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3 1P <br /> Table 1 <br /> Source Test Summary i <br /> USA Gasoline Service Station No.65 <br /> 2500 West Lodi Avenue <br /> j, - Lodi,California <br /> f3 <br /> :i 8/1/03 <br /> Total Influent Concentrations,mg/m' <br /> Total petroleum hydrocarbons as gasoline 36,000 <br /> Benzene <10 <br /> Toluene <10 <br /> Ethylbenzene <10 <br /> Total xylenes <10 <br /> MTBE 57 <br /> Effluent Concentrations,mg/m3 <br /> Total petroleum hydrocarbons as, gasoline <12 <br /> Benzene <0.12 <br /> Toluene <0.12 <br /> Ethyl benzene <0.12 <br /> Total xylenes <0 12 <br /> MTBE <0.12- <br /> 1 - <br /> Destruction Efficiencies,% " <br /> Total petroleum hydrocarbons as'gasoline >99.97 <br /> Benzene >98.86 <br /> MTBE ! >99.79 <br /> I <br /> Estimated Discharge,lbs/day .j. <br /> Total petroleum hydrocarbons as,gasoline <0.08 <br /> Benzene X0.0008 <br /> MTBE <0:0008 <br /> r • <br /> Influent Flowrate into Oxidizer (acf n) .. 73.61 <br /> Applied Vacuum("WC} 18 <br /> Influent Temperature(°F) 80 <br /> E" <br /> 1' <br /> Mg/M3 = milligrams per cubic Imeter • ' <br /> actin = Actual flow rate after temperature&pressure corrections <br /> "WC = inches water column <br /> °F = degree Fahrenheit <br /> lbs/day = pounds per day <br /> = See flow rate correction in Appendix C <br /> Note: Detailed calculations are presented in Appendix C <br /> ,i <br /> Source Test Calcs&Summary Revised Page I <br /> e. <br />