Laserfiche WebLink
I II <br /> i { <br /> E` I <br /> € 1 I <br /> Table 4 Ii <br /> Operating Parameters <br /> Former Unocal Station No 5098 <br /> 5400 and 5606 Pacific Avenue <br /> Stockton, California <br /> Note <br /> (1) scfm=acfm'(460+60)1(460+o F)"4071(407+15) <br /> where 407=atmospheric pressure in inches Water Gauge and 15=blower discharge pressure in inches Water Gauge <br /> if 11 � <br /> (2)VOCs scfm=flow scfm"`VOCs ppmv"10-6 <br /> (3)Combustion Air Flow scfm=300'Valve%1100 I <br /> (4)Combustion Gases Flow scfm=Flow to Oxidizer scfm+Combustion Aur Row scfm <br /> (5)Combustion Gases VOCs scfm=Combustion Gases Flow scfm*(Combustion Gases VOCs ppmv-Background ppmv)'10� <br /> (6)DRE%= (VOC's scfm-Combustion Gases VOC's scfm)/VOC's scfm'100 <br /> (7) Calculated as 2%of LEL(1 4%v) II11 <br /> j <br /> (8) First sampling/data collection event after system switched from thermal oxidizer to activated carbon vapor abatement { <br /> (9) Measured from effluent stack <br /> ppmv-volume parts per million IE <br /> OF-temperature in degree Farehneit,egual to(460+°F) in degree 1,elven <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, NA-Not Analyzed NIA-Not Applicable <br /> I I� <br /> E <br /> I I <br /> I II I I <br /> I <br /> I <br /> I <br /> 06W--293 2 of 2 ENSR Corporation <br /> I I <br /> I � <br />