Where:
Eh | = | The total organic mass flow rate, kg/h |
Q2sd | = | The volumetric flow rate of gases entering or exiting control device, dscm/h, as determined by Reference Method 2 |
n | = | The number of organic compounds in the vent gas |
Ci | = | The organic concentration in ppm, dry basis, of compound i in the vent gas, as determined by Reference Method 18 |
MWi | = | The molecular weight of organic compound i in the vent gas, kg/kg-mol |
0.0416 | = | The conversion factor for molar volume, kg-mol/m3, at 293 K and 760 mm Hg |
10-6 | = | The conversion factor from ppm |
Where:
Eh | = | The total organic mass flow rate, kg/h |
Q | = | The volumetric flow rate of gases entering or exiting control device, dscm/h, as determined by Reference Method 2 |
C | = | The organic concentration in ppm, dry basis, of compound i in the vent gas, as determined by Reference Method 25A |
MW | = | The molecular weight of propane, 44 kg/kg-mol |
0.0416 | = | The conversion factor for molar volume, kg-mol/m3, at 293 K and 760 mm Hg |
10-6 | = | The conversion factor from ppm |
A = F x H
Where:
A | = | total organic emission rate, kg/y |
F | = | the total organic mass flow rate, kg/h, as calculated in subsection (c)(1)(D) |
H | = | the total annual hours of operation for the affected unit, h/y |
Ill. Admin. Code tit. 35, § 725.934
Amended at 22 Ill. Reg. 17620, effective September 28, 1998