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I t s i 1 i <br /> r1 Table 4 <br /> � <br /> Or,erating Parameters <br /> { = <br /> r ii 1 #€ <br /> = For 6r Unocal Station No 5098 <br /> 5400 and 5606 Pacific Avenue, Stockton r 1 <br /> (3)Combustion Air Flow scfm =300Valve%1100 l; <br /> (4)Combustion Gases Flow scfm =Flow to Oxldlze�scfm+Comb! st€on Air Flow scfm p A i , ° I <br /> (5)Combustion Gases VOCs scfm=Combustion Gases Flow scfm'(Colmb€.ist€on Gases VOCs ppmv-Background ppmv)`10-6 <br /> (6)DRE% = (VOC's scfm-Combustion Gases VOC's scfm)NOC's scfm*100 <br /> (7) Calculated as'A.of LEL(1 4%v) <br /> ppmv-volume parts per million <br /> OF-temperature in degree Farehne€t,equal to(460�F)€n degree Kelvin <br /> 1 I i 3 ' <br /> acfm-actual cubic feet per minute, scfm-standard cubic feet per m€n te(at 14 7 ps€a and 60°F) € <br /> DRE-Destruction and Removal Efficiency, NAIj Not{Anal yzed NIA:Not Applicable <br /> n k P G� -• � - l � 1 � � T� �� � - � _ z <br /> 4 <br /> F z} ! a <br /> 1 i Y RR I f <br /> 4_ t Y a <br /> r <br /> k ,I r T <br /> r S � <br /> e <br /> 06940-29 € j _ ENSR C oratron <br /> 1k <br /> I ik 1 4 j <br />