SUBTITLE B: AIR POLLUTION
CHAPTER I: POLLUTION CONTROL BOARD
SUBCHAPTER c: EMISSIONS STANDARDS AND LIMITATIONS FOR STATIONARY SOURCES
PART 219 ORGANIC MATERIAL EMISSION STANDARDS AND LIMITATIONS FOR THE METRO EAST AREA
SECTION 219.APPENDIX D COEFFICIENTS FOR THE TOTAL RESOURCE EFFECTIVENESS INDEX (TRE) EQUATION
Section 219.APPENDIX D Coefficients for the Total Resource Effectiveness Index (TRE) Equation
The Appendix contains values for the total resource effectiveness index (TRE) equation in Subpart V.
If a flow rate falls exactly on the boundary between the indicated ranges, the operator shall use the row in which the flow rate is maximum.
COEFFICIENTS FOR TRE EQUATION
FOR CHLORINATED PROCESS VENT STREAMS WITH
NET HEATING VALUE LESS THAN
OR EQUAL TO 3.5 MJ/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
0.0 |
13.5 |
48.73 |
0. |
0.404 |
-0.1632 |
0. |
0. |
|
13.5 |
700. |
42.35 |
0.624 |
0.404 |
-0.1632 |
0. |
0.0245 |
|
700. |
1400. |
84.38 |
0.678 |
0.404 |
-0.1632 |
0. |
0.0346 |
|
1400. |
2100. |
126.41 |
0.712 |
0.404 |
-0.1632 |
0. |
0.0424 |
|
2100. |
2800. |
168.44 |
0.747 |
0.404 |
-0.1632 |
0. |
0.0490 |
|
2800. |
3500. |
210.47 |
0.758 |
0.404 |
-0.1632 |
0. |
0.0548 |
COEFFICIENTS FOR TRE EQUATION
FOR CHLORINATED PROCESS VENT STREAMS WITH
NET HEATING VALUE GREATER THAN
3.5 MJ/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
0. |
13.5 |
47.76 |
0. |
-0.292 |
0. |
0. |
0. |
|
13.5 |
700. |
41.58 |
0.605 |
-0.292 |
0. |
0. |
0.0245 |
|
700. |
1400. |
82.84 |
0.658 |
-0.292 |
0. |
0. |
0.0346 |
|
1400. |
2100. |
123.10 |
0.691 |
-0.292 |
0. |
0. |
0.0424 |
|
2100. |
2800. |
165.36 |
0.715 |
-0.292 |
0. |
0. |
0.0490 |
|
2800. |
3500. |
206.62 |
0.734 |
-0.292 |
0. |
0. |
0.0548 |
COEFFICIENTS FOR TRE EQUATION
FOR NONCHLORINATED PROCESS VENT STREAMS WiTH
NET HEATING VALUE LESS THAN
OR EQUAL TO 0.48 MJ/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
0. |
13.5 |
19.05 |
0. |
0.113 |
-0.214 |
0. |
0. |
|
13.5 |
1350. |
16.61 |
0.239 |
0.113 |
-0.214 |
0. |
0.0245 |
|
1350. |
2700. |
32.91 |
0.260 |
0.113 |
-0.214 |
0. |
0.0346 |
|
2700. |
4050. |
49.21 |
0.273 |
0.113 |
-0.214 |
0. |
0.0424 |
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED
PROCESS VENT STREAMS WITH NET HEATING VALUE
GREATER THAN 0.48 AND LESS THAN OR
EQUAL TO 1.9 MJ/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
0. |
13.5 |
19.74 |
0. |
0.400 |
-0.202 |
0. |
0. |
|
13.5 |
1350. |
18.30 |
0.138 |
0.400 |
-0.202 |
0. |
0.0245 |
|
1350. |
2700. |
36.28 |
0.150 |
0.400 |
-0.202 |
0. |
0.0346 |
|
2700. |
4050. |
54.26 |
0.158 |
0.400 |
-0.202 |
0. |
0.0424 |
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED
PROCESS VENT STREAMS WITH NET HEATING VALUE
GREATER THAN 1.9 AND LESS THAN OR
EQUAL TO 3.6 MJ/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
.0 |
13.5 |
15.24 |
0. |
0.033 |
0. |
0. |
0. |
|
13.5 |
1190. |
13.63 |
0.157 |
0.033 |
0. |
0. |
0.0245 |
|
1190. |
2380. |
26.95 |
0.171 |
0.033 |
0. |
0. |
0.0346 |
|
2380. |
3570. |
40.27 |
0.179 |
0.003 |
0. |
0. |
0.0424 |
COEFFICIENTS FOR THE EQUATION
FOR NONCHLORINATED PROCESS VENT STREAMS WITH
NET HEATING VALUE GREATER THAN 3.6 MG/scm
|
FLOW RATE |
|
|
|
|
|
|
|
|
(scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
0. |
13.5 |
15.24 |
0. |
0. |
0.0090 |
0. |
0. |
|
13.5 |
1190. |
13.63 |
0. |
0. |
0.0090 |
0.0503 |
0.0245 |
|
1190. |
2380. |
26.95 |
0. |
0. |
0.0090 |
0.0546 |
0.0346 |
|
2380. |
3570. |
40.27 |
0. |
0. |
0.0090 |
0.0573 |
0.0424 |
(Source: Amended at 17 Ill. Reg. 16918, effective September 27, 1993)