or 1A) (for
volumetric
flow rate monitor RATAs),
8851
Method 3
(for
molecular
weight),
and Method 4
(for
moisture determination) in appendix
A to
8852
40 CFR 60,
incorporated
by reference in Section 225.140. The following alternative
reference
8853
method traverse point
locations are permitted for
moisture and gas monitor RATAs:
8854
8855
For
moisture determinations where
the moisture data are used only to determine
8856
stack gas molecular weight, a single reference method point, located at least
1.0
8857
meter from the stack wall, may be
used.
For
moisture
monitoring system RATAs
8858
and for gas monitor
RATAs
in which moisture data are used to correct
pollutant
8859
or
diluent concentrations from a dry
basis to a wet basis (or
vice-versa),
single-
8860
point moisture sampling may only be used if the 12-point stratification
test
8861
described
in Section
6.5.5.1
of this Exhibit is performed prior to the RATA
for at
8862
least
one pollutant or diluent gas,
and
if the
test is passed according to the
8863
acceptance criteria in Section
6.5.5.3(b)
of this Exhibit.
8864
8865
]
For gas monitoring
system
RATAs, the owner or operator may use any of the
8866
following
options:
8867
JCAR350225-081 8507r01
8868
j
At any location (including locations where
stratification is expected), use a
8869
minimum of six
traverse points along a diameter, in the direction of
any
8870
expected stratification. The
points must be located in accordance with
8871
Method 1 in appendix A to 40 CFR 60, incorporated
by
reference
in
8872
Section
225.140.
8873
8874
)
At locations where Section
8.1.3 of PS No. 2 allows the use of a short
8875
reference method measurement line
(with
three
points located
at
0.4,
1.2,
8876
and
2.0 meters
from the stack wall), the owner or operator may use
an
8877
alternative 3-point measurement line,
locating the three points at 4.4, 14.6,
8878
and
29.6
percent of the way across the stack, in accordance with Method
1
8879
in
appendix A to 40 CFR
60,
incorporated
by reference in Section
8880
225.140.
8881
8882
)
At locations
where stratification is likely to occur (e.g., following a wet
8883
scrubber or when dissimilar gas streams are
combined),
the short
8884
measurement line
from Section 8.1.3 of PS No.
2
(or the alternative line
8885
described in subsection
(b)(2)
of this Section) may
be
used in lieu
of the
8886
prescribed
“long” measurement line in Section 8.1.3 of PS No. 2, provided
8887
that the 12-point stratification
test
described
in Section 6.5.5.1 of this
8888
Exhibit is performed and passed one time
at the location (according to the
8889
acceptance criteria of Section
6.5.5.3(a)
of this
Exhibit)
and provided
that
8890
either the 12-point stratification test or the alternative (abbreviated)
8891
stratification
test in Section 6.5.5.2 of this Exhibit is performed and
passed
8892
prior to each
subsequent RATA at the location (according to the
8893
acceptance criteria of Section 6.5.5.3(a) of this Exhibit).
8894
8895
4
A single reference method measurement
point, located no
less
than 1.0
8896
meter from the stack wall and situated along one of the measurement
lines
8897
used for the stratification
test,
may be
used at any
sampling location
if the
8898
12-point
stratification test described in Section 6.5.5.1 of this Exhibit
is
8899
performed and passed prior to each RATA
at
the location (according
to the
8900
acceptance criteria
of Section 6.5.5.3(b) of this Exhibit).
8901
8902
çj
For
mercury monitoring
systems, use the same basic approach for traverse
point
8903
selection that is used for the other
gas
monitoring
system RATAs, except that the
8904
stratification test provisions in Sections 8.1.3
through
8.1.3.5 of Method
3 OA must
8905
apply, rather
than
the provisions
of Sections 6.5.5.1 through 6.5.5.3 of this
8906
Exhibit.
8907
8908
6.5.5.1 Stratification Test
8909
8910
With the units
operating under
steady-state conditions at the normal load level
(or
JCAR350225-081 8507r01
8911
normal operating level),
as
defined
in Section 6.5.2.1 of this Exhibit, use a
8912
traversing
gas sampling probe to measure diluent
(CO2
or
02)
concentrations
at
a
8913
minimum of 12 points, located
according to Method 1 in appendix A to 40
CFR
8914
60, incorporated by reference in Section 225.140.
8915
8916
j
Use
Method
3A in appendix A to 40 CFR 60, incorporated
by
reference in
8917
Section 225.140, to make
the measurements. Data from the reference method
8918
analyzers must be quality assured
by
performing
analyzer calibration error and
8919
system
bias
checks before the series of measurements and
by
conducting
system
8920
bias and
calibration drift checks
after
the measurements, in accordance with the
8921
procedures of Method 3A.
8922
8923
c
Measure for a minimum of 2 minutes at each traverse point. To the extent
8924
practicable, complete the traverse within
a
2-hour period.
8925
8926
)
If the load has remained constant
(±
3.0
percent)
during
the traverse and if the
8927
reference method analyzers
have
passed all of the required quality assurance
8928
checks, proceed with the data analysis.
8929
8930
ç)
Calculate
the average
CO2
(or 02)
concentrations at each of the individual
8931
traverse
points.
Then, calculate
the
arithmetic
average
CO
2
(or
02)
concentrations
8932
for all traverse points.
8933
8934
6.5.5.2 Alternative
(Abbreviated) Stratification Test
8935
8936
With the units operating under steady-state
conditions at the normal load level
(or
8937
normal operating
level),
as defined in Section 6.5.2.1 of this Exhibit,
use a
8938
traversing gas sampling
probe
to measure the diluent
(CO2
or
02)
concentrations
8939
at three points. The points must be located according
to
the specifications
for the
8940
long
measurement line in Section
8.1.3 of PS No. 2 (i.e., locate the points 16.7
8941
percent, 50.0
percent,
and 83.3 percent of the way across the
stack).
Alternatively,
8942
the
concentration measurements may be
made
at six traverse points along a
8943
diameter. The
six points
must be located in accordance with Method 1 in
8944
appendix A to 40 CFR 60, incorporated
by reference in Section 225.140.
8945
8946
Use
Method 3A in appendix A
to
40
CFR 60, incorporated by reference in
8947
Section 225.140, to make the measurements.
Data from the reference method
8948
analyzers must be
quality
assured
by performing analyzer calibration error
and
8949
system
bias checks before
the series of measurements and
by
conducting
system
8950
bias
and
calibration drift checks
after the measurements, in accordance with
the
8951
procedures
of Method 3A.
8952
8953
c
Measure
for a
minimum
of 2 minutes at each traverse point. To the extent
JCAR350225-081 8507r01
8954
practicable, complete
the traverse within
a 1-hour period.
8955
8956
If the load has
remained
constant
(±
3.0
percent)
during the traverse and if the
8957
reference method analyzers
have
passed all of the required
quality assurance
8958
checks, proceed with the data
analysis.
8959
8960
Calculate the
average
CO2
(or
02)
concentrations
at each of the individual
8961
traverse points. Then,
calculate the arithmetic average
CO2
(or
02)
concentrations
8962
for all traverse points.
8963
8964
6.5.5.3 Stratification
Test Results and Acceptance Criteria
8965
8966
For each diluent gas, the
short reference method measurement line described
in
8967
Section
8.1.3 of PS No. 2 maybe used in lieu of the long
measurement line
8968
prescribed in Section 8.1.3
of PS No.
2
if the results of a stratification test,
8969
conducted in accordance
with Section 6.5.5.1 or 6.5.5.2
of
this Exhibit
(as
8970
appropriate see Section
6.5.5(b)(3)
of this Exhibit), show that the concentration
at
8971
each
individual
traverse
point
differs by no more
than
±
10.0 percent from the
8972
arithmetic average concentration
for all traverse points. The results are also
8973
acceptable if the concentration
at
each individual
traverse
point differs by no
more
8974
than
+
Sppm or
±
0.5 percent
CO2
(or
02)
from
the arithmetic average
8975
concentration
for all traverse
points.
8976
8977
For
each diluent gas,
a single reference method measurement point, located
at
8978
least 1.0 meter from the stack wall
and situated along one of the measurement
8979
lines used for the stratification test, may be used for
that diluent gas if the results
8980
of a
stratification test,
conducted in accordance with Section 6.5.5.1 of
this
8981
Exhibit, show that the concentration at each
individual traverse point differs
by no
8982
more
than
±
5.0
percent from the arithmetic average concentration for
all traverse
8983
points. The results are also acceptable if the
concentration at each individual
8984
traverse point differs
by no more than
±
3 ppm or
±
0.3 percent
CO2
(or
0)
from
8985
the arithmetic average concentration for all traverse
points.
8986
8987
The owner or operator must keep the results of
all stratification tests on-site, in
a
8988
format suitable for inspection,
as part of the supplementary RATA records
8989
required under Section 1.1
3(a)(7)
of this Appendix.
8990
8991
6.5.6 Sampling Strategy
8992
8993
Conduct the reference method tests
so
they
will yield results representative
of the
8994
pollutant concentration,
emission rate, moisture, temperature,
and flue gas flow
8995
rate
from the unit
and can be correlated with the pollutant concentration
monitor,
8996
CO
2
or
02
monitor,
flow
monitor, and mercury CEMS measurements. The
JCAR350225-081 8507r01
8997
minimum acceptable
time
for a gas monitoring
system
RATA run or for a
8998
moisture monitoring system RATA run is 21 minutes.
For each run of a gas
8999
monitoring
system
RATA, all necessary
pollutant concentration measurements,
9000
diluent concentration measurements, and moisture measurements
(if
applicable)
9001
must, to the extent practicable, be made within a
60-minute
period.
For
flow
9002
monitor RATAs, the minimum time per run must be 5
minutes. Flow rate
9003
reference method measurements may
be made either sequentially from port to
9004
port
or
simultaneously at two or more sample ports. The
velocity
measurement
9005
probe may be moved from traverse point to
traverse
point
either manually or
9006
automatically. If, during a
flow RATA, significant pulsations in the reference
9007
method readings are observed, be sure to allow enough
measurement time at
each
9008
traverse point to
obtain
an
accurate average reading when a manual readout
9009
method is used (e.g., a “sight-weighted”
average
from a
manometer).
Also, allow
9010
sufficient
measurement time to ensure that stable temperature readings are
9011
obtained at each traverse point, particularly at
the first measurement point at each
9012
sample
port, when a probe is moved sequentially from port-to-port.
A minimum
9013
of one set of auxiliary measurements for
stack gas molecular weight
9014
determination (i.e., diluent gas data and moisture data) is required for every clock
9015
hour
of a flow RATA or for every three test runs
(whichever is less restrictive).
9016
Alternatively,
moisture
measurements
for
molecular weight determination may
be
9017
performed before and
after a series of flow RATA runs at a particular load level
9018
(low,
mid, or
high), provided that the time interval between the two moisture
9019
measurements does not exceed three hours. If this option is
selected, the results
of
9020
the two
moisture determinations must be averaged
arithmetically
and applied
to
9021
all
RATA runs in the series. Successive
flow RATA runs may be performed
9022
without waiting
in-between runs. If an 20
-diluent monitor is used as a CO
2
9023
continuous
emission monitoring system, perform a CO2system
RATA (i.e.,
9024
measure
CO
2.
rather than
02,
with the reference
method).
For moisture
9025
monitoring
systems, an appropriate coefficient, “K” factor
or other suitable
9026
mathematical algorithm
may
be developed prior to the RATA, to
adjust
the
9027
monitoring
system readings with respect to the reference
method. If such a
9028
coefficient,
K-factor or algorithm is developed, it must be applied to the CEMS
9029
readings
during
the RATA and
(if
the RATA is passed), to
the subsequent
CEMS
9030
data, by means of
the automated data acquisition and handling system. The owner
9031
or
operator must keep records of the current coefficient, K
factor
or algorithm,
as
9032
specified in Section 1
.13(a)(5)(F)
of
this Appendix. Whenever the coefficient, K
9033
factor or
algorithm is changed, a RATA of the moisture monitoring system is
9034
required. For the RATA of a mercury CEMS using the Ontario
Hydro Method,
or
9035
for
the RATA of a sorbent
trap
system
(irrespective
of
the reference method
9036
used),
the time per
run must be long enough to collect a sufficient mass of
9037
mercury to
analyze. For the RATA of a sorbent
trap
monitoring system, the type
9038
of
sorbent material used by the traps must be the same as for daily operation of
9039
the
monitoring system;
however,
the size of the traps used
for the RATA maybe
JCAR350225-08
1 8507r01
9040
smaller
than the traps used for daily
operation of the system. Spike
the third
9041
section of each sorbent trap
with elemental mercury,
as
described
in Section 7.1.2
9042
of Exhibit D to this Appendix. Install
a new pair of sorbent traps
prior to each test
9043
run.
For each run, the sorbent trap
data must be validated according
to the quality
9044
assurance criteria in
Section 8 of Exhibit
D
to this Appendix.
9045
9046
)
To properly correlate individual
mercury CEMS data
(in
lb/mmBtu)
and
9047
volumetric flow
rate data with the
reference method data, annotate the
beginning
9048
and end of each reference
method test run (including
the
exact
time of
day)
on
the
9049
individual chart recorders
or other pennanent recording devices.
9050
9051
6.5.7 Correlation of Reference Method
and Continuous Emission Monitoring
System
9052
9053
Confirm that the
monitor
or monitoring system and reference
method test results are
on
9054
consistent
moisture,
pressure, temperature,
and diluent concentration basis
(e.g.,
since the flow
9055
monitor measures
flow rate
on a wet basis, Method 2
test results must also be on a wet basis).
9056
Compare
flow-monitor and reference
method
results on a scfh basis. Also, consider
the response
9057
times of the pollutant concentration monitor, the
continuous emission monitoring
system, and the
9058
flow monitoring
system to ensure
comparison of simultaneous measurements.
9059
9060
For each
relative accuracy test audit run, compare
the measurements obtained from
the monitor
9061
or continuous emission monitoring system
(in
ppm, percent CO
2.lb/mmBtu, or other units)
9062
against the
corresponding reference
method
values. Tabulate the
paired data in a table such
as the
9063
one shown in
Figure 2.
9064
9065
6.5.8
Number of Reference
Method Tests
9066
9067
Perform a
minimum of nine sets of paired monitor
(or
monitoring
system) and
reference method
9068
test data for every
required
(i.e.,
certification, recertification, diagnostic,
semiannual,
or annual)
9069
relative
accuracy
test audit. For 2-level and
3-level relative accuracy test audits
of flow monitors,
9070
perform a minimum of
nine
sets at each of the operating levels.
9071
9072
6.5.9 Reference Methods
9073
9074
The
following
methods are from
appendix A to 40 CFR
60,
incorporated
by reference in Section
9075
225.140, or
have been published by ASTM,
and
are
the reference methods for
performing
9076
relative
accuracy test
audits
under this part: Method 1
or 1A in appendix A-i to 40 CFR
60 for
9077
siting;
Method 2 in
appendices A-i
and A-2 to 40 CFR
60
or its allowable
alternatives
in
9078
appendix A to
40 CFR 60
(except
for
Methods 2B and 2E in appendix
A-l to 40 CFR
60)
for
9079
stack gas
velocity and volumetric flow rate; Methods
3, 3A or 3B in appendix A-2
to
40
CFR
60
9080
for
02
and
2
CQ;
Method
4
in appendix A-3 to 40 CFR
60 for moisture; and for mercury,
either
9081
ASTM
D6784-02
(the
Ontario
Hydro
Method) (incorporated
by reference under Section
9082
225.140),
Method
29 in appendix A-8
to
40
CFR 60, Method
30A,
or
Method 30B.
JCAR350225-08 1 8507r01
9083
9084
7. Calculations
9085
9086
7.1 Linearity Check
9087
9088
Analyze
the
linearity
data for pollutant concentration monitors as follows. Calculate the
9089
percentage error in linearity based
upon the
reference value
at the
low-level,
mid-level,
and high-
9090
level concentrations specified in Section 6.2 of this Exhibit. Perform this calculation
once during
9091
the certification test. Use the following equation to calculate the error in linearity for each
9092
reference
value.
9093
9094
LE
=
R
x
100
(Equation
A-4)
9095
9096
Where:
9097
LE
= Percentage linearity error, based upon the reference value.
R
= Reference value
of
low-, mid-,
or high-level
calibration
gas
introduced
into
the monitoring system.
A
= Average of the monitoring
system
responses.
9098
9099
7.2
Calibration Error
9100
9101
7.2.1 Pollutant Concentration and Diluent Monitors
9102
9103
For
each reference value,
calculate the percentage calibration
error based upon instrument span
9104
for daily
calibration error tests using the following equation:
9105
jR-A
9106
CE=
xlOO
(EquationA-5)
9107
9108
Where:
9109
Calibration error as a percentage of the span of the instrument.
R
= Reference value of zero or upscale
(high-level
or mid-level, as
applicable)
calibration gas introduced into the monitoring system.
A
= Actual monitoring system response to the calibration gas.
S
= Span of the instrument, as
specified
in
Section 2 of this Exhibit.
9110
9111
7.2.2 Flow
Monitor Calibration Error
9112
1CAR350225-08 1 8507r01
9113
For
each reference value, calculate
the percentage calibration
error based upon span using
the
9114
following equation:
9115
9116
CE=
xlOO
(EquationA-6)
9117
9118
Where:
9119
CE
= Calibration
error as a percentage
of span.
R
Low or high level
reference value specified in Section 2.2.2.1
of this Exhibit.
A
= Actual flow monitor
response to the reference value.
S
= Flow monitor calibration
span value as determined under Section 2.1.2.2
of
this Exhibit.
9120
9121
7.3
Relative Accuracy for
02
Monitors,
Mercury
Monitoring Systems,
and
Flow Monitors
9122
9123
Analyze
the
relative accuracy
test audit data
from the reference
method
tests for
CO2
or
02
9124
monitors
used
only
for heat input rate
determination, mercury monitoring systems
used to
9125
determine mercury mass emissions under
Sections 1.14 through 1.18 of Appendix B,
and flow
9126
monitors using the following procedures. Summarize
the results on a data sheet. An example
is
9127
shown in Figure 2. Calculate the mean of the monitor
or monitoring system measurement values.
9128
Calculate the mean of
the reference
method values. Using data from
the automated data
9129
acquisition and
handling system, calculate
the arithmetic differences between
the reference
9130
method
and monitor measurement data sets.
Then calculate the arithmetic mean of the
9131
difference, the
standard deviation,
the confidence coefficient, and
the monitor or monitoring
9132
system relative
accuracy using the following
procedures and equations.
9133
9134
7.3.1 Arithmetic Mean
9135
9136
Calculate the
arithmetic mean of the differences,
d, of a data set as follows.
9137
9138
d=d1 (EquationA-7)
9139
9140
Where:
9141
n
Number of data points.
= The difference between
a reference method value and
the corresponding
continuous
emission
monitoring
system value (RM-
CEMI)
at
a given point in
time i.
9142
CN
ucju
1
C
•
•
Ccoo
•
-
4444
C.LM4
I
I
LQ-
I
lCD
iii
iii
IF’
C-.
C
C
CD
c,)
CD
CD
H
CD
CD
D
D”CD
•
•
Ul
u
N
C-)
C)
CD
CD
C)
C
CD
C)
CD
C)
C
CD
C)
C)
II
CD
p
0
C
D
C-)
C
C)
C)
I
H
C
(ID
LJ’
9
CCOoC—
C
CHU
1
——
—
————
—
I
I—
JJ
C
•
I-
•
:
CC4
:
CC
U1
C
D
LI.)
t’Jt’Jt’J
tJ
JJJ
CCCCCCCC
NCNC)
C
NC4C
H
CD
CD
C-)
C)
CD
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CD
C/)
—
CD
C
C
C,)
CD
Cl)
C
I
I
I
IC
I
C
-‘CD
-t
—.
-t
CD
C
)
-
C
(I)
CD
It)
CD
c
-C)
)
CD
-*
CD
c
C
.c
CD
C
C
CCD
j•)
SQ
C/DC)
CD
-t
CD
CD
-
-t
.C
CDQ
-
—
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C
C)
I
1CAR350225-081
8507r01
9
2.262
20
2.086
40
2.021
10
2.228
21
2.080
60
2.000
11
2.201
22
2.074
>60
1.960
9161
9162
7.3.4
Relative Accuracy
9163
9164
Calculate the
relative
accuracy
of a data set using
the
following equation.
9165
9166
RA—
xlOO
(Equation A-b)
RM
9167
9168
Where:
9169
= Arithmetic
mean of the reference method
values.
= The absolute
value of the mean difference
between the reference method
values and the
corresponding continuous emission monitoring
system
values.
cc
The absolute value of the confidence
coefficient.
9170
9171
7.4 Bias Test
9172
9173
Test
the following
relative
accuracy test audit data sets for
bias: flow
monitors, mercury
9174
concentration
monitoring
systems,
and sorbent trap monitoring systems,
using the procedures
9175
outlined
in Sections 7.4.1 through 7.4.4 of this Exhibit.
For multiple-load flow RATAs,
perform
9176
a
bias test at each load
level designated
as normal under Section 6.5.2.1
of this Exhibit.
9177
9178
7.4.1 Arithmetic Mean
9179
9180
Calculate the
arithmetic mean of the difference,
“d”, of the data set using Equation
A-7 of this
9181
Exhibit. To
calculate bias for a flow monitor,
I?dH
is, for
each
paired data point, the difference
9182
between the
flow rate values
(in
scth)
obtained from the reference method
and the monitor. To
9183
calculate bias
for a mercury monitoring system when
using the Ontario Hydro Method
or
9184
Method 29 in
appendix A-8 to 40
CFR 60, incorporated
by
reference
in Section 225.140, “d”
is,
9185
for
each data
point, the difference between
the average mercury concentration value
(in ig/m
3)
9186
from the
paired Ontario Hydro or Method 29
in appendix A-8 to 40 CFR 60 sampling
trains and
9187
the
concentration measured by the monitoring system.
For sorb ent trap monitoring systems,
use
9188
the
average
mercury concentration
measured by the
paired
traps
in the calculation of
“d”.
9189
9190
7.4.2
Standard
Deviation
9191
JCAR350225-08 1 8507r01
9192
Calculate the standard
deviation,
Sd,
of the data set using Equation A-8.
9193
9194
7.4.3 Confidence Coefficient
9195
9196
Calculate the
confidence coefficient,
cc, of the data set using Equation A-9.
9197
9198
7.4.4 Bias Test
9199
9200
If, for the relative
accuracy
test
audit data set being tested, the mean
difference, d, is less than
or
9201
equal to
the absolute value of the confidence coefficient, cc, the monitor or monitoring system
9202
has passed
the bias test. If the mean difference, d, is greater than the absolute value of the
9203
confidence coefficient,
cc, the monitor
or
monitoring
system has
failed to meet the bias test
9204
requirement.
9205
9206
7.5 Reference Flow-to-Load Ratio or Gross Heat Rate
9207
9208
Except
as provided
in Section 7.6 of this Exhibit,
the owner or operator must
9209
determine R, the reference value of the ratio of flow rate to unit load, each time
9210
that a passing flow RATA is performed at a load level designated as normal in
9211
Section 6.5.2.1 of this Exhibit. The owner or operator
must report the current
9212
value of
in
the electronic
quarterly report required under 40 CFR 75.64,
9213
incorporated
by
reference
in
Section 225.140, and must also report the completion
9214
date of the associated RATA. If two load levels have been designated as normal
9215
under Section 6.5.2.1 of this Exhibit, the owner or operator must
determine
a
9216
separate
Rvalue
for each of the
normal
load
levels. The
reference flow-to-load
9217
ratio
must be calculated as follows:
9218
ref
-5
9219
Rref___X1O
(EquationA-13)
avg
9220
9221
Where:
9222
= Reference value of the flow-to-load
ratio, from the most recent
normal-load flow RATA, scfhlmegawatts, scthll000 lb/hr of steam,
or
scthl
(mmBtu/hr
of steam output).
= Average stack gas volumetric flow rate measured by
the
reference
method during the
normal-load
RATA,
scth.
L
= Average unit
load
during the normal-load flow RATA, megawatts,
1000
lb/hr of steam, or mmBtu/hr of thermal output.
9223
9224
Tn
Equation A-13, for a common stack, determine L
by
summing, for each
JCAR350225-08 1 8507r01
9225
RATA run, the operating loads
of all units discharging through the common
stack,
9226
and
then taking
the arithmetic average
of
the
summed
loads. For a
unit that
9227
discharges its emissions
through
multiple
stacks, either determine a single value
9228
pfQ
for the unit or a separate value
of
0
for each stack. In the former case,
9229
calculate
Q
by summing, for each
RATA run, the
volumetric
flow rates through
9230
the
individual
stacks and then taking the arithmetic average of the
summed RATA
9231
run flow rates. In the
latter case, calculate the value of
O
for each stack
by
9232
taking the arithmetic average, for
all RATA runs, of the flow rates through
the
9233
stack. For
a
unit with
a multiple stack discharge configuration consisting
of a
9234
main stack and a bypass
stack (e.g., a unit with a wet
SO
2
scrubber),
determine
9235
Q
separately
for each stack at the time
of the normal load flow RATA. Round
9236
off the value of R
to two decimal places.
9237
9238
In addition to determining Ror
as an alternative to determine R, a reference
9239
value of the
gross heat rate (GHR) may be determined. In order to use
this option,
9240
quality assured diluent
gas
(Q2
or
02)
must be available for each hour of the
9241
most recent normal-load
flow RATA. The reference value of the GHR
must be
9242
determined as follows:
9243
HeatInput)
9244
(GHR)reJ
=L
avg
xl000
(Equation
A-13a)
avg
9245
9246
Where:
9247
(GHR
= Reference value of the gross heat rate
at the time of the
most recent normal-load flow RATA, Btu/kwh,
Btu/lb
steam load,
or
Btu heat input/mmBtu steam output.
(HeatInput) = Average hourly
heat input during the normal-load flow
RATA, as determined using the applicable
equation
in
Exhibit
C
to this Appendix,
mmBtu/hr. For multiple stack
configurations, if the reference GHR value is determined
separately for each stack, use
the
hourly
heat input
measured
at each stack. If the reference GHR is
determined
at the unit level,
sum
the hourly
heat inputs measured at
the
individual stacks.
= Average unit load during the normal-load
flow RATA,
megawatts, 1000 lb/hr of steam, or mmBtu/hr
thermal
output.
9248
9249
In the calculation of
(HeatInput),
use
Q,
the average
volumetric
flow rate
9250
measured by the reference method during the RATA,
and
use
the
average diluent
9251
gas concentration
measured during the flow RATA
(i.e.,
the arithmetic
average of
JCAR350225-08
1 8507r01
9252
the diluent gas concentrations
for all clock hours in which
a RATA
run was
9253
performed).
9254
9255
7.6 Flow-to-Load Test Exemptions
9256
9257
For
complex
stack configurations (e.g., when
the effluent from a unit is divided
9258
and discharges
through multiple stacks in such
a
manner
that the
flow
rate in the
9259
individual
stacks cannot be
correlated with unit
load),
the owner or operator
may
9260
petition
the USEPA under 40 CFR 75.66,
incorporated by reference in Section
9261
225.140, for an
exemption from the requirements
of
Section
7.7
to
Appendix A to
9262
40
CFR Part 75 and Section 2.2.5
of Exhibit B to Appendix B. The petition must
9263
include sufficient information
and data to demonstrate that
a
flow-to-load
or gross
9264
heat
rate evaluation is infeasible for the
complex stack configuration.
9265
9266
k
Units that
do not produce electrical output
(in
megawatts)
or thermal output (in
lb
9267
of steam per
hour)
are exempted
from the flow-to-load ratio test requirements
of
9268
Section
7.5 of this Exhibit and Section 2.2.5 of
Exhibit
B
to
Appendix
B.
9269
Figure 1. Linearity Error
Dietermination
Percent
of
Date and
Reference
Monitor
reference
time
value
value
Difference
value
Low-level:
Mid-level:
High-level:
JCAR350225-081
8507r01
9270
9271
Figure 2. Relative Accuracy
Determination
(Pollutant
Concentration
Monitors)
SQ2
(ppm
FFNc1)
cQ2
(Pollutant)
(ppm
[FNc1)
Run
and
RM
M
and
RM
M
NL
time
[FNa1
FFNb]
Diff
time
[FNaJ
FFNb1
Diff
1
2
3
4
5
6
7
8
9
10
11
12
Arthmetic
Mean Difference
(Eci.
A-7).
Confidence
Coeffecient
(Eq. A-9).
Relative
Accuracy
(Eq.
A-b).
JCAR35O225O81
8507r01
FFNa1
RM
means “reference
method data”.
FFNb1
M means “monitor data”.
FFNc1
Make sure
the
RM
and M data are on
a
consistent
basis, either wet or dry.
9272
9273
Figure 3. Relative Accuracy Determination
(Flow Monitors)
Flow rate (Low)
Flow rate
(Normal)
Flow rate (High)
(scf/hr)
[FNa]
(scflhr)
[FNa]
(scf/hr)
[FNa]
Date
Date
Date
time
time
RM
M
Diff time RM
M
Diff time RM
M Diff
1
2
3
4
5
6
7
8
9
10
11
12
Arthinetic
Mean Difference
(Eq. A-7).
Confidence
Coeffecient (Eq. A-9).
Relative Accuracy
(Eq. A-b).
[FNa1
Make sure the RM and M
data are on a consistent basis, either wet or dry.
JCAR350225-081 8507r01
9274
9275
Figure 4. Relative Accuracy Determination
(NO/Dilent
Combined
System)
Reference
method data
NO
system
(lb/mrnBtu)
Run
Date
N and time
NQXQ
[FNa]
Q2/Q2%
RM
M
Difference
1
2
3
4
5
6
7
8
9
10
11
12
Arthmetic Mean Difference
(Eq.
A-7).
Confidence Coeffecient
(Eq.
A-9).
Relative Accuracy
(Eq.
A-
10).
{FNa1
Specify
units:
ppm, lb/dscf,
mgjdscm.
9276
9277
Figure
5. Cycle Time
Date of test
JCAR350225-08 1 8507r01
Component/system
ID#:
Analyzer type
Serial Number
High level gas
concentration:
ppml%
(circle one)
Zero level gas
concentration:
ppm/%
(circle one)
Analyzer span setting:
ppm/% (circle one)
Upscale:
Stable
starting monitor value:
ppml%
(circle
one)
Stable
ending monitor reading:
ppm/%
(circle one)
Elapsed
time:
Seconds
Downscale:
Stable starting
monitor value:
ppi%
(circle one)
Stable
ending monitor reading:
ppml%
(circle
one)
Elapsed time:
seconds
Component
cycle time =
seconds
System
cycle time
seconds
9278
9279
A.
To detennine
the upscale cycle time
(Figure
6a),
measure the flue gas
emissions
until
9280
the response
stabilizes. Record the stabilized value
(see
Section
6.4
of
this Exhibit
for the
9281
stability
criteria).
9282
9283
B.
Inject a high-level
calibration
gas
into the port leading to the calibration
cell
or thimble
9284
(Point
B).
Allow the analyzer to stabilize. Record the stabilized
value.
9285
9286
C.
Determine
the
step change. The step change is equal to the
difference between the
9287
final
stable calibration gas value (Point
D)
and the
stabilized stack emissions value
(Point
9288
9289
9290
D. Take 95%
of the step change value and add the result to the
stabilized stack emissions
9291
value
(Point A). Determine the time at
which
95%
of the
step
change occurred
(Point
C).
9292
9293
E. Calculate
the upscale cycle time by
subtracting the time at which the calibration gas
9294
was
injected (Point B)
from the time at which 95% of the step change
occurred
(Point
C).
9295
In
this
example,
upscale cycle time
= (11-5)
6 minutes.
9296
9297
F. To
determine the downscale cycle
time (Figure
6b)
repeat the procedures above,
9298
except
that
a zero gas is
injected when the flue gas emissions have stabilized, and 95% of
9299
the
step
change
in
concentration is subtracted from the stabilized stack
emissions value.
9300
9301
G. Compare
the upscale and downscale
cycle
time
values. The longer of these two times
9302
is the cycle time for the analyzer.
9303
JCAR350225-081 8507r01
JCAR350225-081 8507r01
Develop and implement
a
quality
assurance/quality control (QA/QC) program
for the continuous
emission monitoring systems and
their components. At a minimum, include in each
QA/QC
program a written plan that describes in detail (or that
refers
to separate documents containing)
complete, step-by-step
procedures and operations for each
of
the
following
activities.
Upon
request from regulatory authorities,
the source must make all
procedures,
maintenance records,
and
ancillary supporting documentation from the manufacturer
(e.g., soflware coefficients and
troubleshooting diagrams) available
for
review
during an audit. Electronic storage
of the
information in the
OAIQC
plan is permissible, provided
that the information can be made
available
in hardcopy upon request
during an audit.
1.1 Requirements
for All Monitoring
Systems
1.1.1 Preventive
Maintenance
Keep a written
record of procedures
needed
to maintain the
mnnitcrn a
system
in proper
operating
condition and a schedule for those procedures.
This must, at a minimum, include
procedures specified by the manufacturers of the
equipment and, if applicable, additional or
alternate procedures
developed
for the equipment.
1.1.2
Recordkeeping and Reporting
Keep a
written record describing procedures that will be
used to implement the recordkeeping
and reporting
requirements
in subparts E and
G
of 40 CFR 75, incorporated
by
reference
in
Section
225.140, and Sections 1.10 through 1.13
of Appendix B, as applicable.
1.1.3 Maintenance
Records
Keep a
record of all testing, maintenance, or repair activities
performed on any monitoring
system or
component in
a
location
and
format
suitable for inspection. A maintenance log
may
be
used for
this purpose. The following records should be
maintained: date, time, and description
of
any
testing,
adjustment, repair,
replacement,
or preventive maintenance action performed
on any
monitoring
system and records of any corrective
actions associated with a monitor’s outage
period. Additionally, any
adjustment
that recharacterizes a system’s
ability to record and report
emissions
data
must be recorded (e.g.,
changing of flow monitor or moisture monitoring
system
polynomial
coefficients, K factors or mathematical
algorithms, changing of temperature
and
pressure
coefficients and dilution ratio settings), and
a written explanation of the procedures
used
to make
the adjustments must be kept.
Exhibit B to
Appendix
B — Quality Assurance and Quality
Control Procedures
1. Quality Assurance/Quality
Control Program
9304
9305
9306
9307
9308
9309
9310
9311
9312
9313
9314
9315
9316
9317
9318
9319
9320
9321
9322
9323
9324
9325
9326
9327
9328
9329
9330
9331
9332
9333
9334
9335
9336
9337
9338
9339
9340
9341
9342
9343
9344
9345
9346
1.1.4
JCAR350225-081
8507r01
The requirements in Section 6.1.2 of Exhibit A to this
Appendix must be met by any Air
Emissions Testing Body
(AETB)
performing the semiannual/annual
RATAs described in Section
2.3
of this Exhibit and the mercury
emission
tests described in Sections 1.1 5(c) and
1.15
(d)(4)
of
Appendix
B.
1.2 Specific Requirements for Continuous Emissions
Monitoring
Systems
1.2.1 Calibration Error Test and Linearity
Check Procedures
Keep a written record of the procedures used
for
daily
calibration error tests and linearity
checks
(e.g.,
how gases are to be
injected, adjustments
of flow rates and pressure, introduction
of
reference values, length of time for
mi
ection
of
calibration
gases, steps for obtaining calibration
error or error in linearity,
determination
of interferences, and when calibration adjustments
should be
made).
Identify any calibration error test and
linearity check procedures specific to
the
continuous emission
monitoring
system that
vary
from the procedures in Exhibit A to this
Appendix.
1.2.2 Calibration and
Linearity
Adjustments
Explain how each component of the continuous emission monitoring system will
be
adjusted
to
provide correct responses to calibration gases, reference values, andlor indications
of
interference both
initially and after repairs
or corrective action. Identify equations, conversion
factors and
other factors affecting calibration
of each continuous emission monitoring system.
9372
1.2.3 Relative
Accuracy Test Audit Procedures
9373
Keep a
written record of procedures and details peculiar to the installed
continuous
emission
monitoring
systems that are to be used
for
relative
accuracy test
audits, such as sampling and
analysis
methods.
1.2.4
Parametric Monitoring for Units With Add-on Emission Controls
The
owner or operator shall keep a
written
(or electronic)
record including a list
of operating
parameters
for the add-on mercury emission
controls, as applicable, and the range of each
operating
parameter that indicates the add-on emission controls are operating
properly.
The
owner
or
operator shall keep
a
written
(or electronic)
record of the parametric monitoring
data
during each
mercury missing data period.
1.3 Requirements for Sorbent
Trap
Monitoring Systems
1.3.1 Sorbent
Trap Identification and Tracking
9347
9348
9349
9350
9351
9352
9353
9354
9355
9356
9357
9358
9359
9360
9361
9362
9363
9364
9365
9366
9367
9368
9369
9370
9371
9374
9375
9376
9377
9378
9379
9380
9381
9382
9383
9384
9385
9386
9387
9388
9389
JCAR350225-081 8507r01
9390
Include procedures for inscribing or otherwise permanently marking
a
unique
identification
9391
number
on each
sorbent
trap for tracking
purposes. Keep records of the ID of the monitoring
9392
system
in which each sorbent trap is used and the
dates
and
hours of each mercury collection
9393
period.
9394
9395
1.3.2 Monitoring
System Integrity and Data
Quality
9396
9397
Explain the procedures used to perform the leak checks when sorbent traps are placed in service
9398
and removed from service. Also
explain
the other
QA
procedures used to ensure system integrity
9399
and data
quality, including, but not limited to, gas flow meter calibrations, verification
of
9400
moisture removal, and ensuring
air-tight
pump operation. In addition, the
QA
plan must include
9401
the data
acceptance and quality control criteria in Section 8 of Exhibit
D to this Appendix. All
9402
reference meters used to
calibrate
the gas flow meters (e.g., wet test
meters)
must be periodically
9403
recalibrated. Annual, or more frequent, recalibration is recommended. If
a
NIST-traceable
9404
calibration device is used as a
reference
flow meter, the
QA
plan must include a protocol for
9405
ongoing
maintenance and periodic recalibration to maintain the accuracy and NIST-traceability
9406
of the calibrator.
9407
9408
1.3.3 Mercury Analysis
9409
9410
Explain the
chain of custody
employed
in packing, transporting,
and
analyzing
the sorbent traps
9411
(see
Sections
7.2.8 and 7.2.9 in Exhibit D to this
Appendix.).
Keep records of all mercury
9412
analyses.
The
analyses must be performed in accordance with the procedures described in
9413
Section 10
of Exhibit D to this Appendix.
9414
9415
1.3.4 Laboratory Certification
9416
9417
The QA Plan
must include documentation that
the
laboratory
performing the
analyses
on the
9418
carbon
sorbent
traps is certified by the International Organization for Standardization (ISO)
to
9419
have a proficiency
that meets the requirements of
ISO
17025. Alternatively,
if the laboratory
9420
performs
the spike recovery study described in Section 10.3 of Exhibit D to this Appendix
and
9421
repeats that
procedure annually. ISO certification is not required.
9422
9423
1.3.5 Data Collection Period
9424
9425
State,
and provide
the rationale for, the minimum
acceptable data collection period (e.g., one
9426
day,
one
week,
etc.)
for the size of the sorbent trap selected for the monitoring. Include in
the
9427
discussion
such factors as the
mercury
concentration in the stack gas, the capacity of the sorbent
9428
trap,
and
the minimum mass of
mercury
required
for the analysis.
9429
9430
1.3.6
Relative
Accuracy Test Audit Procedures
9431
9432
Keep
records of the
procedures
and
details
peculiar to the sorbent trap monitoring
systems
that
JCAR350225-08
1 8507r01
9433
are
to be
followed
for
relative accuracy
test
audits,
such
as sampling and analysis
methods.
9434
9435
2.
Frequency of Testing
9436
9437
A summary chart showing each quality assurance test
and the frequency at which each test
is
9438
required is located at the end of this Exhibit in Figure 1.
9439
9440
2.1 Daily Assessments
9441
9442
Perform the following daily
assessments
to quality-assure the
hourly
data recorded
by
the
9443
monitoring
systems during each period of unit operation,
or, for a bypass stack or duct, each
9444
period in which emissions pass
through
the bypass stack or duct. These
requirements
are
9445
effective as of the date when the monitor or continuous emission
monitoring system completes
9446
certification testing.
9447
9448
2.1 .1
Calibration Error Test
9449
9450
Except as provided
in Section 2.1.1.2
of this Exhibit, perform the daily calibration error test
of
9451
each gas
monitoring system (including moisture monitoring
systems consisting of wet- and
dry-
9452
basis
02
analyzers)
according to the procedures in Section 6.3.1 of Exhibit A to this
Appendix,
9453
and
perform the daily
calibration
error test of each flow monitoring system according
to the
9454
procedure in Section
6.3.2
of
Exhibit
A to this Appendix. When two measurement ranges
(low
9455
and high) are
required for a particular parameter, perform
sufficient
calibration error tests
on
9456
each range to
validate the data recorded on that range, according
to the
criteria
in Section 2.1.5
of
9457
this Exhibit.
9458
9459
For units with
add-on emission controls and dual-span or
auto-ranging monitors, and other
units
9460
that
use
the
maximum expected concentration to determine calibration gas values, perform
the
9461
daily calibration
error tests on each scale that
has been used since the previous calibration error
9462
test.
For example, if the pollutant concentration has not exceeded the low-scale value
(based
on
9463
the maximum
expected
concentration)
since the previous
calibration
error test, the calibration
9464
error
test
may be performed
on the
low-scale only. If,
however,
the concentration has exceeded
9465
the low-scale
span
value for one hour or longer since the previous calibration
error test, perform
9466
the
calibration error test on
both the low-
and high-scales.
9467
9468
2.1
.1.1 On-line Daily Calibration Error Tests
9469
9470
Except as
provided in Section 2.1.1.2 of this Exhibit, all daily
calibration error tests must be
9471
performed
while the unit is in operation at normal, stable conditions (i.e., ‘on-line”).
9472
9473
2.1.1.2 0ff-line
Daily Calibration Error Tests
9474
JCAR350225-081 8507r01
9475
Daily
calibrations may be performed while the unit is not operating
(i.e., “off-line”)
and
may be
9476
used to
validate
data for a
monitoring
system
that meets the following conditions:
9477
9478
1.)
An initial demonstration test of the monitoring system is successfully completed
9479
and the
results
are reported in the
quarterly
report
required
under
40
CFR
75.64,
9480
incorporated
by reference in
Section 225.140. The initial demonstration test,
9481
hereafter called the “off-line calibration demonstration”, consists of an off-line
9482
calibration error test followed by an on-line calibration error test. Both the off-line
9483
and on-line
portions
of the
off-line calibration demonstration
must
meet the
9484
calibration error
performance
specification in Section 3.1 of Exhibit A to
9485
Appendix B. Upon completion of the
off-line portion
of the
demonstration,
the
9486
zero and
upscale
monitor responses may be adjusted, but
only
toward the true
9487
values
of
the calibration
gases or
reference
signals
used
to
perform the test
and
9488
only in accordance with the routine calibration
adjustment
procedures specified in
9489
the
quality control program required under Section 1 of this Exhibit. Once these
9490
adjustments are made, no further
adjustments
may be made to the monitoring
9491
system
until after completion of the on-line portion of the off-line calibration
9492
demonstration. Within 26 clock hours after the completion hour of the off-line
9493
portion of the demonstration, the
monitoring
system must
successfully complete
9494
the
first
attempted calibration error test, i.e., the on-line portion of the
9495
demonstration.
9496
9497
)
For each monitoring system that has passed the off-line calibration
demonstration,
9498
off-line
calibration
error tests may be used on a
limited basis
to
validate data,
in
9499
accordance with subsection
(2)
in Section 2.1.5.1 of this Exhibit.
9500
9501
2.1.2
Daily Flow Interference Check
9502
9503
Perform the
daily flow monitor
interference
checks specified
in Section 2.2.2.2 of Exhibit
A to
9504
this
Appendix while
the unit is in operation at normal, stable conditions.
9505
9506
2.1.3
Additional Calibration Error Tests and Calibration
Adjustments
9507
9508
In
addition to the daily calibration error tests required under Section 2.1.1 of this
9509
Exhibit, a
calibration error
test of a
monitor
must be
performed in accordance
9510
with
Section
2.1.1 of this Exhibit, as follows: whenever a daily calibration error
9511
test is failed; whenever a monitoring system is returned to service following repair
9512
or
corrective maintenance
that could affect the monitor’s
ability
to
accurately
9513
measure
and record emissions data; or after making certain calibration
9514
adjustments, as described in this Section.
Except
in the case of the routine
9515
calibration adjustments described in this Section, data from the monitor are
9516
considered invalid until the required additional calibration error test has been
9517
successfully
completed.
JCAR350225-081 8507r01
9518
9519
j)
Routine
calibration
adjustments
of a monitor are permitted after
any successful
9520
calibration error
test. These
routine
adjustments must be made so as to bring
the
9521
monitor readings as close as
practicable
to the known tag values of the calibration
9522
gases or to the actual value of the flow monitor reference signals.
An additional
9523
calibration error test is required following routine calibration adjustments
where
9524
the
monitor’s calibration
has
been
physically
adjusted
(e.g., by turning a
9525
potentiometer) to verify that the adjustments
have been made properly. An
9526
additional calibration error test is not required, however, if the routine calibration
9527
adjustments are made
by
means
of a mathematical algorithm programmed into
the
9528
data acquisition and handling system. It is recommended that routine
calibration
9529
adjustments be made,
at a
minimum,
whenever the daily calibration error exceeds
9530
the limits of the applicable perfonnance specification in Exhibit A to this
9531
Appendix for the pollutant concentration monitor,
CO2or
02
monitor, or flow
9532
monitor.
9533
9534
ç
Additional
(non-routine)
calibration
adjustments
of a monitor are
permitted
prior
9535
to
(but not
during) linearity
checks and
RATAs and at other times, provided that
9536
an appropriate technical justification is included in the quality control
program
9537
required under
Section 1 of this Exhibit. The allowable non-routine adjustments
9538
are
as
follows. The owner or
operator may physically
adjust
the calibration
of a
9539
monitor
(e.g.,
by means of a potentiometer), provided
that
the post-adjustment
9540
zero and upscale responses of the monitor are within the performance
9541
specifications of the instrument given in Section 3.1 of Exhibit A to this
9542
Appendix. An additional
calibration error test is required following such
9543
adjustments to verify that the monitor is
operating within the performance
9544
specifications at both the zero and
upscale
calibration levels.
9545
9546
2.1.4
Data Validation
9547
9548
An out-of-control period occurs when the calibration error of a
CO2
or
02
monitor
9549
(includingQ monitors used to measure
CO2 emissions or percent
moisture)
9550
exceeds 1.0
percent
CO
2or
02,
or when the calibration error of a flow
monitor or
9551
a
moisture sensor exceeds
6.0
percent
of the span value, which is twice the
9552
applicable specification of Exhibit A to this Appendix. Notwithstanding,
a
9553
differential pressure-type flow
monitor for which the calibration error exceeds
6.0
9554
percent of the span
value
will not be considered out-of-control
if
—
9555
absolute value of the difference
between the monitor response and the reference
9556
value in Equation A-6 of Exhibit A
to this Appendix, is < 0.02 inches of water.
9557
For a mercury monitor, an out-of-control
period
occurs
when
the calibration error
9558
exceeds 5.0% of the span value. Notwithstanding,
the
mercury monitor
will not
be
9559
considered out-of-control
if
—
in Equation A-6 does not exceed 1.0
fig/scm.
JCAR350225-081
8507r01
9560
The
out-of-control
period begins
upon failure of the calibration
error test and ends
9561
upon completion of a successful
calibration
error test. Note, that if a failed
9562
calibration, corrective action, and successful calibration
error test occur within
the
9563
same
hour,
emission
data for that hour recorded by the monitor
after the
9564
successful calibration error
test may be used for reporting purposes, provided
that
9565
two or more valid readings
are
obtained
as
required
by Section 1.2 of this
9566
Appendix. Emission data must not be reported from
an out-of-control monitor.
9567
9568
i
An out-of-control
period
also occurs whenever interference of a flow monitor
is
9569
identified. The out-of-control
period
begins with the hour
of completion of the
9570
failed interference check
and ends
with
the hour of completion of an interference
9571
check that is passed.
9572
9573
2.1.5
Quality Assurance of Data With Respect to Daily Assessments
9574
9575
When a monitoring
system
passes
a daily assessment (i.e.,
daily
calibration error test
or daily
9576
flow
interference check), data from that monitoring
system
are
prospectively validated for 26
9577
clock hours
(i.e.,
24
hours plus a 2-hour grace
period)
beginning with the hour in which
the test
9578
is passed,
unless another assessment
(i.e.,
a daily calibration error test, an interference check
of a
9579
flow
monitor, a quarterly linearity check, a quarterly leak
check, or
a relative accuracy test audit)
9580
is failed within the 26-hour period.
9581
9582
2.1.5.1 Data
Invalidation with Respect to Daily Assessments
9583
9584
The following
specific rules apply to the invalidation
of data
with
respect to daily assessments:
9585
9586
fl
Data from
a monitoring system are invalid, beginning with the first
hour
9587
following the expiration of a 26-hour
data validation period or beginning
9588
with the
first hour following the expiration of an 8-hour start-up
grace
9589
period (as provided under Section 2.1.5.2
of this
Exhibit),
if the required
9590
subsequent daily assessment
has not been conducted.
9591
9592
)
For a monitor that
has passed the off-line calibration demonstration,
a
9593
combination of on-line and off-line calibration error tests
may be used to
9594
validate data from
the monitor, as follows. For a particular unit
(or
stack)
9595
operating hour, data from a monitor
may be validated using a successful
9596
off-line
calibration
error
test if:
9597
9598
An on-line calibration
error test has been passed within the
9599
previous 26 unit
(or stack)
operating hours; and
9600
9601
)
the 26
clock hour data validation window for the off-line
9602
calibration
error
test has not expired. If either of these conditions
is
JCAR350225-08
1 8507r01
9603
not met, then the data from
the
monitor are invalid with respect
to
9604
the daily calibration error test requirement. Data from the
monitor
9605
must
remain
invalid until
the appropriate on-line or off-line
9606
calibration error test is successfully completed
so that both
9607
conditions in subsections (a) and
(b)
are met.
9608
9609
For units with
two
measurement
ranges
(low
and high) for a particular
9610
parameter, when separate analyzers are used for the low and high
ranges,
a
9611
failed or expired calibration on one of the ranges does not affect the
9612
quality-assured data status on the
other range. For a dual-range analyzer
9613
(i.e.,
a single analyzer with two measurement scales), a failed calibration
9614
error test on either the low or high
scale results in an out-of-control period
9615
for the monitor. Data from the monitor remain invalid until corrective
9616
actions are taken and “hands-off’ calibration error tests have
been passed
9617
on
both
ranges.
However, if the most recent calibration error test on
the
9618
high scale was passed but has
expired,
while the low scale is up-to-date
on
9619
its calibration error
test
requirements
(or
vice-versa),
the expired
9620
calibration error test does not affect the quality-assured
status of the data
9621
recorded on the other scale.
9622
9623
2.1.5.2
Daily
Assessment
Start-Up Grace Period
9624
9625
For
the purpose of quality assuring data with respect to a daily assessment (i.e., a daily
9626
calibration error test or a flow
interference
check), a start-up grace period may apply when
a unit
9627
begins to operate
after a period of non-operation.
The start-up grace period for a daily calibration
9628
error test is
independent of the start-up grace period for
a
daily
flow
interference
check. To
9629
qualify
for a start-up grace period for a daily assessment, there are two requirements:
9630
9631
D
The unit must
have
resumed operation after being in outage for 1 or
more
9632
hours
(i.e.,
the unit must be in
a start-up
condition)
as evidenced by a
9633
change in unit operating time from zero in one clock hour to an
operating
9634
time greater than zero in the next
clock
hour.
9635
9636
For the monitoring system to be used
to
validate data
during
the grace
9637
period,
the
previous
daily assessment
of the same kind must have been
9638
passed
on-line
within 26 clock
hours prior to the last hour in which the
9639
unit operated before the outage. fri addition, the monitoring
system must
9640
be
in-control with
respect to quarterly and semi-annual or annual
9641
assessments.
9642
9643
If
both of
the
above
conditions are met, then a start-up grace period
of up to 8 clock hours
9644
applies,
beginning with the first hour of unit operation following the outage. During the
start-up
9645
grace
period,
data generated
by
the monitoring
system are considered quality-assured. For
each
JCAR350225-08 1 8507r01
9646
monitoring system, a start-up grace period
for a calibration error test or flow interference check
9647
ends when
either:
(1)
a
daily
assessment of the same kind
(i.e.,
calibration
error test or flow
9648
interference check) is performed
or
(2)
8 clock hours have elapsed (starting with the first
hour of
9649
unit operation following the outage), whichever
occurs first.
9650
9651
2.1.6 Data Recording
9652
9653
Record and tabulate all calibration error test
data according to month, day, clock-hour, and
9654
magnitude in either ppm, percent volume, or scth. Program monitors that automatically
adjust
9655
data to
the corrected calibration
values (e.g., microprocessor
control)
to record either:
(1)
the
9656
unadjusted concentration or flow rate measured in the calibration error
test
prior to resetting the
9657
calibration, or (2) the magnitude
of any
adjustment.
Record
the following applicable flow
9658
monitor interference check data: (1) sample line/sensing port pluggage, and (2)
malfunction of
9659
each
RTD, transceiver, or equivalent.
9660
9661
2.2 Quarterly
Assessments
9662
9663
For each
primary and redundant backup monitor
or monitoring system, perform the following
9664
quarterly assessments. This requirement applies as of the calendar quarter
following
the calendar
9665
quarter
in which the
monitor
or continuous emission monitoring system is provisionally
certified.
9666
9667
2.2.1
Linearity Check
9668
9669
Unless a
particular monitor
(or
monitoring
range)
is exempted under this
subsection or under
9670
Section 6.2 of Exhibit A to this Appendix, perform a
linearity
check, in accordance with
the
9671
procedures in
Section 6.2 of Exhibit A to
this Appendix, for each primary and redundant backup,
9672
mercury,
pollutant concentration monitor and each primary and redundant
backup CO2or
02
9673
monitor (including
02
monitors
used
to measure
CO
2
emissions or to continuously monitor
9674
moisture)
at
least once during each
QA
operating quarter,
as
defined in 40
CFR
72.2,
9675
incorporated by
reference
in
Section 225.140.
For mercury monitors, perform the linearity
9676
checks using
elemental mercury standards. Alternatively, you may perform 3-level
system
9677
integrity checks at
the same three calibration
gas levels
(i.e.,
low,
mid, and
high),
using a
NIST
9678
traceable
source of oxidized mercury. If you choose this
option,
the performance
specification in
9679
Section
3.2(c)
of
Exhibit A to this Part must
be met at each gas level. For units using both
a low
9680
and high
span value, a linearity check is required
only
on the ranges used
to record and report
9681
emission data during the
QA
operating quarter.
Conduct the linearity checks no less than
30 days
9682
apart, to the
extent practicable. The data validation
procedures
in Section
2.2.3(e)
of this Exhibit
9683
must be
followed.
9684
9685
2.2.2
Leak Check
9686
9687
For
differential
pressure flow monitors, perform
a
leak
check
of all sample lines (a manual check
9688
is
acceptable) at least once during each
QA
operating quarter.
For this test, the unit does not have
JCAR350225-081
8507r01
9689
to be in
operation. Conduct
the leak
checks no less than
30 days
apart, to the
extent practicable.
9690
If
a
leak check is
failed, follow the applicable
data
validation
procedures in
Section 2.2.3(g)
of
9691
this
Exhibit.
9692
9693
2.2.3
Data
Validation
9694
9695
A linearity
check must not be commenced
if
the
monitoring system
is operating
9696
out-of-control with
respect to
any of the daily or semiannual
quality
assurance
9697
assessments
required
by
Sections 2.1 and 2.3
of this Exhibit or with
respect
to the
9698
additional
calibration error test
requirements
in Section 2.1.3 of
this Exhibit.
9699
9700
Each
required
linearity
check
must
be done
according
to subsection
(b)(l),
(b)(2)
9701
or (b)(3) of
this Section:
9702
9703
jj
The
linearity check may
be done “cold”,
i.e., with no corrective
9704
maintenance,
repair,
calibration adjustments,
re-linearization
or
9705
reprogramming
of the
monitor prior to
the test.
9706
9707
The
linearity check
may be done after
performing only the routine
or non-
9708
routine calibration adjustments
described
in Section 2.1.3
of this Exhibit
9709
at the various calibration
gas
levels (zero,
low,
mid
or high), but no
other
9710
corrective maintenance,
repair, re-linearization
or reprogramming of
the
9711
monitor. Trial
gas
injection
runs
may be
performed
after
the calibration
9712
adjustments
and
additional
adjustments
within
the allowable limits
in
9713
Section
2.1.3 of this Exhibit
may
be made
prior to the
linearity
check,
as
9714
necessary,
to optimize the
performance
of the monitor. The trial
gas
9715
injections
need
not
be
reported, provided that
they
meet the
specification
9716
for
trial gas
injections
in
Section
1.4(b)(3)(G)(v)
of this Appendix.
9717
However,
if, for
any
trial
injection,
the specification
in Section
9718
1.4(b)(3)(G)(v)
is not met,
the trial
injection
must be counted
as an
aborted
9719
linearity
check.
9720
9721
The
linearity
check
may
be done after repair,
corrective maintenance
or
9722
reprogramming
of the monitor.
In this case,
the monitor must
be
9723
considered
out-of-control
from the hour in
which the repair, corrective
9724
maintenance
or reprogramming
is
commenced
until the
linearity
check
has
9725
been
passed.
Alternatively,
the data validation
procedures
and associated
9726
timelines
in Sections
1.4(b)(3)(B)
through
(I)
of this Appendix
maybe
9727
followed upon completion
of the necessary
repair, corrective
maintenance,
9728
or reprogramming.
If the procedures
in Section
1.4(b)(3)
are used, the
9729
words
“quality
assurance”
apply instead
of the word
“recertification”.
9730
9731
Once a linearity check
has
been commenced,
the test must
be done hands-off.
JCAR350225-081 8507r01
9732
That is, no adjustments of the
monitor
are permitted during the linearity test
9733
period, other than the routine calibration adjustments
following daily calibration
9734
error tests, as
described in Section
2.1.3
of this Exhibit. If a routine daily
9735
calibration error test is performed and passed just prior to a linearity test
(or
9736
during a linearity test period) and a mathematical correction
factor is
9737
automatically applied by the DAHS, the
correction factor
must
be applied
to
all
9738
subsequent
data recorded
by the
monitor, including the
linearity
test
data.
9739
9740
ç)
If a daily calibration error test is failed during a linearity test
period,
prior
to
9741
completing
the test, the linearity test must be
repeated.
Data
from the monitor are
9742
invalidated prospectively from the hour of the failed
calibration error
test
until the
9743
hour of
completion of
a
subsequent successful calibration error test. The linearity
9744
test must not be conunenced until the monitor has
successfully completed a
9745
calibration error test.
9746
9747
An
out-of-control
period occurs when a linearity test is failed
(i.e.,
when the error
9748
in
linearity at any of the three
concentrations in the quarterly
linearity
check (or
9749
any of
the six concentrations, when both ranges of a single analyzer with a dual
9750
range are tested) exceeds the applicable specification in
Section 3.2 of Exhibit
A
9751
to this Appendix) or when a linearity test
is aborted due to a problem with the
9752
monitor or
monitoring
system.
The out-of-control period begins with the hour of
9753
the failed
or aborted linearity check and ends with the hour of completion of a
9754
satisfactory linearity check following
corrective
action and/or
monitor
repair,
9755
unless
the option in subsection (b)(3) of this
Section
to use the data
validation
9756
procedures and associated timelines in
Section
1.4(b)(3)(B)
through
(I)
of this
9757
Appendix
has been selected, in which case the beginning and end of the out-of-
9758
control period must be determined in accordance with
Sections 1.4(b)(3)(G)(i)
9759
and
(ii).
For a dual-range
analyzer, “hands-off’ linearity checks must be passed
on
9760
both
measurement
scales to end the out-of-control period.
9761
9762
fi
No
more than four successive calendar quarters must elapse
after the
quarter in
9763
which a
linearity check of a monitor or monitoring system
(or
range of a monitor
9764
or
monitoring system) was last performed
without
a subsequent linearity test
9765
having been
conducted. If a linearity test has not been completed by the end of the
9766
fourth calendar quarter since the last linearity test, then the
linearity test must
be
9767
completed
within a 168 unit
operating hour or stack operating hour “grace period”
9768
(as
provided in Section 2.2.4 of this Exhibit) following the end of the fourth
9769
successive elapsed calendar quarter, or data from the CEMS
(or
range) will
9770
become invalid.
9771
9772
An
out-of-control period also occurs when a flow monitor
sample
line leak is
9773
detected.
The out-of-control period begins with the hour of the failed
leak
check
9774
and
ends
with the hour of a satisfactory leak check following
corrective action.
1CAR350225-08
1 8507r01
9775
9776
)
For each monitoring system, report the
results of all completed and partial
9777
linearity
tests
that
affect
data validation (i.e.,
all
completed, passed linearity
9778
checks; all
completed,
failed linearity checks; and all
linearity
checks aborted
due
9779
to a problem with the monitor, including
trial gas
injections
counted as failed
test
9780
attempts under subsection (b)(2) of this
Section or under Section 1 .4(b)(3)(G)(vi)
9781
of Appendix
B),
in the quarterly report required under 40 CFR 75.64,
9782
incorporated
by
reference
in Section 225.140. Note that linearity attempts
that are
9783
aborted or invalidated due
to
problems
with
the reference calibration gases or
due
9784
to operational problems
with the affected units need not be reported.
Such partial
9785
tests do not affect the validation
status of emission data recorded by the monitor.
9786
A
record
of
all linearity
tests, trial gas
injections
and test attempts (whether
9787
reported or not) must be kept on-site as
part of the official test log for each
9788
monitoring system.
9789
9790
2.2.4
Linearity
and Leak Check Grace Period
9791
9792
When a required linearity
test or flow monitor leak check has not been
completed
9793
by
the end of the
OA
operating
quarter in which it is due or if, due to infrequent
9794
operation of a unit or infrequent use of a required
high
range
of a monitor or
9795
monitoring system, four successive calendar quarters have elapsed
after
the
9796
quarter in which a linearity
check of a monitor or monitoring
system
(or
range)
9797
was
last performed without
a subsequent linearity test having been done, the
9798
owner or operator has a grace period
of 168 consecutive unit operating hours,
as
9799
defined in
40
CFR 72.2, incorporated
by
reference
in Section
225.140
(or,
for
9800
monitors installed
on common stacks or bypass stacks, 168 consecutive
stack
9801
operating hours, as defined in 40
CFR
72.2)
in which to perform a linearity
test or
9802
leak
check
of that monitor or monitoring system
(or
range). The grace
period
9803
begins with the first unit or stack
operating hour following the calendar quarter
in
9804
which the linearity test was due. Data validation during
a
linearity
or leak check
9805
grace period must be done in accordance
with the applicable provisions in
Section
9806
2.2.3 of this Exhibit.
9807
9808
If, at
the end
of
the 168
unit
(or
stack) operating hour grace
period,
the
required
9809
linearity testor leak check has not been
completed, data from the monitoring
9810
system
(or
range) will be invalid, beginning with the first
unit operating hour
9811
following the expiration
of the
grace
period. Data from the monitoring system
(or
9812
range) remain
invalid
until the hour
of completion of a subsequent successful
9813
hands-off linearity test or leak check of the
monitor or monitoring system
(or
9814
range). Note that
when
a linearity test or a leak check is conducted within
a grace
9815
period for the purpose of
satisfying the linearity test or leak check requirement
9816
from a previous
OA
operating
quarter, the results of that
linearity
test or leak
9817
check
may only be used to meet the linearity
check or leak check requirement
of
JCAR350225-08 1
8507r01
9818
the previous quarter,
not
the quarter in which the missed linearity test
or
leak
9819
check is completed.
9820
9821
2.2.5 Flow-to-Load
Ratio or Gross Heat Rate Evaluation
9822
9823
Applicability and methodology. Unless
exempted
from the flow-to-load ratio test
9824
under Section 7.8 to Appendix A to 40 CFR
75
, the owner
or
operator
must, for
9825
each flow rate monitoring
system installed on each unit, common stack or
9826
multiple stack, evaluate the flow-to-load
ratio quarterly, i.e., for each
OA
9827
operating
quarter
(as
defined in 40 CFR 72.2, incorporated
by
reference
in Section
9828
225.140). At the end
of
each
QA
operating quarter, the owner or operator must
9829
use Equation B-i to calculate the flow-to-load ratio for every hour during
the
9830
quarter in which: the unit
(or
combination
of units, for a common stack) operated
9831
within
±
10.0 percent
of L, the average load during the most recent normal-load
9832
flow RATA and a quality assured hourly
average flow rate was obtained with a
9833
certified flow rate
monitor. Alternatively, for the reasons stated in subsections
9834
(c)(1)
through (6) of this Section, the owner or operator
may
exclude
from the
9835
data
analysis
certain hours
within
±
10.0
percent
of Land may calculate L,
9836
values for only the remaining hours.
9837
9838
Rh
=-iO
(EquationB-i)
9839
9840
Where:
9841
Rh
= Hourly value
of the flow-to-load ratio, scfhlmegawatts, scffi/1000
lb/hr
of steam, or
scflul(mmBtu/hr
thermal output).
= Hourly stack gas volumetric flow rate, as measured
by the
flow
rate
monitor, scfh.
Lh
= Hourly
unit load,
megawatts, 1000 lb/hr of steam, or mmBtulhr
thermal
output must be within
+
10.0 percent of
L during
the
most
recent normal-load
flow RATA.
9842
9843
.11
In
Equation
B-i, the
owner or operator may use either bias-adjusted flow
9844
rates or
unadjusted
flow rates, provided that all
of the ratios are calculated
9845
the same way. For a common stack,
Lh
will be the sum of the hourly
9846
operating
loads of
all units that discharge through the stack. For a unit
that
9847
discharges its emissions through
multiple stacks or that monitors its
9848
emissions in multiple breechings,
Oh
will
be either the combined hourly
9849
volumetric
flow
rate for all of the stacks or ducts
(if
the test is done on a
9850
unit
basis) or the
hourly flow rate through each stack individually (if
the
9851
test
is
performed
separately
for each
stack).
For a unit with a multiple
JCAR350225-08 1
8507r01
9852
stack
discharge configuration consisting
of a main stack
and
a bypass
9853
stack, each of which has a certified flow monitor (e.g., a unit with a wet
9854
SO
2
scrubber), calculate the
hourly flow-to-load ratios separately for each
9855
stack. Round off each value of
Rh
to
two decimal places.
9856
9857
)
Alternatively, the owner or operator may calculate the hourly gross heat
9858
rates
(GHR)
in
lieu of the
hourly
flow-to-load
ratios. The hourly GHR
9859
must be determined
only
for those hours in which quality assured
flow rate
9860
data and diluent gas
(CO
2
or
02)
concentration data are both available
9861
from a certified monitor or
monitoring system or
reference
method. If this
9862
option is selected, calculate each hourly GHR value as follows:
9863
9864
(GHR)h
= (Heatlnput)h
x
1000
(Equation B-la)
9865
9866
Where:
9867
(GHR)h
= Hourly value of the gross heat rate, Btu/kwh, Btullb steam
load, or
1000 mmBtu heat input/mmBtu thermal output.
(Heatlnput)h
= Hourly heat input, as determined from the quality assured
flow
rate and diluent data, using the applicable equation in
Exhibit
C to this Appendix, mmBtu/hr.
Hourly
unit
load, megawatts, 1000 lb/hr of steam, or
mmBtu/hr thermal output; must be within
+
10.0 percent
of
L during the most recent normal-load flow RATA.
9868
9869
In Equation B-la, the owner or
operator
may either use bias-adjusted
flow
9870
rates
or
unadjusted
flow
rates
in the calculation of
(Heatlnput)h,
provided
9871
that all of the heat input values are determined in the same manner.
9872
9873
4
The owner or operator must evaluate the calculated hourly flow-to-load
9874
ratios
(or gross heat
rates)
as follows.
A
separate data
analysis
must be
9875
performed for each primary and each redundant backup flow rate monitor
9876
used to
record and report
data during the quarter. Each analysis must be
9877
based on a minimum of 168 acceptable recorded hourly average flow
rates
9878
(i.e.,
at loads within + 10 percent of
L).
When two RATA load levels
9879
are designated as normal, the
analysis
must be performed at the higher
9880
load
level, unless there are fewer than 168 acceptable data points available
9881
at that load level, in which case the analysis must be performed at the
9882
lower
load level. If, for
a
particular
flow monitor,
fewer
than
168
9883
acceptable hourly flow-to-load ratios
(or
GHR
values) are available
at any
9884
of the load levels designated as normal, a flow-to-load
(or
GHR)
JCAR350225-08
1
8507r01
9885
evaluation is not required for that monitor for that calendar quarter.
9886
9887
For each flow monitor,
use
Equation B-2 in
this
Exhibit to calculate
Eh
9888
the absolute percentage difference between each hourly
Rh
value and R
9889
the
reference value
of the flow-to-load ratio, as detennined in accordance
9890
with Section
7.7 to Appendix A to 40 CFR 75. Note that Rmust always
9891
be based upon the
most
recent normal-load RATA, even if that RATA
was
9892
performed in the calendar quarter being evaluated.
9893
R -R,
9894
Eh
= rf
xlOO
(EquationB-2)
Rrei
9895
9896
Where:
9897
= Absolute percentage difference between the hourly average flow-to-
load
ratio
and the reference value of the
flow-to-load ratio
at
normal
load.
Rh
= The hourly average flow-to-load ratio, for each flow rate recorded
at a
load level within ± 10.0
percent
of L,.
= The reference value of the flow-to-load ratio from the most recent
normal-load flow RATA, determined in accordance with Section
7.7
to Appendix A to 40 CFR 75.
9898
9899
Equation B-2 must be used in a consistent manner. That is, use Rand
Rh
9900
if the flow-to-load ratio is being evaluated, and use
(GHR)ref
and (GHR)h
9901
if
the gross
heat
rate is being evaluated.
Finally,
calculate Efj
9902
arithmetic average of all of the hourly
Eh
values. The owner or operator
9903
must
report
the
results
of
each quarterly flow-to-load
(or
gross
heat rate)
9904
evaluation, as determined from Equation B-2, in the electronic quarterly
9905
report required under 40 CFR 75.64.
9906
9907
i
Acceptable results. The results of a quarterly flow-to-load
(or
gross
heat rate)
9908
evaluation are acceptable, and no further action is required, if the calculated value
9909
of Ef is less
than or equal to:
(1)
15.0 percent, if L for the most recent normal-
9910
load
flow RATA is 60 megawatts (or 500 klb/hr of steam) and if
unadjusted
9911
flow rates were used in the calculations; or
(2)
10.0
percent, if L for the most
9912
recent normal-load
flow RATA
is
60 megawatts (or 500 klb/hr
of steam) and
9913
if
bias-adjusted flow rates were used in the calculations; or
(3)
20.0
percent,
if
9914
L
for the most recent normal-load flow RATA is <60 megawatts
(or
< 500
9915
klb/hr of
steam)
and if unadjusted flow rates were used in the calculations; or (4)
9916
15.0 percent, if L
for
the most recent normal-load
flow
RATA is <60
9917
megawatts (or
< 500
klb/hr of steam) and if bias-adjusted
flow
rates were
used in
JCAR350225-081 8507r01
9918
the
calculations.
If Ef
is
above these
limits, the
owner or operator must
either:
9919
implement Option
1 in Section
2.2.5.1
of this Exhibit;
or perform
a RATA in
9920
accordance
with
Option
2
in Section
2.2.5.2
of
this Exhibit; or re-examine
the
9921
hourly
data used for the flow-to-load
or GHR
analysis
and recalculate
Ef, after
9922
excluding all
non-representative
hourly flow
rates. If Ef is
above
these limits, the
9923
owner
or operator
must
either: implement
Option
1 in Section 2.2.5.1
of this
9924
Exhibit:
perform a
RATA in accordance
with Option 2 in Section
2.2.5.2
of this
9925
Exhibit:
or
(if
applicable)
re-examine
the hourly data used
for the flow-to-load
or
9926
GHR
analysis
and
recalculate Ef, after
excluding all non-representative
hourly
9927
flow rates, as provided
in subsection
(c)
of this Section.
9928
9929
c
Recalculation of Ef.
If
the owner
or operator did not exclude
any hours within
±
9930
10
percent
of L
from the original data
analysis and
chooses
to recalculate
E
9931
the flow rates for the
following hours
are considered non-representative
and
may
9932
be
excluded from
the data analysis:
9933
9934
fl
Any hour in
which the type of
fuel combusted was
different
from
the fuel
9935
burned during
the most recent
normal-load RATA.
For purposes of this
9936
determination,
the type of fuel
is different
if
the fuel is in a different
state
9937
of matter (i.e.,
solid,
liquid,
or gas) than is the fuel
burned during
the
9938
RATA or
if the fuel is
a
different classification
of coal
(e.g.,
bituminous
9939
versus
sub-bituminous).
Also,
for units
that co-fire different
types of
fuels,
9940
if the reference RATA
was done
while
co-firing, then hours
in which
a
9941
single fuel was combusted
may
be
excluded
from
the
data
analysis
as
9942
different fuel
hours
(and
vice-versa
for co-fired hours, if
the reference
9943
RATA was done
while
combusting
only
one type of
fuel):
9944
9945
)
For a unit that is
equipped
with
an
SO
2
scrubber and
which always
9946
discharges its
flue gases to the atmosphere
through
a single stack, any
9947
hour in which the
SO
1 scrubber
was bypassed;
9948
9949
Any hour in which
“ramping”
occurred, i.e., the hourly
load differed
by
9950
more than
+
15.0 percent from the
load
during
the
preceding
hour or
the
9951
subsequent hour;
9952
9953
4
For
a
unit with a
multiple
stack
discharge configuration
consisting
of a
9954
main stack and
a bypass stack,
any hour in which
the flue gases were
9955
discharged
through
both
stacks:
9956
9957
If a normal-load
flow
RATA was performed
and passed during the
quarter
9958
being
analyzed, any hour
prior to completion
of that RATA;
and
9959
9960
)
If a
problem
with
the accuracy of the flow
monitor was
discovered
during
JCAR350225-081
8507r01
9961
the
quarter and was corrected
(as evidenced by
passing the
abbreviated
9962
flow-to-load
test in Section 2.2.5.3
of
this Exhibit),
any
hour prior to
9963
completion of
the
abbreviated
flow-to-load
test.
9964
9965
D
After identifying
and excluding all
non-representative
hourly
data in
9966
accordance with
subsections
(c)(1)
through
(6)
of this
Section,
the
owner
9967
or operator may
analyze the remaining
data a
second
time. At least 168
9968
representative hourly
ratios or GHR values
must be
available to
perform
9969
the analysis: otherwise,
the
flow-to-load
(or GHR)
analysis is not required
9970
for
that monitor for
that calendar quarter.
9971
9972
If, after
re-analyzing
the data, Ef meets
the
applicable
limit in subsection
9973
(b)(1),
(b)(2), (b)(3),
or (b)(4)
of
this
Section,
no
further action is
required.
9974
If,
however,
Ef is
still above the
applicable limit, data
from the
monitor
9975
will be declared out-of-control,
beginning
with
the
first
unit operating
9976
hour
following the
quarter in which Ef
exceeded the
applicable
limit.
9977
Alternatively, if a probationary
calibration
error
test
is performed and
9978
passed
according
to
Section
1.4(b)(3)(B)
of this Appendix,
data
from the
9979
monitor may be declared
conditionally
valid following
the quarter in
9980
which
Ef exceeded the
applicable limit.
The
owner
or operator must then
9981
either implement
Option
1 in Section
2.2.5.1 of this Exhibit
or Option 2 in
9982
Section
2.2.5.2
of
this Exhibit.
9983
9984
2.2.5.1 Option
1
9985
9986
Within
14
unit
operating
days of the end
of the calendar
quarter for which
the Ef value is
above
9987
the
applicable
limit,
investigate and troubleshoot
the
applicable flow monitors.
Evaluate
the
9988
results of each
investigation
as follows:
9989
9990
If the
investigation
fails to
uncover a problem
with
the
flow monitor, a RATA
9991
must be
performed in accordance
with
Option 2 in Section
2.2.5.2 of
this
Exhibit.
9992
9993
If a
problem
with the flow
monitor is
identified through the
investigation
9994
(including
the need to
re-linearize the monitor
by
changing
the polynomial
9995
coefficients
or K
factors),
data from the
monitor are considered
invalid back
to
the
9996
first unit
operating hour after
the
end of the
calendar
quarter
for which Ef was
9997
above the
applicable
limit.
If the option to use
conditional
data validation was
9998
selected under
Section
2.2.5(c)(8)
of this
Exhibit, all
conditionally
valid data
will
9999
be invalidated,
back to the first unit
operating
hour after the
end of the calendar
10000
quarter
for
which
Ef was above
the applicable limit.
Corrective
actions must be
10001
taken. All corrective
actions (e.g.,
non-routine
maintenance, repairs,
major
10002
component
replacements,
re-linearization
of
the monitor,
etc.)
must be
10003
documented
in
the operation
and
maintenance records
for the monitor.
The owner
JCAR350225-08 1 8507r01
10004
or
operator then
must either complete
the abbreviated flow-to-load test in Section
10005
2.2.5.3 of this Exhibit,
or, if the corrective action taken has required
10006
relinearization of the flow monitor,
must perform a 3-load RATA. The
10007
conditional data
validation procedures
in
Section
1.4(b)(3)of
this
Appendix may
10008
be applied to the 3-load
RATA.
10009
10010
2.2.5.2
Option
2
10011
10012
Perform
a single-load RATA
(at
a load
designated as normal under Section 6.5.2.1 of Exhibit
A
10013
to this Appendix) of each flow monitor for which
Ef is outside of the applicable limit. If the
10014
RATA is
passed hands-off, in accordance
with Section
2.3.2(c)
of this Exhibit, no further
action
10015
is required and the out-of-control period for the monitor
ends at the date and hour of
completion
10016
of a
successful RATA, unless the option
to use conditional data validation was selected
under
10017
Section
2.2.5(c)(8)
of
this
Exhibit.
In that case, all conditionally
valid data from the monitor are
10018
considered to be quality-assured, back
to the first unit operating hour following the end
of the
10019
calendar quarter
for which
the Ef value was above the applicable
limit. If the
RATA
is failed,
all
10020
data
from the monitor will be invalidated,
back
to the first
imit
operating hour following the
end
10021
of the calendar quarter for which the Ef value was above the
applicable limit. Data from the
10022
monitor remain
invalid
until the required
RATA has been passed. Alternatively, following
a
10023
failed
RATA and corrective actions, the conditional
data validation procedures of Section
10024
1 .4(b)(3)
of this Appendix may be used until the RATA
has been passed. If the corrective
actions
10025
taken following the
failed
RATA included
adjustment
of the
polynomial coefficients or K factors
10026
of
the flow
monitor,
a
3-level
RATA is required, except as otherwise specified in Section
2.3.1.3
10027
of this Exhibit.
10028
10029
2.2.5.3 Abbreviated Flow-to-Load
Test
10030
10031
The following abbreviated flow-to-load test
may be performed after any
10032
documented repair,
component replacement, or other corrective maintenance
to
a
10033
flow monitor (except for changes affecting
the linearity of the flow monitor,
such
10034
as
adjusting
the flow
monitor coefficients or K
factors)
to demonstrate
that the
10035
repair, replacement, or other maintenance has
not significantly affected the
10036
monitor’s ability to accurately
measure the stack gas volumetric flow rate.
Data
10037
from the monitoring system are considered invalid
from the hour of
10038
commencement of the repair,
replacement, or maintenance until either
the hour in
10039
which the abbreviated flow-to-load
test
is
passed, or the hour in which a
10040
probationary calibration error test is passed following
completion of the repair,
10041
replacement, or maintenance
and any associated adjustments to the monitor.
If the
10042
latter option is selected, the abbreviated
flow-to-load
test must be completed
10043
within 168 unit operating hours of the probationary
calibration error test
(or,
for
10044
peaking units, within 30 unit operating days, if
that is less
restrictive).
Data
from
10045
the monitor
are
considered to be conditionally valid
(as
defined
in 40
CFR 72.2,
10046
incorporated
by
reference in
Section
225.140),
beginning with the hour
of the
JCAR350225-08 1 8507r01
10047
probationary calibration error
test.
10048
10049
)
Operate
the units in
such a way as to reproduce, as closely as
practicable,
the
10050
exact conditions at the time
of
the
most recent normal-load
flow
RATA. To
10051
achieve this, it is recommended that the
load
be held constant to within
+ 10.0
10052
percent
of the
average
load during the RATA and that the diluent gas
(CQ2
or
02)
10053
concentration be
maintained within
±
0.5 percent
CO2
or
02
of the average diluent
10054
concentration during the RATA.
For
common stacks, to the
extent
practicable, use
10055
the same combination of units and load levels that were used during the RATA.
10056
When the
process
parameters
have
been set, record a minimum of six and a
10057
maximum of 12 consecutive hourly average flow rates, using the flow monitors
10058
for which Ef
was
outside the applicable limit. For peaking units, a minimum of
10059
three and a maximum of 12 consecutive hourly average flow rates are required.
10060
Also
record the corresponding hourly
load
values
and, if applicable, the hourly
10061
diluent gas concentrations. Calculate the flow-to-load ratio
(or GHR)
for each
10062
hour in
the test hour period,
using Equation
B-i or B-ia.
Determine
Eh
for each
10063
hourly flow- to-load ratio
(or GHR).
using Equation B-2 of this Exhibit and then
10064
calculate Ef,
the arithmetic
average of the Eh values.
10065
10066
ç)
The results of the abbreviated flow-to-load test will be considered acceptable,
and
10067
no
further
action is
required if the value of
Eh
does not exceed the applicable limit
10068
specified
in Section 2.2.5
of this Exhibit. All conditionally
valid
data recorded
by
10069
the flow
monitor will be considered quality assured, beginning with the
hour of
10070
the
probationary calibration error test that preceded the abbreviated flow-to-load
10071
test
(if
applicable). However, if Ef is outside the applicable limit, all conditionally
10072
valid data recorded by the flow monitor
(if
applicable) will be considered invalid
10073
back to
the hour of the probationary calibration error test that preceded the
10074
abbreviated flow-to-load test, and a single-load RATA is required in accordance
10075
with
Section
2.2.5.2 of this Exhibit. If the flow monitor must
be
re-linearized,
10076
however, a 3-load RATA is required.
10077
10078
2.3
Semiannual and Annual Assessments
10079
10080
For each
primary and redundant backup monitoring system, perform relative accuracy
10081
assessments either
semiannually or annually, as specified in Section 2.3.1.1 or 2.3.1.2 of this
10082
Exhibit for the
type
of test and the performance achieved. This requirement applies as of the
10083
calendar
quarter following
the calendar quarter in
which the monitoring system is provisionally
10084
certified.
A
summary chart showing the frequency with which a relative accuracy test
audit must
10085
be
performed,
depending on the accuracy achieved, is located at the end of this Exhibit in Figure
10086
2.
10087
10088
2.3.1 Relative Accuracy Test
Audit
(RATA)
10089
JCAR350225-081 8507r01
10090
2.3.1.1 Standard RATA Frequencies
10091
10092
Except for mercury monitoring systems,
and as otherwise
specified
in
Section
10093
2.3.1.2 of this Exhibit, perform relative accuracy test audits semiannually, i.e.,
10094
once every two
successive
QA
operating quarters
(as
defined in 40 CFR 72.2,
10095
incorporated by reference in
Section
225.140)
for each primary and redundant
10096
backup
flow monitor,
CO2
or
02
diluent
monitor used to
determine heat input,
10097
moisture monitoring system. For each primary and redundant backup mercury
10098
concentration monitoring system and each sorbent trap monitoring system,
10099
RATAs must be performed
annually,
i.e.,
once
every four successive
QA
10100
operating quarters
(as
defined in
40
CFR 72.2). A calendar quarter that does not
10101
qualify as a
OA
operating quarter must
be
excluded in determining the deadline
10102
for the next RATA. No more than eight successive calendar quarters must elapse
10103
after the quarter in which a RATA was last performed without a subsequent
10104
RATA
having been
conducted.
If
a RATA has not been
completed
by the end of
10105
the eighth calendar quarter since the quarter of the last RATA, then the RATA
10106
must be
completed within
a
720 unit
(or stack)
operating
hour grace
period
(as
10107
provided
in Section 2.3.3 of this
Exhibit)
following the end of the eighth
10108
successive elapsed calendar quarter, or data from the CEMS will become invalid.
10109
10110
})
The relative accuracy test audit frequency of a CEMS may be reduced, as
10111
specified in Section 2.3.1.2 of this Exhibit, for primary or redundant backup
10112
monitoring systems which qualify for less frequent testing. Perform all required
10113
RATAs in accordance with the applicable procedures and provisions in Sections
10114
6.5
through 6.5.2.2 of Exhibit
A to
this
Appendix and
Sections 2.3.1.3
and 2.3.1.4
10115
of
this Exhibit.
10116
10117
2.3.1.2 Reduced RATA Frequencies
10118
10119
Relative accuracy
test
audits of primary and redundant
backup
CO2
or
02
diluent monitors
used
10120
to determine
heat input, moisture monitoring systems, flow monitors may be performed annually
10121
(i.e.,
once every
four
successive
QA
operating quarters, rather than once every two successive
10122
QA
operating
quarters)
if any of the following conditions are met for the specific monitoring
10123
system involved:
10124
10125
The
relative accuracy during the audit of
aQ
2
or
02
diluent monitor
used to
10126
determine heat input is 7.5
percent:
10127
10128
j
The
relative accuracy during the audit
of a
flow
monitor is
7.5
percent at each
10129
operating level tested:
10130
10131
For low flow
(1
0.0
fs),
as measured by the reference method during the RATA
10132
stacks/ducts, when
the
flow
monitor
fails to achieve a relative accuracy 7.5
JCAR350225-08 1 8507r01
10133
percent
during the audit, but the monitor
mean
value, calculated using Equation
10134
A-7 in Exhibit A
to this Appendix
and converted
back
to
an equivalent velocity in
10135
standard feet
per second
(fps),
is within
+
1.5
fps of the reference method mean
10136
value, converted to an equivalent velocity in fps;
10137
10138
çj)
For a
CO
2
or
02
monitor, when
the
mean difference
between
the reference method
10139
values from the
RATA and the corresponding monitor values is within
±
0.7
10140
percent CO2
oQ; and
10141
10142
When the
relative accuracy of a continuous moisture monitoring system is 7.5
10143
percent or when the mean difference between the
reference method values from
10144
the RATA and
the corresponding monitoring system values is within
±
1.0
10145
percent H
2
O.
10146
10147
2.3.1.3
RATA Load
(or
Operating) Levels and
Additional RATA Requirements
10148
10149
For
CO
2
or
02
diluent monitors used to
determine heat input, mercury
10150
concentration
monitoring systems, sorbent trap monitoring systems, moisture
10151
monitoring
systems,
the
required semiannual or annual RATA
tests must be
done
10152
at the load level (or operating
level)
designated
as
normal under Section 6.5.2.1(d)
10153
of Exhibit A to
this Appendix. If two load levels
(or
operating
levels)
are
10154
designated as
normal, the required RATAs may be done at either load
level
(or
10155
operating
level).
10156
10157
}
For flow monitors installed and bypass stacks,
and for flow monitors that qualify
10158
to perform only
single-level RATAs under Section 6.5.2(e) of Exhibit A to this
10159
Appendix, all required semiannual or annual relative accuracy
test audits must
be
10160
single-load
(or
single-level) audits at
the normal load
(or
operating
level),
as
10161
defined
in Section
6.5.2.1(d)
of Exhibit A to this
Appendix.
10162
10163
For all
other flow monitors, the RATAs must be performed as
follows:
10164
10165
J
An annual 2-load
(or
2-level) flow
RATA
must be
done at the two most
10166
frequently used load
levels
(or
operating levels), as determined under
10167
Section
6.5.2.1(d)
of Exhibit A to this
Appendix, or (if applicable) at
the
10168
operating levels determined
under Section
6.5.2(e)
of Exhibit A to this
10169
Appendix. Alternatively, a 3-load
(or
3-level) flow RATA at the low, mid,
10170
and high load levels
(or
operating
levels),
as defined
under Section
10171
6.5.2.1(b)
of Exhibit A to this Appendix,
may
be
performed in lieu
of the
10172
2-load
(or
2-level) annual
RATA.
10173
10174
)
If the
flow monitor is on
a
semiannual RATA frequency, 2-load
(or
2-
10175
level)
flow RATAs and single-load
(or
single-level) flow RATAs at
the
JCAR350225-08
1
8507r01
10176
normal load level (or normal operating level) maybe performed
10177
alternately.
10178
10179
)
A single-load (or single-level) annual flow RATA may be performed
in
10180
lieu of the
2-load
(or
2-level)
RATA if the results of an historical load data
10181
analysis show
that in the time period extending from the ending date of the
10182
last annual flow RATA to a date that
is no
more than 21
days prior to the
10183
date of the current annual flow RATA, the unit
(or
combination of units,
10184
for a common
stack)
has operated at a single load level
(or
operating level)
10185
(low,
mid, or
high),
for 85.0 percent of the time. Alternatively, a flow
10186
monitor may qualify for a single-load (or single-level) RATA if the 85.0
10187
percent criterion is met in the time period extending from the beginning
of
10188
the
quarter in which
the last annual flow RATA was performed through
10189
the end of the calendar quarter preceding the quarter of current annual
10190
flow RATA.
10191
10192
4)
A 3-load (or 3-level) RATA, at the low-,
mid-, and high-load
levels
(or
10193
operating levels), as determined under Section 6.5.2.1 of Exhibit A to
this
10194
Appendix,
must be performed at least once every twenty consecutive
10195
calendar quarters, except for flow monitors
that are exempted from 3-load
10196
(or 3-level)
RATA testing under Section 6.5.2(b) or 6.5.2(e)
of
Exhibit
A
10197
to this Appendix.
10198
10199
)
A 3-load
(or
3-level)
RATA
is required whenever a flow monitor is re
10200
linearized, i.e., when its polynomial
coefficients or K factors are changed,
10201
except for flow monitors that are exempted from 3-load (or 3-level)
10202
RATA testing
under
Section
6.5.2(b)
or 6.5.2(e) of Exhibit A to this
10203
Appendix. For monitors so exempted under Section 6.5.2(b),
a single-load
10204
flow RATA is required. For monitors so exempted under Section 6.5.2(e),
10205
either a single-level RATA or a 2-level RATA is required, depending
on
10206
the number of
operating
levels documented in the monitoring plan for
the
10207
unit.
10208
10209
)
For all multi-level flow audits, the audit points at adjacent load levels
or at
10210
adjacent
operating levels
(e.g., mid and high) must be separated by no less
10211
than 25.0 percent of the “range of operation,” as defined
in Section 6.5.2.1
10212
of Exhibit A to this Appendix.
10213
10214
ci)
A RATA of a
moisture monitoring system must
be performed whenever the
10215
coefficient, K factor or mathematical algorithm determined under Section
6.5.6 of
10216
Exhibit A to this Appendix is changed.
10217
10218
2.3.1.4 Number
of
RATA
Attempts
JCAR350225-08 1 8507r01
10219
10220
The
owner or operator may
perform
as many
RATA
attempts as are
necessary
to
achieve the
10221
desired
relative accuracy test
audit frequencies. However, the data validation procedures in
10222
Section 2.3.2 of this
Exhibit must be followed.
10223
10224
2.3.2
Data
Validation
10225
10226
A
RATA must not commence if the monitoring system is operating out-of-control
10227
with respect to any of the daily and quarterly quality
assurance assessments
10228
required by
Sections 2.1 and 2.2 of this Exhibit or with respect to the additional
10229
calibration error test requirements in Section
2.1.3
of
this Exhibit.
10230
10231
Each required RATA must be done according to
subsection
(b)(1’), (b)(2)
or
(b)(3)
10232
of this
Section:
10233
10234
D
The
RATA may be done “cold”, i.e., with no corrective
maintenance,
10235
repair,
calibration
adjustments,
re-linearization or reprogramming of the
10236
monitoring
system
prior to the test.
10237
10238
The RATA maybe done after
performing
only
the routine or non-routine
10239
calibration adjustments described in Section 2.1.3 of this Exhibit at the
10240
zero
and/or
upscale
calibration gas levels, but no other
corrective
10241
maintenance, repair, re-linearization or reprogramming of
the monitoring
10242
system. Trial RATA runs may be
performed after the calibration
10243
adjustments
and additional
adjustments within
the allowable limits in
10244
Section
2.1.3 of this Exhibit maybe made prior to the RATA, as
10245
necessary, to
optimize
the performance of
the
CEMS.
The trial RATA
10246
runs need not
be reported, provided that they meet the specification for
10247
trial RATA runs in Section
1.4(b)(3)(G)(v)
of this
Appendix. However,
if,
10248
for any trial run, the
specification in Section
(b)(3)(G)(v)
of this Appendix
10249
is not met, the trial run must be counted as
an
aborted
RATA attempt.
10250
10251
The RATA may be done after repair,
corrective maintenance, re
10252
linearization
or
reprogramming of the monitoring system. In this case, the
10253
monitoring system will be considered
out-of-control
from the hour in
10254
which the repair,
corrective maintenance, re-linearization or
10255
reprogramniing is commenced until the RATA has been passed.
10256
Alternatively, the data validation procedures
and associated timelines
in
10257
Sections
1.4(b)(3)(B)
through
(I)
of
this Appendix
maybe
followed
upon
10258
completion of the
necessary repair, corrective maintenance, re
10259
linearization or reprogramming. If the procedures in Section 1.4(b)(3) of
10260
this
Appendix are used, the words “quality assurance” apply
instead
of the
10261
word “recertification”.
JCAR350225-081
8507r01
10262
10263
Once a RATA is commenced, the test
must be done hands-off. No
adjustment
of
10264
the monitor’s calibration is permitted during
the
RATA
test period, other than the
10265
routine
calibration
adjustments following daily calibration error tests, as described
10266
in Section 2.1.3
of
this Exhibit.
If a routine daily calibration error test is
10267
performed and passed just prior to
a
RATA
(or
during a RATA test period) and
a
10268
mathematical correction factor is automatically applied
by the DAHS, the
10269
correction factor must be applied to all subsequent data recorded by the monitor,
10270
including the RATA test data. For 2-level
and 3- level flow monitor audits, no
10271
linearization or reprogramming of the monitor is permitted in between load
levels.
10272
10273
For single-load
(or
single-level) RATAs, if a daily calibration error test is failed
10274
during
a RATA test period, prior to
completing the test, the RATA must be
10275
repeated. Data from the monitor are invalidated prospectively from the hour
of the
10276
failed calibration error test until the hour
of
completion
of a subsequent successful
10277
calibration error test. The subsequent RATA must not be commenced until the
10278
monitor has
successfully passed
a calibration error
test
in accordance with Section
10279
2.1.3 of this
Exhibit.
Notwithstanding these requirements, when ASTM D6784-02
10280
(incorporated
by
reference under
Section
225.140)
or Method 29 in appendix
A-8
10281
to
40 CFR 60, incorporated
by
reference in Section 225.140,
is
used
as the
10282
reference method for the RATA of a mercury CEMS, if
a
calibration error
test of
10283
the CEMS is failed during a RATA test period, any test runs completed prior
to
10284
the failed
calibration error
test need not
be repeated; however, the RATA may
not
10285
continue until a subsequent calibration
error test of the mercury CEMS has been
10286
passed. For multiple-load
(or
multiple-level) flow
RATAs, each load level (or
10287
operating
level)
is treated as a separate RATA
(i.e.,
when a calibration error
test is
10288
failed
prior
to
completing the
RATA at a particular load level (or operating level),
10289
only the RATA at that load level
(or
operating level) must be repeated;
the results
10290
of any
previously-passed RATAs
at the other load levels (or operating levels)
are
10291
unaffected, unless re-linearization of the monitor is required
to
correct
the
10292
problem that caused the calibration
failure, in which case a subsequent 3-load
(or
10293
3-level)
RATA is required), except as otherwise provided in Section 2.3.1.3(c)(5)
10294
of
this Exhibit.
10295
10296
ç
For
a
RATA performed using
the option in subsection
(b)(1)
or (b)(2) of this
10297
Section, if the RATA is failed
(that
is, if the relative
accuracy
exceeds
the
10298
applicable
specification
in Section 3.3 of Exhibit A to this
Appendix)
or if
the
10299
RATA is aborted prior to completion
due to a problem with the CEMS, then
the
10300
CEMS is out-of-control and all emission
data
from
the CEMS are
invalidated
10301
prospectively from the hour in which the RATA is failed
or
aborted.
Data
from
10302
the CEMS
remain invalid
until the hour of completion of
a
subsequent RATA
that
10303
meets the
applicable
specification
in Section 3.3 of Exhibit A to this Appendix.
If
10304
the option in subsection
(b)(3) of this
Section
to use the data validation
JCAR350225-08 1 8507r01
10305
procedures
and
associated
timelines
in
Sections
1 .4(b)(3)(B) through(b)(3)(I)
of
10306
this
Appendix
has been selected,
the beginning and
end of the
out-of-control
10307
period must
be
determined
in
accordance
with
Section 1 .4(b)(3)(G)(i)
and
(ii)
of
10308
this Appendix.
Note that when
a RATA is aborted
for a reason other than
10309
monitoring
system malfunction
(see
subsection (g) of this
Section),
this
does
not
10310
trigger
an
out-of-control
period for the
monitoring system.
10311
10312
fi
For
a 2-level
or
3-level flow RATA,
if, at any load level
(or
operating
level),
a
10313
RATA
is
failed or aborted
due to a
problem
with the flow
monitor, the RATA
at
10314
that
load level
(or
operating
level)
must
be repeated. The flow
monitor is
10315
considered
out-of-control
and data from the
monitor are
invalidated from the
hour
10316
in
which the test is
failed
or aborted and
remain invalid until
the passing of a
10317
RATA
at
the failed
load level
(or operating
level),
unless
the option in subsection
10318
(b)(3)
of this Section
to use the
data
validation
procedures
and associated
10319
timelines
in Section
1.4(b)(3)(B)
through
(b)(3)(I)
of
this
Appendix has been
10320
selected,
in
which
case the beginning
and end of the out-of-control
period
must be
10321
determined in accordance
with Section
1.4(b)(3)(G)(i)
and (ii) of this Appendix.
10322
Flow
RATA(s)
that
were previously passed
at the other load
levels
(or
operating
10323
levelss)
do
not have
to be repeated unless
the flow monitor
must be re-linearized
10324
following
the failed or aborted
test. If the flow
monitor is re-linearized,
a
10325
subsequent
3-load
(or
3-level)
RATA is
required,
except
as otherwise
provided in
10326
Section
2.3.1.3(c)(5)
of this
Exhibit.
10327
10328
g
For each
monitoring
system,
report
the results of all completed
and
partial
10329
RATAs
that
affect
data
validation
(i.e.,
all
completed,
passed
RATAs
all
10330
completed, failed RATAs
and all
RATAs aborted due
to a problem with the
10331
CEMS,
including
trial RATA runs counted
as failed test attempts
under
10332
subsection (b)(2) of
this Section or under
Section
1.4(b)(3)(G)(vi))
in the
10333
quarterly
report
rejuired under 40 CFR
75.64, incorporated
by
reference
in
10334
Section
225.140. Note
that RATA attempts
that
are aborted
or invalidated due
to
10335
problems
with
the
reference method or
due
to operational problems
with
the
10336
affected units need not
be reported.
Such runs do not affect
the validation status
of
10337
emission
data
recorded
by
the CEMS.
However, a
record
of
all RATAs,
trial
10338
RATA runs and RATA
attempts
(whether
reported
or not)
must be kept on-site
as
10339
part
of the
official
test log for each monitoring
system.
10340
10341
Each
time that a
hands-off RATA of
a
mercury concentration
monitoring system,
10342
a
sorbent
trap
monitoring
system, or a flow
monitor is passed,
perform
a
bias
test
10343
in accordance
with
Section
7.4.4 of Exhibit A
to
this Appendix.
10344
10345
j)
Failure of the
bias
test
does not result
in the monitoring
system being
out-of
10346
control.
10347
JCAR350225-081 8507r01
10348
2.3.3 RATA Grace
Period
10349
10350
The owner or operator has
a grace
period
of 720 consecutive unit operating
hours,
10351
as defined in 40 CFR 72.2, incorporated
by reference in Section 225.140
(or,
for
10352
CEMS installed on common stacks or bypass stacks,
720 consecutive stack
10353
operating
hours,
as defined in 40 CFR
72.2),
in which
to
complete
the required
10354
RATA for a
particular
CEMS whenever:
10355
10356
fl
A
required
RATA has not been performed
by the end of the
QA
operating
10357
quarter in which it
is due; or
10358
10359
A required 3-load
flow RATA has not been performed
by
the end of
the
10360
calendar
quarter in which it is due.
10361
10362
j)
The
grace
period
will begin with the first unit
(or stack)
operating hour following
10363
the calendar quarter in which the required RATA
was due. Data
validation
during
10364
a
RATA grace
period must be done in accordance with the applicable provisions
10365
in Section 2.3.2 of this Exhibit.
10366
10367
ci
If, at
the end of the 720
unit
(or
stack)
operating hour grace period, the RATA
has
10368
not been completed, data
from the
monitoring
system will be invalid, beginning
10369
with the first unit operating hour following
the expiration of the grace period.
10370
Data from the CEMS remain invalid until the hour
of completion of a subsequent
10371
hands-off RATA. The deadline for the next test will
be
either two
QA
operating
10372
quarters
(if
a
semiannual RATA frequency is
obtained)
or four
OA
operating
10373
quarters
(if
an annual RATA frequency is
obtained) after the quarter in which
the
10374
RATA is completed, not to exceed eight calendar
quarters.
10375
10376
When a RATA is done during a grace period in order
to satisfy a RATA
10377
requirement from
a
previous
quarter, the deadline for the next RATA must
be
10378
determined as follows:
10379
10380
1)
If the
grace
period RATA qualifies for a reduced, (i.e., annual),
RATA
10381
frequency the deadline
for
the
next
RATA will be set at three
QA
10382
operating quarters after the
quarter
in which the grace period
test
is
10383
completed.
10384
10385
)
If the grace period RATA qualifies for the
standard, (i.e., semiannual),
10386
RATA
frequency the deadline
for the next RATA will be set
at two
OA
10387
operating quarters
after the quarter in which the grace period test is
10388
completed.
10389
10390
Notwithstanding
these requirements, no more than eight successive
JCAR350225-081 8507r01
10391
calendar quarters must
elapse
after the quarter in which the grace period
10392
test is completed, without a subsequent RATA having been conducted.
10393
10394
2.4
Recertification, Quality Assurance, and RATA Frequency
(Special
Considerations)
10395
10396
When a significant change is made to a monitoring system
such
that
10397
recertification of the monitoring system is required in accordance with Section
10398
1.4(b)
of this Appendix, a recertification test (or tests) must be perfonned to
10399
ensure that the CEMS continues to generate valid data. In
all
recertifications, a
10400
RATA
will
be one
of
the required tests; for some recertifications, other tests
will
10401
also be required. A recertification test may be used to satisfy the quality assurance
10402
test
requirement of this Exhibit. For example, if, for a particular change made
to a
10403
CEMS, one of the required recertification tests is a linearity
check
and the
10404
linearity check is successful, then, unless another recertification event occurs in
10405
that same
QA
operating quarter, it would not be necessary to
perform an
10406
additional linearity test of the CEMS in that
quarter
to meet the quality assurance
10407
requirement of Section
2.2.1
of this
Exhibit.
For this
reason, EPA recommends
10408
that
owners
or operators coordinate
component
replacements,
system
upgrades,
10409
and other events that may require recertification, to the extent practicable, with
10410
the periodic
quality
assurance testing required by
this Exhibit. When a quality
10411
assurance
test is done for the dual purpose
of
recertification and routine quality
10412
assurance, the applicable data validation procedures in Section
1.4(b)(3)
must be
10413
followed.
10414
10415
)
Except as provided in
Section 2.3.3
of this Exhibit,
whenever a passing RATA
of
10416
a gas
monitor is performed, or a passing 2-load
(or 2-level)
RATA or a passing
3-
104 17
load
(or
3-level) RATA of a flow monitor is performed (irrespective of whether
10418
the RATA is
done to satisfy
a recertification
requirement or to meet the quality
10419
assurance requirements of this Exhibit, or
both),
the RATA frequency
(semi-
10420
annual or
annual)
must be
established based
upon the date and time of completion
10421
of the RATA and the relative accuracy percentage obtained. For 2-load
(or
2-
10422
level)
and
3-load
(or
3-level) flow RATAs, use the highest percentage relative
10423
accuracy at any of the loads
(or levels)
to determine the
RATA
frequency. The
10424
results of a
single-load
(or single-level)
flow RATA may be used to establish the
10425
RATA frequency when the single-load
(or
single-level)
flow RATA
is
10426
specifically
required under
Section
2.3.1.3(b) of this Exhibit or when the single-
10427
load
(or
single-level) RATA is allowed under Section 2.3.1.3(c) of this Exhibit for
10428
a unit that has operated at one load level
(or
operating
level)
for
85.0
percent of
10429
the time since the
last
annual flow RATA. No other
single-load (or single-level)
10430
flow RATA may
be used
to establish
an annual RATA frequency; however,
a
2-
10431
load
or 3-load (or a 2-level
or
3-level) flow RATA may be performed at any time
10432
or in
place
of any required single-load
(or single-level)
RATA, in order to
10433
establish an annual RATA frequency.
JCAR350225-08 1 8507r01
10434
10435
2.5 Other Audits
10436
10437
Affected units
may
be subject to
relative accuracy test
audits at any time. If a monitor or
10438
continuous
emission monitoring
system
fails the relative accuracy
test
during the
audit,
the
10439
monitor
or continuous emission monitoring
system
will be considered to be out-of-control
10440
beginning with the date and time of completion of the audit, and continuing until a successful
10441
audit test is
completed following corrective action.
10442
10443
2.6
System Integrity Checks for Mercury Monitors
10444
10445
For
each mercury concentration monitoring system (except for a mercury monitor that does not
10446
have a
converter),
perform a single-point
system
integrity check weekly, i.e., at least once
every
10447
168 unit or stack
operating hours,
using a
NIST-traceable
source of oxidized mercury. Perform
10448
this check
using
a mid- or high-level gas concentration, as defined in Section 5.2 of Exhibit
A to
10449
this
Appendix. The
performance
specifications
in
subsection
(3)
of Section
3.2
of Exhibit A to
10450
this
Appendix must
be met, otherwise the monitoring
system
is considered out-of-control,
from
10451
the hour
of the failed check until a subsequent system integrity check is passed. If a required
10452
system integrity
check is not performed and passed within 168 unit or stack operating
hours of
10453
last
successful check, the monitoring system will also be considered out of control, beginning
10454
with the
169th unit or stack operating hour after the last successful check, and continuing until
a
10455
subsequent system integrity check is passed. This weekly check is not required if the daily
10456
calibration assessments
in Section 2.1.1 of this Exhibit are performed using
a NIST-traceable
10457
source
of oxidized
mercury.
10458
10459
[Note: The
following TABLE/FORM is too wide to be displayed on one screen. You must print
10460
it for a
meaningful
review
of
its contents. The table has been divided into multiple
pieces with
10461
each piece
containing information to help you assemble a printout of the table. The information
10462
for each
piece
includes: (1)
a
three line message preceding the tabular
data showing by line
#
and
10463
character
#
the
position of the upper left-hand corner of the piece and the position of the piece
10464
within
the entire
table; and
(2)
a numeric scale following the tabular data displaying the
character
10465
positions.]
10466
10467
Figure 1 for
Exhibit B of Appendix B Part 75. — Qaulity Assurance Test Requirements
Basic
QA
test frequency requirements
FFN*]
Daily
Quarterly
Semiannual
[FN*]
Weekly
[FN*1
FFN*1
Annual
Calibration
Error
Test
(2
Pt.)
/
JCAR350225-08
1
8507r01
Interference
Check
(flow)
/
Flow-to-Load
Ratio
/
Leak Check
(DP
flow
monitors)
/
Linearity
Check or System
Integrity Check
[FN**]
(3
pt.)
Single-point System
Integrity
/
Check
FFN**1
RATA
(SO
2,
NOXQ
/
O)
[FN11
RATA
(All Hg monitoring
/
systems)
RATA
(flow)
[FN1J
[FN21
/
10468
10469
[FN*1
“Daily”
means operating days, only.
“Weekly”
means
once every 168 unit or stack
10470
operating hours.
“Quarterly”
means once every QA operating
quarter.
“Semiannual”
means
10471
once every two
QA
operating quarters. “Annual” means once every four
QA
operating
10472
quarters.
FFN**1
The system integrity check applies
only
to Hg monitors with converters.
10473
The
single-point weekly system integrity check is not required if
daily calibrations
are
10474
performed
using a NIST-traceable
source
of
oxidized
Hg.
The 3-point quarterly system
10475
integrity check is not
required if a linearity check is
performed.
10476
10477
[FN11
Conduct RATA
annually
(i.e.,
once every four QA operating quarters), if monitor
10478
meets
accuracy requirements to qualify for less frequent testing.
FFN21
For flow monitors
10479
installed on peaking units,
bypass stacks, or units that qualify for
single-level
RATA
testing
10480
under
Section
6.5.2(e)
of this
part,
conduct all RATAs at a
single, normal load
(or
operating
10481
level).
For other
flow monitors, conduct annual RATAs at two load levels (or operating
10482
levels).
Alternating
single-load
and
2-load
(or
single-level
and
2-level)
RATAs may
be done
10483
if a
monitor is on a
semiannual frequency. A single-load
(or
single-level) RATA may be
10484
done in lieu
of a 2-load
(or
2-level) RATA if, since the last
annual flow RATA, the
unit has
10485
operated at one load
level
(or
operating
level)
for
85.0 percent of the time. A 3-level
10486
RATA is required
at least once every five calendar years and
whenever
a flow monitor is re
10487
linearized,
except for flow monitors exempted from 3-level RATA testing
under
Section
10488
6.5.2(b)
or
6.5.2(e)
of Exhibit A to this Appendix.
10489
10490
10491
Figure
2 for Exhibit B of
Appendix
B
— Relative
Accuracy Test
Frequency Incentive
System
10492
JCAR350225-081 8507r01
RATA
Semiannual
[FNW1
(percent)
Annual FFNW1
SQ2
orNOx
[FNY1
7.5% <RA lO.0% or* 15.0 ppm
RA 7.5% or± 12.0
ppm
[FNX1
FFNX1.
Q
2
-diluent
7.5%
<RA
10.0% or ± 0.030
RA
7.5% or ± 0.025
lb/mmBtu FFNX1
lb/mmBtu =G5X.
NOx-diluent
7.5% <RA
10.0% or
± 0.020
RA
7.5%
or
± 0. 015
lb/mmBtu
FFNX]
lb/mmBtu [FNX].
Flow
7.5% <RA 10.0% or± 2.0
fps
RA 7.5% or± 1.5
fps
[FNX]
[FNX1.
C0
2
or02
7.5%<RA 10.0%or± 1.0
RA
7.5%or±0.7%
cQLQ2
FFNX1
cQLQ2
FFNX1.
HgFFNX1
N/A
RA<20.0%or±l.0
<<mu>>g/scm
FFNX1.
Moisture
7.5%<RA
10.0%or± 02
1.5%H RA
7.5%or± 1.0%H
20
[FNX1
FFNX].
10493
10494
[FNW]
The deadline for the next RATA
is the end of the second (if semiannual)
or fourth
(if
10495
annual)
successive
QA
operating quarter
following the quarter in which the CEMS
was last
10496
tested. Exclude calendar quarters with fewer than 168 unit
operating hours
(or,
for comi-non
10497
stacks
and bypass stacks, exclude quarters
with fewer than 168 stack operating
hours)
in
10498
determining the RATA deadline. For
2
SO
monitors,
QA
operating quarters in which
only
10499
very
low sulfur fuel as defined in 40
CFR 72.2, incorporated by reference
in Section
10500
225.140, is combusted may also be excluded. However, the exclusion
of calendar
quarters
is
10501
limited as follows: the deadline for the next
RATA will be no more than
8
calendar
quarters
10502
afler the
quarter in which a RATA
was last
performed.
FFNX]
The difference between
10503
monitor_and_reference method mean values
applies to moisture monitors,
CO2.and
02
10504
monitors,
low emitters
of SO
2,
NON,
or H, or and low flow,
only. The specifications for
Hg
10505
monitors also apply to sorbent trap monitoring
systems.
[FWY1
A
NOx
concentration
10506
monitoring system used to determine
NO
mass emissions
under 40 CFR 75.71,
10507
incorporated
by
reference in Section
225.140.
JCAR350225-081 8507r01
10508
10509
Exhibit
C to Appendix
B--Conversion Procedures
10510
10511
1.
Applicability
10512
10513
Use
the
procedures in this
Exhibit
to convert measured
data from a
monitor or continuous
10514
emission monitoring
system
into the appropriate
units of the standard.
10515
10516
2.
Procedures for Heat
Input
10517
10518
Use the
following
procedures to compute
heat input
rate
to an affected
unit
(in
mmBtu/hr or
10519
mmBtu/day):
10520
10521
2.1
10522
10523
Calculate and
record heat input
rate
to an affected unit
on an hourly basis.
The owner or operator
10524
may
choose to
use the
provisions
specified
in
40
CFR
75.16(e),
incorporated
by
reference
in
10525
Section 225.140,
in
conjunction
with the
procedures
provided
in Sections
2.4 through 2.4.2
to
10526
apportion
heat
input among each unit
using
the common
stack or common pipe
header.
10527
10528
2.2
10529
10530
For an affected
unit that
has a flow monitor
(or
approved
alternate
monitoring system under
10531
subpart E of
40 CFR 75, incorporated
by reference
in Section
225.140,
for measuring volumetric
10532
flow
rate)
and
a diluent gas
(02
or
CO)
monitor, use
the
recorded
data
from
these monitors
and
10533
one of
the following
equations
to calculate hourly
heat input rate
(in mmBtu/hr).
10534
10535
2.2.1
10536
10537
When
measurements
of CO2
concentration
are on a wet
basis,
use the
following equation:
10538
1%CO
10539
HI=Q
—
2w
WF
100
(EquationF-15)
10540
10541
Where:
10542
HI
Hourly
heat input rate during
unit operation, mmBtulhr.
=
Hourly average volumetric
flow rate during
unit
operation,
wet
basis, seth.
= Carbon-based F-factor,
listed
in Section
3.3.5 of appendix
F
to
40 CFR 75
for
each
fuel, scf/mmBtu.
%çQ
Hourly concentration
of 2
CO during
unit operation, percent
JCAR350225-081
8507r01
CO2
wet
basis.
10543
10544
10545
2.2.2
10546
10547
When
measurements
of CO2 concentration
are on
a
dry basis,
use
the
following
equation:
10548
10549
HI
= Qhr
(100 — %H2
0)
%C02d
(Equation
F-
16)
L
100F
]
100
J
10550
10551
Where:
10552
ffl
Hourly heat input rate
during unit operation,
mmBtu/hr.
Hourly
average
volumetric
flow rate during
unit operation,
wet
basis, scfh.
F
Carbon-based
F-factor,
listed
in Section 3.3.5
of appendix
F to 40
CFR 75 for each fuel,
scf/mniBtu.
%CO
Hourly
concentration
of
7
CO
during unit
operation, percent
wet
basis.
=
Moisture content of
gas in the stack, percent.
10553
10554
2.2.3
10555
10556
When measurements
of
02
concentration
are on a wet basis,
use
the following
equation:
10557
10558
HI
= Q__[(20.9/100X100/H
2
O)%O
2
Wl
(Equation
F-17)
10559
10560
Where:
10561
HI
Hourly
heat input rate during
unit operation,
mmBtu/hr.
= Hourly
average volumetric
flow rate
during
unit operation, wet
basis,
scth.
F
Carbon-based
F-factor, listed
in Section 3.3.5 of
appendix F to 40 CFR
75
for each
fuel, scf/mmBtu.
Hourly
concentration
of
02
during unit operation,
percent
O
wet basis.
= Hourly average
stack
moisture
content,
percent
by volume.
10562
10563
2.2.4
10564
10565
When
measurements of
O
concentration are
on a
dry
basis,
use the following
equation:
JCAR350225-081
8507r01
10566
10567
HI
= Qw[(b00l20)1[(20.902u]
(Equation
F-18)
10568
10569
Where:
10570
ffl
Hourly
heat
input rate
during unit
operation, mmBtu/hr.
=
Hourly
average
volumetric flow
during unit operation,
wet basis,
scfh.
F
=
Dry basis F-factor, listed
in Section
3.3.5 of appendix F
to 40
CFR
75 for
each
fuel,
dscf/mmBtu.
= Moisture
content
of the
stack
gas, percent.
=
Hourly concentration
of
02
during
unit operation, percent
Ocy
basis.
10571
10572
10573
10574
Heat Input
Summation
(for
Heat Input
Detennined Using
a Flow Monitor
and Diluent
Monitor)
10575
10576
2.3.1
10577
10578
Calculate total
quarterly heat
input
for a unit
or common stack using
a flow monitor
and diluent
10579
monitor to
calculate heat input,
using
the
following
equation:
10580
10581
HIq = HI
1t
(Equation
F-18a)
hour—I
10582
10583
Where:
10584
HIq
= Total heat
input for
the quarter, mmBtu.
HI
=
Hourly heat input
rate during unit
operation, using
Equation F-15, F
16, F-17, orF-18,
mmBtu/hr.
tj
Hourly operating
time
for the unit
or common
stack, hour or fraction
of
an hour
(in
equal
increments
that can range from
one
hundredth
to
one quarter
of an hour,
at
the option of the owner
or operator).
10585
10586
2.3.2
10587
10588
Calculate
total
cumulative
heat input for
a unit or common
stack using
a
flow
monitor and
10589
diluent
monitor
to
calculate heat input,
using
the following
equation:
10590
JCAR350225-08 1 8507r01
HI =
the — current — quarter
HIq
q=1
10591
10592
10593
10594
10595
10596
10597
10598
10599
10600
10601
10602
10603
10604
10605
10606
10607
10608
10609
10610
(Equation F-i 8b
Where:
HI
= Total heat input
for the quarter, mmBtu.
HIq
Total
heat
input
for the quarter, mmBtu.
2.4 Heat Input Rate Apportionment
for
Units
Sharing a Common Stack or Pipe
2.4.1
Where applicable, the owner or operator of an affected
unit that determines heat input rate at the
unit
level by apportioning the heat input monitored at a common
stack or common pipe using
megawatts must
apportion
the heat input rate using the following
equation:
(Equation
F-2 1
a)
Where:
HI
= Heat input rate
for a unit, mmBtu/hr.
HI
= Heat
input
rate
at
the
common stack or pipe, mmBtu/hr.
MW
= Gross electrical output,
MWe.
tj
= Unit operating time, hour or fraction
of an hour (in equal
increments that can range from one
hundredth
to
one quarter of
an hour, at the option of the owner
or operator).
tCS
= Common stack or common pipe
operating time, hour or
fraction of an hour
(in
equal
increments that
can range from
one
hundredth
to
one quarter of an hour, at the option
of
the
owner or
operator).
n
Total number
of
units
using
the
common stack or pipe.
i
= Designation of a particular unit.
2.4.2
JCAR350225-08 1
8507r01
10611
10612
Where applicable,
the
owner
or
operator of
an affected unit that
determines the
heat input rate
at
10613
the unit
level
by
apportioning
the heat input
rate monitored at
a common stack or common
pipe
10614
using
steam
load must apportion
the heat
input
rate
using
the following
equation:
10615
10616
(Equation
F-21b)
10617
10618
Where:
10619
HI
= Heat
input
rate for a unit, mmBtu/hr.
HIcs
= Heat
input
rate at the common
stack or
pipe,
mmBtu/hr.
SF = Gross
steam load, lb/hi,
or mmBtu/hr.
tj
= Unit
operating time,
hour or fraction of an
hour (in equal
increments
that
can range
from one
hundredth
to
one quarter
of
an hour,
at the
option
of the owner or
operator).
= Common
stack or common
pipe operating time,
hour or
fraction of
an hour
(in
equal increments
that
can range from
one
hundredth
to
one quarter of an
hour, at
the
option of the
owner or operator).
n
= Total
number of units using
the common
stack or pipe.
i
= Designation
of a particular
unit.
10620
10621
2.5
Heat Input
Rate Summation
for Units with Multiple
Stacks or
Pipes
10622
10623
The
owner or
operator
of an
affected unit that
determines the heat
input rate at
the unit level
by
10624
summing
the
heat
input rates
monitored at
multiple stacks or
multiple pipes must
sum the heat
10625
input
rates
using the following
equation:
10626
—
HIt
10627
—
(Equation
F-21c)
tunit
10628
10629
Where:
10630
Heat
input
rate for
a unit, mmBtu/hr.
JCAR350225-08 1 8507r01
= Heat input rate
for the individual stack, duct, or
pipe,
mmBtulhr.
Unit operating
time, hour or fraction
of the hour (in equal
increments
that can range from one hundredth to one quarter
of an hour, at the option
of the owner or operator).
t
5
= Operating time for the individual
stack or pipe, hour or
fraction
of the hour
(in
equal increments
that
can range from
one
hundredth
to
one quarter of an hour, at the option
of the
owner or operator).
s
= Designation
for a particular
stack, duct, or pipe.
10631
10632
3. Procedure for Converting
Volumetric Flow to STP
10633
10634
Use the following
equation
to convert volumetric flow
at actual temperature and pressure to
10635
standard
temperature
and pressure.
10636
10637
FSTP = FActual (TSfd
I
TStack
XStack /Sd)
(Equation
F-22)
10638
10639
Where:
10640
= Flue gas volumetric
flow rate at standard temperature
and
pressure, scth.
Ectuai
Flue gas volumetric flow
rate at actual
temperature
and
pressure, acth.
Tst
= Standard
temperature 528 degreesR.
ISCk
= Flue
gas temperature at flow monitor location,
degreesR,
where degreesR = 460
+
degreesF.
SCk
= The absolute
flue gas pressure = barometric pressure
at the
flow monitor location
+
flue
gas static pressure, inches of
mercury.
P
5t
The absolute flue gas pressure
= barometric pressure at the
flow monitor location
+
flue gas static pressure, inches
of
mercury.
10641
10642
4. Procedures
for
Mercury
Mass Emissions.
10643
10644
4.1
10645
10646
Use
the procedures
in this Section
to calculate the hourly mercury
mass emissions
(in
ounces)
at
10647
each
monitored
location
for the affected
unit or group of units that discharge
through a common
10648
stack.
JCAR350225-08 1 8507r01
10649
10650
4.1.1
10651
10652
To
determine the hourly mercury mass emissions when
using a
mercury concentration
10653
monitoring system that measures on a wet basis and a flow monitor, use the following equation:
10654
10655
Mh —KChQhth
(Equation F-28)
10656
10657
Where:
10658
Mb
Mercury mass emissions
for
the hour rounded off to
three
decimal places
(ounces).
K = Units conversion constant, 9.978 x 1
0b0
oz-scm/ig-scf.
Hourly mercury concentration, wet basis,
adjusted
for bias if the bias-test
procedures in Exhibit A
to
this Appendix show that
a
bias-adjustment
factor
is necessary,
(ig/wscm).
Qh
= Hourly stack gas volumetric
flow rate,
adjusted
for bias,
where the
bias-test
procedures in Exhibit A to this Appendix shows a bias-adjustment factor
is
necessary,
(scifi).
Unit or stack operating time, as defined in 40 CFR 72.2,
(hr.).
10659
10660
4.1.2
10661
10662
To determine
the hourly mercury mass emissions when using a mercury concentration
10663
monitoring system that
measures on
a
dry
basis or a sorbent trap monitoring system and a flow
10664
monitor, use the
following
equation:
10665
10666
Mh = KChQhth
(1—
B)
(Equation F-29)
10667
10668
Where:
10669
Mb
= mercury mass
emissions
for the hour rounded off to three decimal places
(ounces).
K
= Units
conversion
constant, 9.978 x
10b0
oz-scm/<<mu>>g-scf.
Hourly mercury
concentration,
dry basis,
adjusted
for bias if the bias-test
procedures
in Exhibit A to
this
Appendix
show that a bias-adjustment
factor is necessary, (jig/dscm). For sorbent
trap
systems,
a
single value
of
Ch
(i.e.,
a flow-proportional average concentration for the data collection
period) is
applied
to each hour in the data collection period for a particular
pair
of traps.
JCAR350225-08 1 8507r01
Qh
= Hourly stack
gas volumetric
flow
rate,
adjusted
for bias, where the bias-
test
procedures
in Exhibit
A to this Appendix shows
a
bias-adjustment
factor is necessary,
(seth).
Moisture fraction
of
the stack
gas expressed as a decimal (equal to
%H
20
100)
th
= Unit or stack operating
time as defined in 40 CFR 72.2, (hr.).
10670
10671
4.1.3
10672
10673
For
units
that are demonstrated
under Section 1.15(d) of this
Appendix to emit less than 464
10674
ounces of mercury per year, and for which
the owner or operator elects not to continuously
10675
monitor the mercury concentration,
calculate the hourly mercury
mass emissions using Equation
10676
F-28 in Section 4.1 .1 of this Exhibit, except
that
“Ch”
will be the applicable default mercury
10677
concentration from Section 1.15(c),
(d),
or (e) of this Appendix, expressed
in jig/scm. Correction
10678
for the stack gas moisture content is not required when
this methodology is used.
10679
10680
4.2
10681
10682
Use the following equation to calculate
quarterly and year-to-date mercury mass
emissions in
10683
ounces:
10684
10685
Mtime
period
=
(Equation F-30)
10686
10687
Where:
10688
Mtime period
= Mercury mass
emissions
for the given time
period, i.e., quarter or
year-
to-date rounded
to the nearest
thousandth.
(ounces).
Mercury mass emissions for the
hour rounded to three decimal
places
(ounces).
n
The number of hours
in the given time period (quarter or
year-to-date).
10689
10690
4.3 If heat input rate monitoring is required,
follow
the applicable procedures
for heat input
10691
apportionment and summation in Sections 2.3, 2.4
and
2.5
of this Exhibit.
10692
10693
5. Moisture Determination
From Wet and Dry
O
Readings
10694
10695
If a
correction for the stack gas moisture content
is required in any of the emissions or
heat
input
10696
calculations
described in this Exhibit,
and if the hourly moisture
content is determined from
wet-
10697
and
dry-basis
02
readings, use Equation
F-3 1 to calculate the percent
moisture, unless a “Kr’
10698
factor
or other mathematical algorithm is
developed as described in Section
6.5.6(a)
of Exhibit A
JCAR350225-081
8507r01
10699
to this
Appendix:
10700
10701
%H
20
= (02d—02W)
x
100
(Equation
F-31)
10702
10703
Where:
10704
ll2O
Hourly
average stack
gas moisture content,
percentH20
= Dry-basis
hourly average
oxygen
concentration,
percent
02
=
Wet-basis hourly average
oxygen concentration,
percent
02
10705
10706
Exhibit
D
to Appendix
B
— Quality
Assurance
and
Operating
Procedures for Sorbent
Trap
10707
Monitoring
Systems
10708
10709
1.0 Scope
and Application
10710
10711
This Exhibit
specifies sampling,
and analytical,
and
quality-assurance
criteria
and procedures
for
10712
the
performance-based
monitoring of vapor-phase
mercury (Hg)
emissions in
combustion flue
10713
gas
streams,
using a
sorbent
trap monitoring system
(as
defined
in Section
225.130).
The
10714
principle employed
is
continuous
sampling using
in-stack
sorbent
media
coupled
with
analysis
of
10715
the
integrated
samples. The
performance-based
approach of this Exhibit
allows for
use
of various
10716
suitable
sampling
and
analytical
technologies while
maintaining
a
specified and documented
10717
level of data
quality
through performance
criteria. Persons
using this
Exhibit
should have a
10718
thorough
working
knowledge of Methods
1, 2, 3,
4
and 5
in appendices A-i
through A-3 to 40
10719
CFR 60,
incorporated
by
reference in Section
225.140,
as
well as the
determinative technique
10720
selected for
analysis.
10721
10722
1.1 Analytes
10723
10724
The
analyte
measured by
these procedures
and
specifications
is total
vapor-phase
mercury in the
10725
flue gas,
which
represents
the sum of elemental
mercury
(Hg°, CAS Number
7439-97-6)
and
10726
oxidized forms
of mercury,
in mass concentration
units of micrograms
per
dry standard cubic
10727
meter
(pg/dscm).
10728
10729
1.2
Applicability
10730
10731
These
performance
criteria
and procedures
are applicable to monitoring
of vapor-phase
mercury
10732
emissions
under
relatively
low-dust conditions
(i.e.,
sampling in the
stack
after all
pollution
10733
control
devices),
from coal-fired
electric utility steam
generators
which are subject to Sections
10734
1.14
through 1.18
of Appendix B.
Individual
sample
collection
times
can range
from
30 minutes
10735
to several
days
in
duration,
depending
on the mercury
concentration in the
stack. The monitoring
10736
system
must
achieve the
performance
criteria
specified
in
Section 8 of
this Exhibit and the
10737
sorbent
media
capture
ability
must not
be exceeded.
The
sampling rate must
be maintained at a
1CAR350225-081
8507r01
10738
constant proportion
to the total stack flow
rate to ensure
representativeness
of the sample
10739
collected. Failure
to achieve certain
performance
criteria will
result in
invalid mercury
emissions
10740
monitoring
data.
10741
10742
2.0
Principle
10743
10744
Known
volumes
of
flue gas
are
extracted from
a stack
or
duct through paired,
in-stack, pre
10745
spiked
sorbent
media
traps
at an appropriate
nominal flow rate.
Collection
of
mercury
on the
10746
sorbent media in the stack
mitigates
potential
loss
of mercury
during
transport
through
a
10747
probe/sample
line. Paired
train
sampling
is required to
determine measurement
precision
and
10748
verify acceptability of
the measured emissions
data.
10749
10750
The sorbent traps are
recovered from the sampling
system,
prepared for analysis,
as needed,
and
10751
analyzed by
any suitable determinative
technique
that can meet
the performance
criteria. A
10752
section of each sorbent
trap is spiked with Hg°
prior
to sampling.
This section
is analyzed
10753
separately
and the recovery
value is
used
to correct the individual
mercury sample
for
10754
measurement bias.
10755
10756
3.0 Clean
Handling and Contamination
10757
10758
To avoid mercury
contamination
of
the
samples,
special
attention should
be paid to cleanliness
10759
during transport,
field handling,
sampling, recovery,
and laboratory analysis,
as
well
as
during
10760
preparation
of
the sorbent cartridges.
Collection
and
analysis
of blank
samples (field,
trip, lab)
is
10761
useful
in
verifying the absence
of contaminant
mercury.
10762
10763
4.0 Safety
10764
10765
4.1
Site hazards
10766
10767
Site
hazards must be thoroughly
considered
in advance
of
applying these
10768
procedures/specifications
in the field;
advance
coordination with
the site is critical
to
understand
10769
the
conditions and
applicable
safety
policies.
At a minimum, portions
of the sampling
system
10770
will be hot,
requiring appropriate
gloves,
long sleeves, and caution
in handling this
equipment.
10771
10772
4.2 Laboratory
safety policies
10773
10774
Laboratory
safety
policies
should
be
in
place to minimize risk
of chemical exposure
and to
10775
properly
handle waste
disposal. Personnel
must
wear appropriate
laboratory attire
according
to
a
10776
Chemical
Hygiene
Plan established by
the laboratory.
10777
10778
4.3
Toxicity or carcinogenicity
10779
10780
The
toxicity
or carcinogenicity
of any reagents
used must be considered.
Depending
upon
the
JCAR350225-0818507r01
10781
sampling and
analytical technologies
selected,
this
measurement may
involve hazardous
10782
materials,
operations, and equipment
and this
Exhibit does not address
all of the safety
problems
10783
associated with
implementing
this approach.
It
is the responsibility of
the
user
to
establish
10784
appropriate
safety and health practices
and determine
the applicable
regulatory limitations
prior
10785
performance.
Any chemical should
be regarded as a
potential health
hazard and exposure
to
10786
these
compounds
should be
minimized.
Chemists
should
refer to the Material
Safety
Data
Sheet
10787
(MSDS)
for each
chemical used.
10788
10789
4.4
Wastes
10790
10791
Any
wastes
generated
by this procedure must
be
disposed
of according to a hazardous
materials
10792
management
plan that
details and tracks
various waste streams
and
disposal
procedures.
10793
10794
5.0 Equipment
and Supplies
10795
10796
The
following list is
presented as an example
of key equipment
and supplies
likely required to
10797
perform
vapor-phase
mercury monitoring using
a
sorbent
trap monitoring system.
It
is
10798
recognized
that
additional
equipment
and
supplies may be needed.
Collection
of paired samples
10799
is
required.
Also
required
are a certified stack
gas
volumetric
flow monitor that
meets the
10800
requirements
of Section
1.2
to this
Appendix
and an
acceptable
means of
correcting for the
stack
10801
gas
moisture
content, i.e.,
either
by
using data
from a certified continuous
moisture
monitoring
10802
system or
by
using an
approved
default moisture
value
(see
40
CFR
75.11(b),
incorporated
by
10803
reference in Section
225.140).
10804
10805
5.1 Sorbent
Trap Monitoring
System
10806
10807
A
typical
sorbent
trap monitoring system
is shown in
Figure K-i. The monitoring
system must
10808
include the
following
components:
10809
10810
5.1.1 Sorbent Traps
10811
10812
The
sorbent
media used
to
collect
mercury must be configured
in a trap
with three distinct and
10813
identical
segments
or sections, connected
in series,
that
are amenable to separate
analyses.
10814
Section
1 is
designated
for
primary
capture of gaseous mercury.
Section
2 is designated as
a
10815
backup
section
for
determination of vapor-phase
mercury
breakthrough. Section
3 is designated
10816
for
OAIOC
purposes
where
this
section
must be spiked with
a known amount
of
gaseous
Hg°
10817
prior to
sampling and
later analyzed to
determine recovery efficiency.
The
sorbent media may
be
10818
any
collection
material
(e.g.,
carbon,
chemically-treated
filter, etc.)
capable
of
quantitatively
10819
capturing and
recovering
for subsequent
analysis, all gaseous
forms of mercury for
the intended
10820
application.
Selection of the
sorbent media
must
be based on the
material’s ability
to achieve
the
10821
performance
criteria
contained
in Section 8 of this
Exhibit as well as
the sorbent’s
vapor-phase
10822
mercury
capture
efficiency for
the emissions matrix
and the expected
sampling duration
at the
10823
test
site. The
sorbent media must be
obtained
from
a
source that can demonstrate
the quality
JCAR350225-08
1
8507r01
10824
assurance and control necessary to ensure consistent
reliability. The paired sorbent traps are
10825
supported on a probe
(or
probes) and inserted directly
into the flue
gas
stream.
10826
10827
5.1.2 Sampling
Probe
Assembly
10828
10829
Each probe assembly must have a leak-free Exhibit to
the sorbent
traps.
Each sorbent trap must
10830
be mounted at the
entrance
of or
within
the probe such that the gas sampled enters the
trap
10831
directly. Each probe/sorbent trap assembly must
be heated to a temperature sufficient to prevent
10832
liquid condensation in the sorbent traps. Auxiliary heating
is
required
only where the stack
10833
temperature is too
low to prevent condensation.
Use a calibrated thermocouple to monitor
the
10834
stack
temperature. A single probe capable of operating
the paired
sorbent
traps may be used.
10835
Alternatively,
individual probe/sorbent
trap assemblies may be used, provided that the individual
10836
sorbent traps are co-located to ensure representative
mercury
monitoring
and are sufficiently
10837
separated to
prevent aerodynamic interference.
10838
10839
5.1.3 Moisture
Removal Device
10840
10841
A robust moisture
removal device or
system, suitable for continuous duty
(such
as a Peltier
10842
cooler),
must be used to remove water vapor from the
gas stream prior to entering the gas flow
10843
meter.
10844
10845
5.1.4
Vacuum Pump
10846
10847
Use a
leak-tight, vacuum pump capable of operating within
the
candidate
system’s flow range.
10848
10849
5.1.5 Gas Flow Meter
10850
10851
A gas
flow meter (such as a
dry
gas meter, thermal mass flow meter, or other suitable
10852
measurement
device)
must be used to determine the
total sample volume on a dry basis, in
units
10853
of
standard cubic meters. The meter must be sufficiently accurate to measure the total
sample
10854
volume to
within 2 percent and must be calibrated at selected
flow
rates across the range of
10855
sample flow rates at
which the sorbent
trap monitoring system typically operates. The
gas flow
10856
meter must
be equipped with any necessary auxiliary measurement devices
(e.g., temperature
10857
sensors, pressure
measurement
devices)
needed to correct the sample volume to standard
10858
conditions.
10859
10860
5.1.6
Sample
Flow
Rate
Meter and Controller
10861
10862
Use a flow
rate indicator and controller for maintaining necessary sampling
flow
rates.
10863
10864
5.1.7
Temperature Sensor
10865
10866
Same as Section
6.1.1.7 of Method 5 in appendix A-3 to 40
CFR 60, incorporated by reference
in
JCAR350225-08 1 8507r01
10867
Section 225.140.
10868
10869
5.1.8
Barometer
10870
10871
Same as
Section 6.1.2 of Method 5 in appendix A-3 to 40 CFR 60, incorporated by reference in
10872
Section 225.140.
10873
10874
5.1.9 Data Logger (Optional)
10875
10876
Device for recording
associated
and necessary ancillary information (e.g., temperatures,
10877
pressures,
flow, time,
etc.).
10878
10879
5.2
Gaseous
Hg° Sorbent Trap Spiking System
10880
10881
A known
mass of gaseous Hg° must be spiked onto section 3 of each
sorbent trap prior
to
10882
sampling. Any
approach
capable
of quantitatively delivering known masses of Hg° onto sorbent
10883
traps is
acceptable. Several
technologies
or devices are available to meet this
objective. Their
10884
practicality is a function
of mercury mass spike levels. For low levels, NIST-certified or NIST
10885
traceable gas
generators or tanks may be suitable, but will likely require long preparation times.
10886
A more
practical,
alternative system,
capable of delivering almost any mass
required, makes
use
10887
of
NIST-certified or
NIST-traceable mercury
salt
solutions (e.g., Hg(N03)2). With this
system,
10888
an
aliquot of known
volume and concentration is added to a reaction vessel containing a
10889
reducing agent (e.g.,
stannous
chloride);
the mercury salt solution is reduced to Hg° and purged
10890
onto section 3 of
the sorbent trap using an impinger sparging system.
10891
10892
5.3 Sample Analysis Equipment
10893
10894
Any
analytical system capable
of quantitatively
recovering and
quantifying total gaseous
10895
mercury from
sorbent media is acceptable provided that the analysis can meet the perfonnance
10896
criteria in
Section 8 of this
procedure.
Candidate
recovery techniques include leaching,
digestion,
10897
and
thermal
desorption.
Candidate analytical techniques include ultraviolet atomic fluorescence
10898
(UV
AF);
ultraviolet atomic
absorption
(UV AA),
with and without gold trapping; and in-situ
X
10899
ray
fluorescence
(XRF) analysis.
10900
10901
6.0 Reagents and Standards
10902
10903
Only
NIST-certified
or NIST-traceable calibration gas standards and reagents must be used for
10904
the
tests
and
procedures
required
under this Exhibit.
10905
10906
7.0
Sample
Collection and Transport
10907
10908
7.1 Pre-Test Procedures
10909
JCAR350225-08
1 8507r01
10910
7.1.1 Selection of Sampling
Site
10911
10912
Sampling
site information
should
be obtained in accordance
with Method
1 in
appendix
A-i
to
10913
40 CFR 60,
incorporated
by
reference
in Section 225.140.
Identify a
monitoring
location
10914
representative
of
source mercury emissions.
Locations
shown to be free of
stratification through
10915
measurement
traverses
for
gases such as SO
and NOmay
be one such approach.
An estimation
10916
of the
expected stack
mercury concentration
is required to establish
a target
sample flow rate,
10917
total gas
sample
volume,
and the mass of Hg°
to
be spiked onto
section 3 of each
sorbent trap.
10918
10919
7.1.2
Pre-sampling
Spiking of Sorbent
Traps
10920
10921
Based
on
the estimated
mercury concentration
in the stack, the target
sample
rate
and the target
10922
sampling
duration, calculate
the
expected
mass loading for section
1 of each sorbent
trap
(for an
10923
example
calculation,
see
Section 11.1 of this
Exhibit).
The
pre-sampling spike
to be added to
10924
section 3 of
each sorbent trap
must be within
±
50 percent of
the expected
section
1 mass
10925
loading.
Spike
section
3 of each sorbent trap
at this level, as
described in Section
5.2 of this
10926
Exhibit.
For each sorbent
trap,
keep an
official record of the mass
of Hg° added to
section 3.
This
10927
record
must
include,
at
a minimum, the ID number
of the trap, the
date and time
of the spike, the
10928
name of the
analyst performing
the
procedure,
the mass of Hg°
added to section 3 of
the trap
10929
(jig), and the
supporting
calculations. This record
must
be maintained
in a
format
suitable for
10930
inspection
and
audit
and
must
be made available
to the regulatory
agencies upon request.
10931
10932
7.1.3 Pre-test Leak
Check
10933
10934
Perform
a
leak check
with the
sorbent
traps in place. Draw
a vacuum in each
sample train.
10935
Adjust the
vacuum in
the sample train to
mercury. Using the
gas
flow meter,
determine leak rate.
10936
The
leakage
rate
must
not exceed
4
percent
of the target
sampling rate. Once the
leak check
10937
passes this
criterion,
carefully
release the
vacuum
in the sample
train then
seal the sorbent trap
10938
inlet
until
the probe
is
ready for insertion into
the
stack
or
duct.
10939
10940
7.1.4
Determination
of
Flue
Gas
Characteristics
10941
10942
Determine
or
measure
the flue
gas
measurement environment
characteristics
(gas
temperature,
10943
static
pressure, gas
velocity, stack moisture,
etc.)
in order to determine
ancillary
requirements
10944
such as
probe
heating
requirements
(if
any),
initial sample
rate, proportional sampling
10945
conditions,
moisture
management,
etc.
10946
10947
7.2
Sample
Collection
10948
10949
7.2.1
10950
10951
Remove
the plug
from the end of each
sorbent trap and store
each
plug
in a clean sorbent
trap
10952
storage
container.
Remove the
stack
or
duct port
cap
and insert the
probes.
Secure the probes and
JCAR350225-081 8507r01
10953
ensure
that
no
leakage occurs between
the
duct
and environment.
10954
10955
7.2.2
10956
10957
Record initial data including the
sorbent trap
ID, start time,
starting
dry gas
meter readings,
10958
initial
temperatures,
set-points,
and any other appropriate information.
10959
10960
7.2.3
Flow Rate Control
10961
10962
Set the initial sample
flow rate at the target value from Section 7.1.1 of this Exhibit. Record the
10963
initial
gas
flow meter reading, stack
temperature
(if
needed to convert to standard conditions),
10964
meter temperatures
(if
needed),
etc. Then, for every operating hour during the sampling period,
10965
record the date and time,
the
sample
flow rate,
the gas
flow meter reading, the stack temperature
10966
(if
needed), the flow
meter temperatures
(if
needed), temperatures of heated
equipment such
as
10967
the vacuum lines and
the probes
(if heated), and the sampling system vacuum readings. Also,
10968
record the
stack gas flow rate, as measured by the certified
flow
monitor,
and the ratio of the
10969
stack gas flow rate to
the sample flow rate. Adjust the sampling flow rate to maintain
10970
proportional
sampling, i.e., keep the ratio of the stack gas flow rate to sample
flow rate
constant,
10971
to within
±
25 percent of the
reference
ratio from the
first hour of the data collection period
(see
10972
Section
11 of this
Exhibit).
The sample flow rate through a sorbent trap monitoring system
10973
during any hour
(or
portion of an
hour)
in which the unit is not operating must be
zero.
10974
10975
7.2.4
Stack Gas Moisture
Determination
10976
10977
Determine stack gas
moisture using a continuous moisture monitoring system, as described in 40
10978
CFR
75.11(b),
incorporated by reference in Section
225.140.
Alternatively, the
owner or
10979
operator may use
the appropriate fuel-specific
moisture default value provided in 40 CFR
75.11,
10980
incorporated by
reference
in Section 225.140, or a site-specific moisture default value approved
10981
by
the Agency.
10982
10983
7.2.5
Essential Operating
Data
10984
10985
Obtain and
record any
essential
operating data for the
facility during the test period, e.g., the
10986
barometric pressure
for correcting the sample volume measured by a dry gas meter to standard
10987
conditions. At
the
end of the data collection period,
record the final gas flow meter reading and
10988
the
final values of all
other essential parameters.
10989
10990
7.2.6 Post Test Leak
Check
10991
10992
When
sampling is
completed, turn off the sample pump, remove the probe/sorbent trap from the
10993
port
and carefully
re-plug the end of each sorbent trap. Perform a leak check with the sorbent
10994
traps
in place, at
the maximum vacuum reached during the sampling period.
Use the same
10995
general
approach described in
Section
7.1.3 of this
Exhibit. Record
the
leakage
rate and vacuum.
JCAR350225-08
1
8507r01
10996
The leakage rate
must
not exceed
4 percent of the average
sampling rate for the data
collection
10997
period. Following the leak check, carefully
release the vacuum in the sample train.
10998
10999
7.2.7 Sample Recovery
11000
11001
Recover each sampled sorbent trap
by
removing
it from the probe, sealing
both ends. Wipe
any
11002
deposited
material from the outside of the sorbent trap.
Place the sorbent trap into an appropriate
11003
sample storage container and
store/preserve in appropriate
manner.
11004
11005
7.2.8
Sample Preservation, Storage,
and
Transport
11006
11007
While the performance criteria of this approach provide
for verification of appropriate
sample
11008
handling, it is still important that the user consider,
determine, and plan for suitable
sample
11009
preservation,
storage, transport,
and holding times for these
measurements. Therefore,
11010
procedures in ASTM D6911-03 “Standard Guide
for
Packaging and Shipping Environmental
11011
Samples
for
Laboratory
Analysis”
(incorporated
by
reference
under
Section
225.140)
must
be
11012
followed for all samples.
11013
11014
7.2.9
Sample Custody
11015
11016
Proper
procedures
and documentation for sample chain
of custody are critical to ensuring
data
11017
integrity. The chain
of custody
procedures in ASTM D4840-99
(reapproved
2004)
“Standard
11018
Guide for
Sample Chain-of-Custody
Procedures” (incorporated
by
reference
under
Section
11019
225.140)
must be followed for all samples
(including
field samples and blanks).
11020
11021
8.0 Quality Assurance and
Quality Control
11022
11023
Table K-i summarizes the
QAIQC
performance criteria
that are used to validate the mercury
11024
emissions data
from sorb ent trap monitoring
systems, including the relative
accuracy
test audit
11025
(RATA) requirement
(see
Section
1.4(c)(7),
Section
6.5.6 of Exhibit A to this Appendix,
and
11026
Section 2.3
of Exhibit B to this Appendix).
Except as provided in Section 1.3(h)
of this
11027
Appendix and as
otherwise indicated
in Table K-i, failure
to
achieve
these performance criteria
11028
will result
in invalidation of mercury emissions
data.
11029
11030
11031
Table
K-i. Quality
Assurance/Quality
Control
Criteria for Sorbent Trap Monitoring
Systems
OAIQC
test or
Acceptance
criteria
Frequency
Consequences if
not
specification
met
Pre-test leak check
4% of target
Prior
to sampling
Sampling
must
not
sampling
rate
commence until
the
leak
check is passed.
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JCAR350225-08
1 8507r01
Analysis
of
independent
calibration standard
Within ± 10%
of true
value
Following daily
calibration,
prior to
analyzing
field
samples
Recalibrate
and repeat
independent standard
analysis
until
successful.
Spike recovery from
Section 3 of sorbent
75-125% of spike
amount
Every
sample
[FN**]
See Note,
below.
RATA
RA 20.0%orMean
difference
1.
0<<mu>>g/dscm
for low emitters
For initial certification
and annually
thereafter
Data from
the
system
are invalidated
until a
RATA is
passed.
Gas flow meter
calibration
Calibration factor
(Y)
within
± 5% of
average value from
the
most
recent
3-
point calibration
At three settings prior
to initial use and at
least quarterly
at one
setting thereafter. For
mass flow meters,
initial calibration
with
Recalibrate the meter
at three orifice
settings to determine
a
new value
of
Y.
stack gas is required
Temperature sensor
calibration
Absolute
temperature
measured
by
sensor
within± 1.5%ofa
reference sensor
Prior to initial use and
at least quarterly
thereafter
Recalibrate. Sensor
may not be used
until
specification is met.
11032
Barometer
calibration
Absolute pressure
measured by
instrument within
±
10 mm Hg of reading
with
a mercury
barometer
Prior
to initial use and
at least quarterly
thereafter
Recalibrate.
Instrument
may not
be
used until
specification
is met.
[FN**1
Note: If both traps fail to meet the acceptance criteria, the data from the pair
of traps are
invalidated.
However, if
only
one of the paired
traps
fails to meet this particular acceptance
criterion
and the other sample meets all of the applicable
QA
criteria, the results of the valid
trap
may be
used
for reporting under this part, provided that the measured
Hg
concentration
is
multiplied by a
factor
of
1.111. When
the data from both traps are invalidated and quality-
assured
data from
a certified backup monitoring
system, reference method, or approved
alternative
monitoring system are unavailable,
missing data substitution must be used. 9.0
Calibration
and Standardization.
11033
11034
11035
11036
11037
11038
11039
11040
11041
JCAR350225-081
8507r01
11042
9.1
11043
11044
Only NIST-certified
and NIST-traceable calibration
standards
(i.e.,
calibration
gases, solutions,
11045
etc.) must be used for the spiking and
analytical
procedures in this Exhibit.
11046
11047
9.2
Gas Flow Meter Calibration
11048
11049
9.2.1 Preliminaries
11050
11051
The manufacturer
or supplier of the gas flow meter should perform all necessary
set-up, testing,
11052
programming, etc., and should provide the end user with any necessary instructions, to ensure
11053
that the meter will
give an accurate readout of dry
gas
volume in standard
cubic meters for the
11054
particular field application.
11055
11056
9.2.2
Initial Calibration
11057
11058
Prior to its initial use, a
calibration
of the flow meter must be performed. The initial calibration
11059
may be done by
the manufacturer, by the equipment supplier, or
by
the end user. If
the flow
11060
meter is
volumetric in nature (e.g., a dry gas
meter),
the manufacturer, equipment supplier,
or
11061
end user may perform a
direct volumetric calibration
using any gas. For a mass flow meter, the
11062
manufacturer,
equipment supplier, or end user may calibrate the meter using
a bottled gas
11063
mixture containing
12
±
0.5%
CO
2.7
±
0.5%
02,
and
balance
,
2
N
or these same gases in
11064
proportions
more
representative of the expected stack gas composition. Mass flow meters
may
11065
also be
initially
calibrated on-site, using actual stack gas.
11066
11067
9.2.2.1
Initial Calibration Procedures
11068
11069
Determine an average
calibration factor
(Y)
for the gas flow meter, by calibrating it at three
11070
sample flow
rate settings covering the range of sample flow rates at which the sorbent trap
11071
monitoring system
typically operates.
You may either follow the procedures in Section 10.3.1
of
11072
Method 5 in
appendix A-3 to 40 CFR 60, incorporated by reference in Section 225.140, or
the
11073
procedures in Section
16 of Method 5 in appendix
A-3 to
40 CFR
60.
If a dry
gas meter is being
11074
calibrated,
use at least five
revolutions
of the meter at each flow rate.
11075
11076
9.2.2.2 Alternative Initial Calibration Procedures
11077
11078
Alternatively, you
may
perform
the initial calibration
of
the gas flow meter using a reference
gas
11079
flow
meter (RGFM). The RGFM may either be:
(1)
A wet test meter calibrated according to
11080
Section
10.3.1 of Method 5 in
appendix
A-3 to 40 CFR 60, incorporated by reference in Section
11081
225.140;
(2) a gas
flow metering device
calibrated
at multiple
flow
rates
using the procedures in
11082
Section
16 of
Method 5 in appendix A-3
to
40 CFR
60;
or (3) a NIST-traceable calibration
11083
device
capable
of measuring volumetric flow to an accuracy of 1
percent.
To calibrate
the gas
11084
flow
meter using the RGFM,
proceed
as follows: While the sorbent trap monitoring system
is
JCAR350225-08 1 8507r01
11085
sampling the actual stack gas or a
compressed
gas
mixture that
simulates
the stack gas
11086
composition
(as applicable),
connect
the RGFM to the discharge of the system.
Care
should
be
11087
taken
to
minimize
the
dead volume between the sample flow
meter being tested and the RGFM.
11088
Concurrently measure dry gas volume with the RGFM and the flow
meter being calibrated the
11089
for a minimum of 10 minutes at each of three flow rates covering the typical range
of operation
11090
of the sorbent trap
monitoring
system. For each 10-minute
(or
longer) data collection period,
11091
record the
total
sample volume, in units of dry standard cubic meters
(dscm),
measured
by the
11092
RGFM and the gas flow meter being tested.
11093
11094
9.2.2.3 Initial Calibration
Factor
11095
11096
Calculate
an individual calibration factor Yi at each tested flow
rate from Section 9.2.2.1 or
11097
9.2.2.2 of this Exhibit (as applicable), by taking the ratio of the reference
sample
volume
to the
11098
sample volume recorded by the gas flow meter. Average the three Yi values,
to determine Y,
the
11099
calibration factor for the flow
meter. Each
of the three individual values of Yi must be within ±
11100
0.02
of
Y.
Except
as otherwise provided in Sections 9.2.2.4 and 9.2.2.5
of
this
Exhibit, use the
11101
average Y value from
the
three level calibration
to
adjust
all subsequent gas volume
11102
measurements made with the gas flow meter.
11103
11104
9.2.2.4 Initial On-Site Calibration
Check
11105
11106
For a mass
flow meter that was initially calibrated using a compressed
gas mixture, an on-site
11107
calibration check must be performed before using the flow meter to provide data for
this
part.
11108
While sampling stack gas, check the calibration of the flow meter at one intermediate flow
rate
11109
typical of normal
operation of the monitoring
system. Follow the basic procedures in Section
11110
9.2.2.1 or
9.2.2.2
of this Exhibit. If the on-site calibration check shows
that the
value
of Yi, the
11111
calibration factor at the tested flow rate, differs by more than 5
percent
from the value
of Y
11112
obtained in the
initial calibration of the meter, repeat
the full 3-level calibration of the meter
11113
using
stack gas to determine a new
value
of Y, and apply the new Y value to all subsequent
gas
11114
volume
measurements made with the gas flow meter.
11115
11116
9.2.2.5 Ongoing Quality Assurance
11117
11118
Recalibrate the gas flow meter quarterly at one intermediate flow
rate setting representative
of
11119
normal
operation
of the
monitoring
system. Follow the basic procedures in Section 9.2.2.1
or
11120
9.2.2.2 of this
Exhibit. If a quarterly recalibration
shows that the value of Yi, the calibration
11121
factor at
the tested flow rate, differs from the current value of
Y by
more than
5 percent, repeat
11122
the
full 3-level
calibration
of
the meter
to determine a new value of Y, and apply the new
Y
11123
value
to all
subsequent
gas
volume measurements
made with the gas flow meter.
11124
11125
9.3 Thermocouples and Other Temperature Sensors
11126
11127
Use
the
procedures
and
criteria
in Section
10.3 of Method 2 in appendix A-i to 40 CFR
60,
JCAR350225-081 8507r01
11128
incorporated by reference
in Section 225.140,
to calibrate in-stack temperature sensors and
11129
thermocouples. Dial thermometers must be calibrated against mercury-in-glass
thermometers.
11130
Calibrations must be performed prior to initial use and at least quarterly thereafter. At each
11131
calibration
point, the
absolute temperature measured
by the temperature sensor must agree
to
11132
within
±
1.5 percent of the temperature measured with the reference sensor,
otherwise the sensor
11133
may not cOntinue to be used.
11134
11135
9.4 Barometer
11136
11137
Calibrate against a mercury barometer. Calibration must be performed prior to initial use and
at
11138
least quarterly thereafter. At each calibration point, the absolute pressure measured
by the
11139
barometer must agree to
within
±
10
mm mercury of the pressure measured by the mercury
11140
barometer, otherwise the barometer may not continue to be used.
11141
11142
9.5 Other Sensors and Gauges
11143
11144
Calibrate all other sensors and gauges according to the procedures specified
by
the instrument
11145
manufacturers.
11146
11147
9.6
Analytical System Calibration
11148
11149
See Section 10.1 of this
Exhibit.
11150
11151
10.0 Analytical Procedures
11152
11153
The analysis of the mercury
samples
may be conducted using any instrument or technology
11154
capable of
quantifying total mercury from the sorbent media and meeting
the performance
11155
criteria
in Section 8 of this Exhibit.
11156
11157
10.1 Analyzer System Calibration
11158
11159
Perform
a multipoint
calibration
of the analyzer at three or more upscale points over the desired
11160
quantitative
range
(multiple
calibration ranges must be calibrated, if necessary). The
field
11161
samples analyzed must fall
within a
calibrated,
quantitative
range and meet the necessary
11162
performance
criteria. For samples that are suitable for aliquotting, a series
of
dilutions
may be
11163
needed to
ensure that the samples fall within a calibrated range. However, for sorbent media
11164
samples that are
consumed during analysis
(e.g., thermal desorption techniques), extra care
must
11165
be
taken to
ensure that the analytical system is appropriately calibrated
prior to sample analysis.
11166
The
calibration curve ranges should be determined based on the anticipated level
of mercury
11167
mass on
the sorbent media.
Knowledge
of estimated stack mercury concentrations and total
11168
sample volume may be
required
prior
to analysis. The calibration
curve
for use with the various
11169
analytical
techniques (e.g., UV AA, TJV
AF, and
XRF)
can be
generated
by directly introducing
11170
standard
solutions into the analyzer or by spiking
the
standards onto the sorbent
media and then
JCAR350225-08 1 8507r01
11171
introducing into
the analyzer after
preparing the
sorbent/standard
according
to the
particular
11172
analytical
technique.
For each
calibration curve, the
value
of the
square
of the linear
correlation
11173
coefficient, i.e.,
,
2r
must be
0.99, and the analyzer
response
must be within
±
10
percent
of
11174
reference
value at each upscale
calibration
point.
Calibrations must
be performed
on the day
of
11175
the
analysis,
before analyzing
any
of the
samples.
Following
calibration, an independently
11176
prepared standard
(not
from same calibration
stock solution)
must be analyzed.
The
measured
11177
value
of
the independently
prepared standard
must be within
±
10 percent
of the expected value.
11178
11179
10.2
Sample Preparation
11180
11181
Carefully separate
the three sections of
each sorbent trap.
Combine for analysis
all materials
11182
associated
with each section,
i.e.,
any
supporting substrate
that the
sample
gas passes through
11183
prior to entering a
media
section (e.g.,
glass
wool,
polyurethane
foam,
etc.)
must be analyzed
11184
with that segment.
11185
11186
10.3
Spike
Recovery
Study
11187
11188
Before
analyzing any
field samples,
the laboratory must
demonstrate the ability
to recover and
11189
quantify mercury
from the sorbent media
by
performing
the following spike
recovery study
for
11190
sorbent media
traps
spiked
with elemental
mercury.
11191
11192
Using
the procedures
described in
Sections
5.2
and 11.1 of this Exhibit,
spike
the
third
section
of
11193
nine sorbent
traps with gaseous
Hg°, i.e.,
three
traps at each of three
different mass loadings,
11194
representing
the range of masses
anticipated in the
field samples.
This
will
yield
a
3 x
3 sample
11195
matrix. Prepare and
analyze
the third section
of each spiked
trap, using the techniques
that
will
11196
be used to
prepare and analyze
the field
samples. The average
recovery
for
each spike
11197
concentration must be
between 85 and 115
percent.
If multiple
types of sorbent
media
are to
be
11198
analyzed, a
separate spike
recovery
study
is required for each
sorbent material.
If
multiple
ranges
11199
are
calibrated, a separate
spike recovery study
is
required
for each range.
11200
11201
10.4 Field
Sample
Analysis
11202
11203
Analyze
the sorbent trap
samples following
the
same procedures
that were used
for conducting
11204
the spike
recovery study. The
three sections
of each sorbent trap
must
be analyzed
separately
11205
(i.e.,
section 1, then section
2, then section
3).
Quantify
the
total mass of mercury
for
each
11206
section based
on analytical
system
response
and the calibration
curve from
Section 10.1 of
this
11207
Exhibit.
Determine
the
spike recovery
from sorbent trap
section 3. The
spike
recovery
must
be
11208
no less
than 75 percent
and no greater than
125
percent.
To report the final
mercury mass
for
11209
each trap, add
together
the mercury
masses collected in
trap sections 1
and 2.
11210
11211
11.0
Calculations
and Data Analysis
11212
11213
11.1
Calculation of
Pre-Samnling
Snikina
Level
JCAR350225-081
8507r01
11214
11215
11216
11217
11218
11219
11220
11221
11222
11223
11224
11225
11226
11227
11228
11229
11230
11231
11232
11233
11234
11235
11236
11237
11238
11239
11240
11241
Determine
sorbent
trap
section
3
spiking
level
using
estimates
of the stack
mercury
concentration,
the
target
sample flow
rate, and
the expected
sample
duration.
First, calculate
the
expected
mercury
mass that
will be collected
in section
1 of
the trap. The
pre-sampling
spike
must
be
within
±
50
percent
of
this mass.
Example
calculation:
For an estimated
stack
mercury
concentration
of 5
ig/m
3
,
a target
sample
rate
of 0.30
L/min,
and
a sample
duration of
5 days:
(0.30
L/min)
(1440
minlday)
(5
days)
(10
m
3
/liter) (5tg/m
3
)
10.8
ig
A
pre-sampling
spike
of 10.8
.ig
±
50 percent
is, therefore,
appropriate.
11.2
Calculations
for
Flow-Proportional
Sampling
For the
first hour
of
the
data collection
period,
detennine
the reference
ratio
of the stack
as
volumetric
flow
rate to
the
sample
flow rate,
as
follows:
KQ
Rref
=
ref
(Equation
K-i)
Frei
Where:
Reference
ratio
of hourly
stack
gas
flow
rate
to
hourly
sample
flow
rate
Average stack
gas
volumetric
flow
rate
for
first
hour of
collection
period
=
Average
sample
flow rate
for first hour
of the
collection
period, in appropriate
units
(e.g.,
liters/mm,
cc/mm, dscm/min)
K
= Power
often
multiplier,
to
keep
the
value
of
between
1 and 100.
The
appropriate
K value
will
depend
on the selected
units of
measure
for the
sample
flow
rate.
Then,
for each
subsequent
hour
of
the data collection
period,
calculate
ratio of
the stack
gas
flow rate
to the
sample
flow rate
using
the
equation K-2:
R,
1 =
(Equation
K-2)
Where:
=
Ratio of hourly
stack
gas flow rate
to
hourly
sample flow
rate
Qh
= Average
stack
gas
volumetric
flow
rate
for the hour
JCAR350225-081 8507r01
Fh
= Average sample
flow rate for the hour, in appropriate
units
(e.g.,
liters/mm,
cc/mm, dscm/min)
K
Power often multiplier, to keep the value
of
Rh
between
1 and 100. The
appropriate
K
value
will
depend on the selected units
of measure for the
sample flow rate
and the range of expected stack gas flow rates.
11242
11243
11244
Maintain the value of
Rh
within
+ 25
percent of Rthroughout the data collection
period.
11245
11246
11.3 Calculation of
Spike
Recovery
11247
11248
Calculate the
percent recovery
of each section 3 spike, as follows:
11249
11250
%R=ix100
(EguationK-3)
11251
11252
Where:
11253
Percentage recovery of the pre-sampling
spike
M3
Mass of mercury recovered
from section 3 of the sorbent trap, fig)
%R
Percentage recovery
of the pre-sampling spike
11254
11255
11.4 Calculation of Breakthrough
11256
11257
Calculate
the percent breakthrough to the second
section
of the sorbent trap, as follows:
11258
11259
Where:
11260
11261
%B=--x100
(EguationK-4)
11262
11263
Where:
11264
%B
= Percent breakthrough
Mass
of mercury
recovered from section 2 of the
sorbent trap, (jig)
M
1 = Mass of mercury recovered from section
1 of the sorbent trap,
fig)
11265
11266
11.5 Calculation
of Mercury Concentration
11267
11268
Calculate
the mercury concentration for each sorbent trap,
using the following
equation:
11269
JCAR350225-08
1 8507r01
M*
11270
C
=—
(EguationK-5)
11271
11272
Where:
11273
C
Concentration of mercury for the collection period, igm1dscm)
M*
= Total mass of mercury recovered from sections 1 and
2
of the sorbent trap,
= Total volume of dry gas metered during the collection period,
(dscm).
For
the
purposes of this Exhibit, standard temperature and pressure are defined
as 20
°C
and 760 mm mercury, respectively.
11274
11275
11.6 Calculation of Paired Trap Agreement
11276
11277
Calculate the relative deviation
(RD)
between the mercury concentrations
measured
with the
11278
paired sorbent
traps:
11279
jC -C
11280
RD=
a
b
xlOO
fEguationK-6)
Ca +Cb
11281
11282
Where:
11283
RD = Relative
deviation
between the mercury concentrations from traps
??atl
and
btt
(percent)
Ca
= Concentration of mercury for the collection period, for sorbent trap
tat
(jigm/dscm)
Concentration of
mercury
for the
collection
period,
for sorbent trap
b”
TT
fligmldscm)
11284
11285
11.7 Calculation of Mercury
Mass
Emissions
11286
11287
To
calculate
mercury mass emissions, follow the procedures in Section 4.1.2 of Exhibit
C
to
11288
this
Appendix. Use the average of the two mercury concentrations from the paired traps
in
11289
the
calculations, except as
provided
in Section 2.2.3(h) of Exhibit B to this Appendix or in
11290
Table
K-i.
11291
11292
12.0 Method Performance
11293
11294
These
monitoring
criteria and procedures
have been applied to coal-fired utility
boilers
11295
(including units with
post-combustion emission controls), having vapor-phase mercury
11296
concentrations
ranging from 0.03 ig/dscm to 100 ig/dscm.
JCAR350225-08 1 8507r01
11297
11298
(Source:
Added at 33 Iii. Reg.
effective