SUBTITLE B: AIR POLLUTION
CHAPTER I: POLLUTION CONTROL BOARD
SUBCHAPTER c: EMISSIONS STANDARDS AND LIMITATIONS FOR STATIONARY SOURCES
PART 215 ORGANIC MATERIAL EMISSION STANDARDS AND LIMITATIONS
SECTION 215.APPENDIX F COEFFICIENTS FOR THE TOTAL RESOURCE EFFECTIVENESS INDEX (TRE) EQUATION
Section 215.APPENDIX F 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 |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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 LESS THAN 3.5 MJ/scm |
|||||||
|
FLOW RATE |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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 |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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 THE 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 |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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 |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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 |
|
COEFFICIENTS FOR TRE EQUATION FOR NONCHLORINATED PROCESS VENT STREAMS WITH NET HEATING VALUE GREATER THAN 3.6 MJ/scm |
|||||||
|
FLOW RATE |
a |
b |
c |
d |
e |
f |
|
|
(scm/min) |
|||||||
|
Min. |
Max. |
||||||
|
|
|
|
|
|
|
|
|
|
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: Added at 11 Ill. Reg. 20829, effective December 14, 1987)