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' Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER- 375 West Hazelton Avenue, Stockton, CA <br /> 2• 30 October 2002 to 11 November 2002 <br /> The average analytical TPH-g concentration for this tune nntervaI was determined to be 260,ug/l(10-30-02= 130µg/l <br /> and 11-11-02=390,ug/l,avg =260,ug/1) The average flow rates during this time was calculated at 0 48 inches of water <br /> or approximately 39 cubic feet per minute(table 6), the operational period was equal to 288 hours of running time <br />' C = 260µg/1=0 000660 kg/m3 <br /> Q = 0 48 inches water = 38 ft3/min <br /> t=288 hours <br /> Converting Q to m3/hour yields <br />' Q=(38 fe/mm) •(60 nun/hour) •(0 0283168m3/ft3)=64 56 m3/hour <br /> M,C • Q• t=(0 000260 kg/m3)•(64 56 m3/hour) • (288 hours)=4 83 kg of gasoline <br />' Converting kg of gasoline to pounds of gasoline yields r <br /> 4 83 kg of gas• 2 2046 lbs of gas/kg of gas = 10.66 lbs of gasoline <br />' Converting pounds of gasoline to gallons of gasoline yields <br /> 10 66 lbs of gas • 0 16 gal of gas/lbs of gas =1 70 gallons of gasoline <br /> 1 <br /> I <br /> i <br /> I <br /> I <br /> I <br /> I - <br /> I <br /> f <br />