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Table 1 <br /> Source Test Summary <br /> USA Gasoline Service Station No 65 <br /> 2500 West Lodi Avenue <br /> Lodz,California <br /> 10/22/2003 11/4/2003 <br /> Total Influent Concentz ztzons, rng/m3 <br /> Total petroleum hydrocarbons as gasoline 1 200 140 <br /> Benzene <1 3 <0 25 <br /> Toluene <1 3 <0 25 <br /> Ethylbenzene <1 3 <0 25 <br /> Total xylenes 3 3 68 <br /> MTBE 2.10 80 <br /> Effluent Concentrations,mg/m3 <br /> Total petroleum hydrocarbons as gasoline <15 <1 <br /> Benzene <0 15 <0 15 <br /> Toluene 0 18 <0 15 <br /> Ethvl benzene <0 15 <0 15 <br /> Total wlenes 049 <0 15 <br /> MTBE <0 15 <0 15 <br /> Destruction Efficiencies, % <br /> . Total petroleum hydrocarbons as gasoline >98 75 >89 63 <br /> JBenzene >92 00 >40 00 <br /> MTBE >99 96 >99 80 <br /> Estimated Discharge , lbs/day <br /> Total petroleum hvdrocarbons as gasoline <0 079 <0 028 <br /> Benzene <0 0008 <0 0003 <br /> MTBE <0 0005 <0 0003 <br /> Influent Flowrate into carbon vessel (scfin) 5698 21 10 <br /> Applied Vacuum ("WC) 10 10 <br /> Influent Temperature(°F) 72 72 <br /> ntg/nz' = milligrams per cubic meter <br /> scfrn = Actual flo« rate after temperature& pressure cotrectzons <br /> "WC = inches water cohmin <br /> "F = degree Fahrenheit <br /> lbs/day = pounds per day <br /> -- — —— --- ' -- _ <br /> -See flow rate correction in Appendix C <br /> Note Detailed calculations are presented in Appendz\C <br /> SoUrCL I est Calcs& Sununary_I 106 Pagel <br />