TITLE 35: ENVIRONMENTAL PROTECTION
SUBTITLE B: AIR POLLUTION
CHAPTER I: POLLUTION CONTROL BOARD
SUBCHAPTER c: EMISSION STANDARDS AND LIMITATIONS FOR STATIONARY SOURCES
PART 214
SULFUR LIMITATIONS
SUBPART A: GENERAL PROVISIONS
Section
214.100
| Scope and Organization |
214.101
| Measurement Methods |
214.102
| Abbreviations and Units |
214.103
| Definitions |
214.104
| Incorporations by Reference |
| |
SUBPART B: NEW FUEL COMBUSTION EMISSION SOURCES
Section
214.121
| Large Sources | |
214.122
| Small Sources | |
| | |
SUBPART C: EXISTING SOLID FUEL COMBUSTION EMISSION SOURCES
Section
214.140 Scope
214.141
| Sources Located in Metropolitan Areas |
214.142
| Small Sources Located Outside Metropolitan Areas |
214.143
| Large Sources Located Outside Metropolitan Areas |
| |
SUBPART D: EXISTING LIQUID OR MIXED FUEL COMBUSTION EMISSION SOURCES
Section
214.161
| Liquid Fuel Burned Exclusively |
214.162
| Combination of Fuels |
| |
SUBPART E: AGGREGATION OF SOURCES OUTSIDE METROPOLITAN AREAS
Section
214.181
| Dispersion Enhancement Techniques |
214.182
| Prohibition |
214.183
| General Formula |
214.184
| Special Formula |
214.185
| Alternative Emission Rate |
214.186
| New Operating Permits |
| |
SUBPART F: ALTERNATIVE STANDARDS FOR SOURCES INSIDE METROPOLITAN AREAS
Section
214.201
| Alternative Standards for Sources in Metropolitan Areas |
214.202
| Dispersion Enhancement Techniques |
| |
SUBPART K: PROCESS EMISSION SOURCES
Section
214.300
| Scope |
214.301
| General Limitation |
214.302
| Exception for Air Pollution Control Equipment |
214.303
| Use of Sulfuric Acid |
214.304
| Fuel Burning Process Emission Source |
| |
SUBPART O: PETROLEUM REFINING, PETROCHEMICAL AND CHEMICAL MANUFACTURING
Section
214.380
| Scope |
214.381
| Sulfuric Acid Manufacturing |
214.382
| Petroleum and Petrochemical Processes |
214.383
| Chemical Manufacturing |
214.384
| Sulfate and Sulfite Manufacturing |
| |
SUBPART P: STONE, CLAY, GLASS AND CONCRETE PRODUCTS
Section
214.400
| Scope |
214.401
| Glass Melting and Heat Treating |
214.402
| Lime Kilns |
| |
SUBPART Q: PRIMARY AND SECONDARY METAL MANUFACTURING
Section
214.420
| Scope |
214.421
| Combination of Fuels at Steel Mills in Metropolitan Areas |
214.422
| Secondary Lead Smelting in Metropolitan Areas |
214.423
| Slab Reheat Furnaces in St. Louis Area |
| |
SUBPART V: ELECTRIC POWER PLANTS
Section
214.521
| Winnetka Power Plant |
| |
SUBPART X: UTILITIES
Section
214.560
| Scope |
214.561
| E. D. Edwards Electric Generating Station |
214.562
| Coffeen Generating Station |
| |
Appendix A
| Rule into Section Table |
Appendix B
|
Section into Rule Table |
Appendix C
|
Method used to Determine Average Actual Stack Height and Effective Height of Effluent Release |
Appendix D
|
Past Compliance Dates |
| |
AUTHORITY: Implementing Section 10 and authorized by Section 27 of the Environmental Protection Act [415 ILCS 5/10 and 27].
SOURCE: Adopted as Chapter 2: Air Pollution, Rule 204: Sulfur Emission Standards and Limitations, R71-23, 4 PCB 191, filed and effective April 14, 1972; amended in R74-2 and R75-5, 32 PCB 295, at 3 Ill. Reg. 5, p. 777, effective February 3, 1979; amended in R74-2, R75-5, 38 PCB 129, at 4 Ill. Reg. 28, p. 417, effective June 26, 1980; amended in R78-17, 40 PCB 291, at 5 Ill. Reg. 1892, effective February 17, 1981; amended in R77-15, 44 PCB 267, at 6 Ill. Reg. 2146, effective January 28, 1982; amended and renumbered in R80-22(A), at 7 Ill. Reg. 42204219, effective March 28, 1983; codified 7 Ill. Reg. 1357913597; amended in R80-22(B), at 8 Ill. Reg. 6172, effective April 24, 1984; amended in R84-28, at 10 Ill. Reg. 9806, effective May 20, 1986; amended in R86-31, at 12 Ill. Reg. 17387, effective October 14, 1988; amended in R86-30, at 12 Ill. Reg. 20778, effective December 5, 1988; amended in R87-31 at 15 Ill. Reg. 1017, effective January 15, 1991; amended in R02-21 at 27 Ill. Reg. 12101, effective July 11, 2003; amended in R04-12 at _ Ill. Reg. _, effective _.
SUBPART D: EXISTING LIQUID OR MIXED FUEL COMBUSTION EMISSION SOURCES
Section 214.162
| Combination of Fuels |
| |
a)
| No person shall cause or allow the emission of sulfur dioxide into the atmosphere in any one hour period from any fuel combustion emission source burning simultaneously any combination of solid, liquid and gaseous fuels to exceed the allowable emission rate determined by the following equation: |
| |
E = AX + BY + CZ
b)
| Symbols in the equation mean the following: |
| |
E = allowable sulfur dioxide emission rate;
ASS =
| solid fuel sulfur dioxide emission standard which is applicable; |
| |
BSd =
| distillate oil sulfur dioxide emission standard determined from the table in subsection (d); |
| |
CSR =
| residual fuel oil sulfur dioxide emission standard which is applicable; |
| |
XHS = actual heat input from solid fuel;
YHd = actual heat input from distillate fuel oil;
ZHR = actual heat input from residual fuel oil;
c)
| That portion of the actual heat input that is derived: |
| |
1)
| From the burning of gaseous fuels produced by the gasification of solid fuels shall be included in XHS; |
| |
2)
| From the burning of gaseous fuels produced by the gasification of distillate fuel oil shall be included in YHd; |
| |
3)
| From the burning of gaseous fuels produced by the gasification of residual fuel oil shall be included in ZHR; |
| |
4)
| From the burning of gaseous fuels produced by the gasification of any other liquid fuel shall be included in ZHR; and, |
| |
5)
| From the burning of by-product gases such as those produced from a blast furnace or a catalyst regeneration unit in a petroleum refinery shall be included in ZHR. |
| |
d)
| Metric or English units may be used in the equation of subsection (a) as follows: |
| |
Parameter
|
Metric
|
English
|
|
|
|
E
|
kg/hr
|
lbs/hr
|
ASS, CSR
|
kg/MW-hr
|
lbs/mmbtulbs/Mbtu
|
BSd
|
0.46 kg/MW-hr
|
0.3 lbs/mmbtulbs/Mbtu
|
XHS, YHd, ZHR
|
MW
|
mmbtu/hrMbtu/hr
|
(Source: Amended at _ Ill. Reg. _, effective _)
SUBPART E: AGGREGATION OF SOURCES OUTSIDE METROPOLITAN AREAS
Section 214.183
| General Formula |
| |
a)
| The general formula is: |
| |
E = A XB YC
(in English units)
(in Metric units)
b)
| Symbols used in the general formula mean the following: |
| |
E =
| Total allowable emission of sulfur dioxide (in lbs/hr or kg/hr) into the atmosphere in any one-hour period from all fuel combustion emission sources owned or operated by such person and located within a 1.6 km (1 mile) radius from the center point of any such emission source. |
| |
XHA =
| Average actual stack height as determined by method outlined in Appendix C. |
| |
YHE =
| Effective height of effluent release as determined by method outlined in Appendix C. |
| |
c)
| The general formula may be used with either metric or English units as follows: |
| |
Parameter
|
Metric
|
English
|
|
|
|
E
|
kg/hr
|
lbs/hr
|
X, Y
|
m
|
ft
|
A
|
0.04347 kg/hr
|
0.007813 lbs/hr
|
B
|
0.11
|
0.11
|
C
|
2
|
2
|
(Source: Amended at _ Ill. Reg. _, effective _)
Section 214.184
| Special Formula |
| |
a)
| If the maximum total emissions of sulfur dioxide into the atmosphere in any one hour period from all fuel combustion emission sources owned or operated by any person and located within a 1 mile (1.6 km) radius from the center point of any such fuel combustion emission sources exceed, during normal cyclical variations in firing rate and fuel, the emissions allowed under Section 214.183 but, as of April 1, 1978, were in compliance with either the formula detailed below or a Pollution Control Board (Board) order, then the owner or operator of the emission sources shall not cause or allow such emissions to exceed the emissions allowed under Section 214.183 or the formula detailed below, whichever the owner or operator of the emission sources determines shall apply. |
| |
b)
| |
| |
E = 0.22222
(in English units)
(in Metric units)
H = P1 H1 + P2 H2 + ... Pn Hn
(Note: P1 + P2 ... Pn = 1)
c)
| As used in these equations, symbols mean the following: |
| |
E =
| total emission of sulfur dioxide, (in pounds per hour,lbs/hr or kg/hr) into the atmosphere in any one hour period from all fuel combustion emission sources owned or operated by such person and located within a 1 mile (1.6 km) radius from the center point of any such emission source; |
| |
Pi, i = 1, 2,...,
|
n =
|
percentage of total emissions E emitted from source I divided by 100, and
|
Hi, i = 1, 2,...,
|
n =
|
physical height in feet above grade of stack i.
|
Pi=
| (for i=1, 2, . . ., n) percentage or total emissions E emitted from source i expressed as decimal equivalents (e.g., 21% = 0.21), and |
| |
Hi=
| (for i=1, 2, . . ., n) physical height (in feet or meters) above grade of stack i. |
| |
(Source: Amended at _ Ill. Reg. _, effective _)
SUBPART Q: PRIMARY AND SECONDARY METAL MANUFACTURING
Section 214.421
| Combination of Fuels at Steel Mills in Metropolitan Areas |
| |
a)
| Section 214.162 notwithstanding, no person shall cause or allow the emission of sulfur dioxide into the atmosphere in any one hour period from any existing fuel combustion emission source at a steel mill located in the Chicago or St. Louis (Illinois) major metropolitan area burning any solid, liquid or gaseous fuel, or any combination thereof, to exceed the allowable emission rate determined by the following equation: |
| |
E = AW + BX + CY + DZ
E = SSHS + SdHd + SRHR + SGHG
b)
| Symbols in the equation mean the following: |
| |
E = allowable sulfur dioxide emission rate;
ASS =
| solid fuel sulfur dioxide emission standard which is applicable; |
BSd =
| distillate oil sulfur dioxide emission standard determined from the table in subsection (d); |
CSR =
| residual oil sulfur dioxide emission standard which is applicable; |
DSG =
| maximum by-product gas sulfur dioxide emissions which would result if the applicable by-product gas which was burned had been burned alone at any time during the 12 months preceding the latest operation, on or before March 28, 1983, of an emission source using any by-product gas. |
WHS = actual heat input from solid fuel;
XHd = actual heat input from distillate fuel oil;
YHR = actual heat input from residual fuel oil;
ZHG =
| actual heat input from by-product gases, such as those produced from a blast furnace. |
| |
c)
| That portion of the actual heat input that is derived: |
| |
1)
| From the burning of gaseous fuels produced by the gasification of solid fuels shall be included in WHS; |
| |
2)
| From the burning of gaseous fuels produced by the gasification of distillate fuel oil shall be included in XHd; |
| |
3)
| From the burning of gaseous fuels produced by the gasification of residual fuel oil shall be included in YHR; and |
| |
4)
| From the burning of gaseous fuels produced by the gasification of any other liquid fuel shall be included in ZHG. |
| |
d)
| Metric or English units may be used in the equation of subsection (a) as follows: |
| |
Parameter
|
Metric
|
English
|
|
|
|
E
|
kg/hr
|
lbs/hr
|
ASS, CSR, DSG
|
kg/MW-hr
|
lbs/mmbtulbs/Mbtu
|
BSd
|
0.46 kg/MW-hr
|
0.3 lbs/mmbtulbs/Mbtu
|
WHS, XHd, YHR, ZHG
|
MW
|
mmbtu/hrMbtu/hr
|
(Source: Amended at _ Ill. Reg. _, effective _)
APPENDIX C
Method used to Determine Average Actual Stack Height and Effective Height of Effluent Release
Q (Btu/sec) = Heat emission rate (in btu/sec or Kcal/sec) as determined by method outlined below.
∆H (feet) =
| Plume rise (in feet or meters). |
| |
H =
| Physical height (in feet or meters), above grade of each stack, except that for purposes of this calculation the value used for such stack height shall not exceed good engineering practice as defined by Section 123 of the Clean Air Act and Regulations promulgated thereunder, unless the owner or operator of the source demonstrates to the Agency that a greater height is necessary to prevent downwash or fumigation conditions. |
| |
T (Degrees Rankine) =
| Exit temperature of stack gases (in degrees Rankine or degrees Kelvin) from each source during operating conditions which would cause maximum emissions. |
| |
V (feet/sec) =
| Exit velocity of stack gases (in feet/sec or meters/sec) from each source under operating conditions which would cause maximum emissions. |
| |
D (feet) = Diameter of stack (in feet or meters).
P =
| Percentage of total emissions expressed as decimal equivalents emitted from each source. Example: 21% = 0.21. NOTE: The sum of P1 + P2 ... + Pn = 1. The emission values to be used are those which occur during operating conditions which would cause maximum emissions. |
| |
X HA =
| Average actual stack height (in feet or meters). |
| |
YHE =
| Effective height of effluent release (in feet or meters). |
| |
STEP 1: Determine weighted average stack parameters utilizing the following formulae:
D = P1 D1 + P2 D2 + ... + Pn Dn
V = P1 V1 + P2 V2 + ... + Pn Vn
T = P1 T1 + P2 T2 + ... + Pn Tn
HAX = P1 H1 + P2 H2 + ... + Pn Hn
NOTE: P1, D1, V1, T1, P1, D1, V1, T1, and H1 H1 are the percentage of total emissions, stack diameter, exit velocity of gases, exit temperature of stack gases, and physical stack height, respectively, for the first source; P2, D2, V2, T2, P2, D2, V2, T2, and H2 H2 are the respective values for the second source; similarly, Pn, Dn, Vn, Tn, Pn, Dn, Vn, Tn, and Hn Hn are the respective values for the nth source, where n is the number of the last source.
STEP 2:
| Calculate heat emission rate utilizing the following formula and the weighted average stack parameters obtained in Step 1: |
| |
Q + 7.54D2V (T - 515)
T
![](html/index47804.jpg)
(in English units)
| |
| |
![](html/index47805.jpg)
(in Metric units)
| |
| |
STEP 3:
| Calculate plume rise utilizing the appropriate formula given below and the total heat emission rate obtained in Step 2: |
| |
H = 2.58 (Q)0.6 for Q 6000 btu/sec.
(X)0.11
(in English Units for QH≥ 6000 btu/sec)
(in Metric Units for QH≥ 1500 kcal/sec)
H = 0.718 (Q)0.75 for Q 6000 btu/sec.
(X)0.11
(in English Units for QH< 6000 btu/sec)
(in Metric Units for QH< 1500 kcal/sec)
STEP 4:
| Calculate the weighted average facility effective height of effluent release utilizing the plume rise obtained in Step 3, the average stack height obtained in Step 1 and the formula given below: |
| |
Y = X + H
STEP 5:
| Calculate the total facility hourly emission limitation utilizing the weighted actual stack height obtained in Step 1, the effective stack height given in Step 4, and the following formula: |
| |
E = (X)0.11 (Y)2
128
(in English units)
(in Metric units)
(Source: Amended at _ Ill. Reg. _, effective _)
IT IS SO ORDERED.
I, Dorothy M. Gunn, Clerk of the Illinois Pollution Control Board, certify that the Board adopted the above order on January 22, 2004, by a vote of 5-0.
Dorothy M. Gunn, Clerk
Illinois Pollution Control Board
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