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rW Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER- 375 West Hazelton Avenue, Stockton, CA <br /> 2. 21 February to 11 March 2002 <br /> I The average analytical TPH-g concentration for this tune interval was determined to be 395 gg/l(02-21-02=3104g/l <br /> and 03-11-02=480 F.cg/l,avg =395µg/1) The average flow rates during this time was calculated at 0 30 inches of water <br /> or approximately 30 cubic feet per minute(table 5),the operational period was equal to 432 hours of running time <br /> C = 395 Mg/l=0 000395 kg/m' 4 <br /> Q - 0 30 inches water :* 30 ft3/min <br /> t=432 hours <br /> IConverting Q to m3/hour yields <br /> Q =(30 ft3/min) •(60 nun/hour)•(0 0283168m'/ft3)=50 97 i0hour <br /> M=C• Q • t=(0 000395 kg/m') -(50 97 m3/hour) • (432 hours)=8 70 kg of gasoline <br /> I Converting kg of gasoline to pounds of gasoline yields <br /> 8 70 kg of gas • 2 2046 lbs of gas/kg of gas= 19 17 lbs of gasoline <br /> I Converting pounds of gasoline to gallons of gasoline yields <br /> 19 17 lbs of gas • 0 16 gal of gas/lbs of gas =3 06 gallons of gasoline <br /> I <br /> I <br /> • <br />