SUBTITLE B: AIR POLLUTION
CHAPTER I: POLLUTION CONTROL BOARD
SUBCHAPTER c: EMISSIONS STANDARDS AND LIMITATIONS FOR STATIONARY SOURCES
PART 218 ORGANIC MATERIAL EMISSION STANDARDS AND LIMITATIONS FOR THE CHICAGO AREA
SECTION 218.APPENDIX D COEFFICIENTS FOR THE TOTAL RESOURCE EFFECTIVENESS INDEX (TRE) EQUATION
Section 218.APPENDIX D Coefficients for the Total Resource Effectiveness Index (TRE) Equation
This Appendix contains values for the total resource effectiveness index (TRE) equation in Subpart V.
If a flow rate falls exactly on the boundary between the indicated ranges, the operator shall use the row in which the flow rate is maximum.
COEFFICIENTS FOR TRE EQUATION
FOR CHLORINATED PROCESS VENT STREAMS WITH
NET HEATING VALUE LESS THAN
OR EQUAL TO 3.5 MJ/scm
|
FLOW RATE (scm/min) |
|
|
|
|
|
|
|
|
Min. |
Max. |
a |
b |
c |
d |
e |
f |
|
|
|
|
|
|
|
|
|
|
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 |
FOR TRE EQUATION
FOR NON-CHLORINATED 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
1.98 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 |
0.033 |
0. |
0. |
0.0424 |
FOR TRE EQUATION
FOR NONCHLORINATED PROCESS VENT STREAMS WITH
NET HEATING VALUE GREATER THAN 3.6 MJ/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 |