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Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER- 375 West Hazelton Avenue, Stockton, CA <br /> 2. 23 April to 13 May 2002 <br />' The average analytical TPH-g concentration for this time interval was determined to be 180,ug/l(04-23-02= 190/cg/l <br /> and 05-13-02= 170,ug/l,avg =180 pg/1) The average flow rates dung this time was calculated at 0 43 inches of water <br /> or approxttnately 37 cubic feet per minute(table 6), the operational pend was equal to 480 hours of running time <br />' C 180 Ag/l=0 000180 kg/m' <br /> Q = 0 43 inches water= 37 ft/mm <br /> t=480 hours <br />' Converting Q to r0hour yields <br />' Q=(37 fl/min)•(60 min/hour)•(0 0283168i0ft3)=62 86 rn3/hour <br /> M=C• Q • t=(0 000180 kg/rn3) 9(62 86 rn/hour) • (480 hours)=5 43 kg of gasoline <br />' <br /> Converting kg of gasoline to pounds of gasoline yields <br /> 5 43 kg of gas• 2 2046 lbs of gas/kg of gas= 1197 lbs of gasoline <br /> Converting pounds of gasoline to gallons of gasoline yields <br /> 11 97 lbs of gas • 0 16 gal of gas/lbs of gas =1.92 gallons of gasoline <br /> Ii <br /> I <br /> I <br /> I <br /> I <br /> I <br /> As <br /> I <br /> f <br />