Document QXqgN4rwa7mg3EqBZox519k3o

1 K = Constant..i.740 x 10~7 (l/ppm) (mole/scm) (Hj/kcal) where standard temperature for mole/scm Is 20*C. Cl = Concentration of sample component-1. reported on a net basis. In ppm. as measured by Reference netbod 18 or ASTH 01946-07 (reapproved 1977). Incorporated by reference In Section 215.10S. Ml = Met. heat of combustion of sample component V. kcal/nole based on combustion at 2S C and 760 na Hg. If. published values are. not available or caiihot. be calculated, the beats of combustion of vent stream components ' are required to. be determined using ASTH 02382-76. Incorporated by reference lit Section 21S.10S. e) The emission rate of total.organic compounds In the process vent stream shall be calculated using the following equation: n E IC'F C1M1 , i 1=1 Where: E = . Emission rate.of total organic compounds (minus, methane and ethane) In the sample In kg/hr. i' s 'Constant 2.494 x ;I0~* (1/ppm) . .(mole/scm) (kg/g) (mln/hr). where standard temperature for (mole/scm) Is 20C. Hi s Molecular weight of sample component 1 (g/mole). ' F = Vent stream flowrate (scm/mln), at a standard temperature of 20*C. f) The total .vent stream concentration (by volume) of compounds containing halogens (ppmv; by compound) sha11.be sunned from the Individual concentrations of compounds containing halogens which were measured by Reference Method 18. (Source: Added at 11 111. Reg. 20829. effective Oecember 14. 1987) ' 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 CHtORINATEO PROCESS VENT STREAMS WITH NET HEATING VALUE LESS THAN OR EQUAL TO 3VS MJ/scm FLOW RATE (soa/mln) - : Min. Max. a- b - e ' d e f 0.0 13. s. 48.73 0. 0.404 -0.1632 0. 0. ' 13.5 700; 42.3S 0.624 0.404 -0.1632 0. 0.024 i 700. 1400. 84.38 0.678 0;404 -0.1632 0. 0.034- 1400. 2100. 126.41 0.712 0.404 -8.1632 0. 0.042 2100. 2800. 168.44 0.747 0.404 -0.1632 0. 0.049 2800. 3S00. 210.47 0.7S8 0.404 -0.1632 0. 0.QS4 COEFFICIENTS FOR TRE EQUATION FOR CHtORINATEO PROCESS VENT STREAMS WITH NET HEAUNG VALUE GRCATIR THAM J.S- MJ/scm FLOW RATE. (scmAaln) Min. Max. J .a. b C . d e . r.. 0; TJ.S 47:76 , 11.5 700. 41.S8 700. 1400. 82.84 1400. 1108, . 121,16 2100. 2800. 165.36 2800. 1500. 206.62 0... 0.60S 0.658 8.691 0.71S 0.734 -<r:29r o. 0. -0.292 0. 0. -0.292 . 0. 0. -8.292,8, 8, -0.292 0. 0. -0.292 0. 0. 0. 0.0245 0.0346 0,0424 0.0490 0.0548 COEFFICIENTS FOR TRE EQUATION FOR RQNCMLORIMATEO PROCESS..VENX. STREAMS WITH NET KEATING VALUE'LESS THAN OR EQUAL TO 0.48 MJ/scm FLOWRATE (scm/mln) Kin. Hax. a b c de f 0. W.S 13S0. 2700. 13.5 1350. 2700. 4050. 19.05 0. 0.113 -0.214 0. 0. 16.61 0.239 0ill3 >0.214 0. 0.0245 3*9V 0,260- 0^10- -0>M4.- 0-- 0,0346 49.21 0.273 0.113 -0.214 0. 0.0424 COEFFICIENTS FOR TRE EQUATION FOR NONCHlORnWTED" .* PROCESS VENT STREAMS WITH NET HEATING VALUE GREATER THAN 0.48 AMO LESS THAN OR EQUAL TO 1.9 HJ/SCm FLOW RATE. (scm/mln) Min. Max. . a b c de f 8. 13.S 1350. 2700. 13.5 13S0. 2700. 40S0. 19.-74- Or 18.30 0.138 36.28 0.150 54.26 0.158 0v400 -r282- 80.400 -0.202 0. 0.400 -0.202 0. 0.400 -0.202 0. 0. ~ 0.024S 0.0346 0.0424 - 142 -