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Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER-375 West Hazelton Avenue, Stockton, CA <br /> 2. 17 July g 2002 to 20 August 2002 <br /> The average analytical TPH-g concentration for this time interval was determined to be 660,ug/l(07-17-02=1,100#g/l <br /> and 08-20-02=220,g/l,avg =660 pg/1) The average flow rates during this time was calculated at 0 51 inches of water <br /> or approximately 39 cubic feet per minute(table 6), the operational period was equal to 816 hours of running time <br /> C = 660 µg/1=0 000660 kg/m' <br /> Q = 0 51 inches water = 39 tt/min <br /> t=816 hours <br /> Converting Q to m'/hour yields <br /> Q=(39 fl'/nun) •(60 nun/hour)•(0 0283168m/ft)=66 26 m'/bour <br /> M=C• Q• t=(0 000660 kg/m) •(66 26 m3/hour) • (8 16 hours)=35 69 kg of gasoline <br />' Converting kg of gasoline to pounds of gasoline yields <br /> 35 69 kg of gas - 2 2046 lbs of gas/kg of gas=78 67 lbs of gasoline <br />' Converting pounds of gasoline to gallons of gasoline yields <br /> 78 67 lbs of gas • 0 16 gal of gas/lbs of gas =12 59 gallons of gasoline <br /> • <br />