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ARCO Products Company VES Operating Report <br /> First Quarter 1996 <br /> • SUMMARY OF OPERATIONAL DATA <br /> Reporting Period 111196-3/31/96 <br /> Current well source NA <br /> Current source(prior to dilution,in ppmv) Influent summary(laboratory data) <br /> TPH conc this period NA <br /> TPH conc last period NA <br /> Initial TPH conc NA <br /> Benzene conc this Period NA <br /> Benzene conc last period NA <br /> Initial benzene conc NA <br /> Current process(after dilution,in ppmv) Influent summary(laboratory data) <br /> TPH conc this period NA <br /> TPH conc last period NA <br /> Initial TPH conc NA <br /> Benzene conc this period NA <br /> Benzene conc last period NA <br /> Initial benzene conc NA <br /> System parameters/Emissions <br /> Efluent TPH conc emissions(lb/day) NA <br /> . Effluent TPH permit requirement VOC emmisstons not to exceed 1 4 lbs/day <br /> %TPH destruction NA <br /> Effluent benzene conc emissions(lb/day) NA <br /> Effluent benzene permit requirement VOC emmissions not to exceed 1 4 lbs/day <br /> %benzene destruction NA <br /> Average stack temperature NA <br /> Average source flow(SCFM) NA <br /> Average process flow(SCFM) NA <br /> Average source vacuum(in H2O) NA <br /> Assumptions <br /> I The quantity of hydrocarbons removed was estimated using the influent TPH concentrations at the oxidizer inlet <br /> 2 Percent up time was calculated by dividing actual operating hours as determined from hourmeter readings by the <br /> total hours of the reporting period <br /> 3 Source flow,process flow,and source vacuum are based on averages established during site visits <br /> Example calcculations <br /> ' TPH recovered(in Ibs/day)=C x Q x 0 00038 <br /> HC Removed=Q x C x 0 00038 x(#hours/24) <br /> • LB HC/Utility=LB HC/(therms x 60 cents/therm+ kwh x 12 cents(kwh) <br /> Where <br /> C=Average influent TPH concentration(ppmv) <br /> Q=Influent flow rate(SCFM) <br /> 0 00038 is a constant and is derived as follows 1 0E-06ppmv x 60min/1 hr x 24 hr/day x 1 lb mol/379 cu R x 100 lbs/lb mol <br />