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{ Table 5 M <br /> Operating Parameters <br /> t Former Unocal Station No 5098 <br /> 5400 and 5606 Pacific Avenue <br /> Stockton, California <br /> r, <br /> Note j <br /> (1) scfm=acfm*(460+60)/(460+0 F)*407/(407+15) ' <br /> where 407=atmospheric pressure in inches Water Gauge <br /> and 5=Flower discharge pressure in inches Water Gauge t <br /> i <br /> F <br /> (2)VOCs scfm=flow scfm*VOCs ppmv*10-6 I; F <br /> (3)Combustion Au Flow scfm=300*Valve%/100 ji F <br /> r <br /> (4)Combustion Gases Flow scfm=Flow to Oxidizer scfm+1, <br /> i Combustion Air Flow scfm <br /> (5)Combustion Gases VOCs scfm=Combustionbases Flow scfm*(combustion Gases VOCs ppmv-Background ppmv)*10"s r ` <br /> (6)DRE%_ (VOC's'scfm-Combustion Gases VOC's scfm)NOC's scfm*100 r <br /> (7) Calculated as 2%of LEL(1 4%v) j ; <br /> ppmv-volume parts per million s �, 1� <br /> OF-temperature in degree Farehneit,equal to(460+°F)in degree!!!Kelvin s <br /> acfm-actual cubic feet per minute, scfm-standard cubic feet per minute(at 14 7 psis and 60°F) <br /> DRE-Destruction and Removal Efficiency, s N -Not Anained N/A=Not Applicable _ <br /> t , <br /> � r r <br /> - <br /> i <br /> IL <br /> - <br /> F <br /> ¢ a I <br /> E <br /> 4 <br /> s j r <br /> { I <br /> - <br /> I r� G <br /> E � � <br /> s 1 <br /> I L I' <br /> a 1 <br /> 06940_2 2# ENSR Co oration <br />