| A. System Measurements Performed by TUV, Rheinland, Cologne, Germany V/L = 1.5 RVP = 10.16 psia (summer grade gasoline) Storage Tank Liquid Temperature = 59 F True Vapor Pressure = 5.18 psia Headspace Equilibrium Concentration = 35 percent
Mass Balances: May 4, 1998: Volume Dispensed = 4,005 L Feed = 3384 L, percent HC = 29.3, g HC = 2699 Retentate = 1515 L, percent HC = 1.24, g HC = 51.3 Permeate = 1869 L, percent HC = 51.4, g HC = 2616
April 27-28, 1998: Volume Dispensed = 3,599 L Feed = 2979 L, percent HC = 28.3, g HC = 2297 Retentate = 1148 L, percent HC = 0.52, g HC = 16.2 Permeate = 1831 L, percent HC = 45.8, g HC = 2281
Measured Vent Emission Values: May 4, 1998: 5.61E-03 lb HC/gallon dispensed April 27-28, 1998: 5.31E-03 lb HC/gallon dispensed
B. Average Value: (5.61E-03 + 5.31E-03)/2 = 5.46E-03 lb HC/gallon dispensed
C. Predicted Value from ARID’s mathematical Evaporative Loss Model (ELM): 5.55E-03 lb HC/gallon dispensed
D. Model Accuracy: 5.46/5.55 = 98.4 percent
E. Actual Emissions: (Assuming No Membrane System Installed) 4.91 Tons/yr-station @ 150,000 gallons per month = 1,890 gallons/yr-station
F. Membrane System Recovery Efficiency: May 4, 1998: 97 percent (2,616/2,699) April 28, 1998: 99 percent (2,281/2,297) |