Eh = total organic mass flow rate, kg/h
Q2sd = volumetric flow rate of gases entering or exiting control device, as determined by Method 2, dscm/h
n = number of organic compounds in the vent gas
Ci = organic concentration in ppm, dry basis, of compound i in the vent gas, as determined by Method 18
MWi = molecular weight of organic compound i in the vent gas, kg/kg-mol
0.0416 = conversion factor for molar volume, kg-mol/m3 (@ 293 K and 760 mm Hg)
10-6 = conversion from ppm
Eh = (Q)(C)(MW)(0.0416)(10-6)
where:
Eh = total organic mass flow rate, kg/h
Q = volumetric flow rate of gases entering or exiting control device, as determined by Method 2, dscm/h
C = organic concentration in ppm, dry basis, as determined by Method 25A
MW = molecular weight of propane, 44
0.0416 = conversion factor for molar volume, kg-mol/m3 (@ 293 K and 760 mm Hg)
10-6 = conversion from ppm
where:
EA = total organic mass emission rate, kg/y
Eh = total organic mass flow rate for the process vent, kg/h
H = total annual hours of operations for the affected unit, h
La. Admin. Code tit. 33, § V-1711