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Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER- 375 West Hazelton Avenue, Stockton, CA <br /> 3. 20 August 2002 to 11 September 2002 <br /> The average analytical TPH-g concentration for this time interval was determined to be 150µg/1(08-11-02=220,ug/l <br /> and 09-11-02=80µg/l,avg = 150µg/1) The average flow rates during this time was calculated at 0 43 inches of water <br /> or approximately 37 cubic feet per minute(table 6),the operational period was equal to 528 hours of running time <br /> C = 150 jig/1=0 000150 kg/xn3 <br /> Q z 0 43 inches water = 37 ft3/min <br /> t=528 hours <br /> Converting Q to m3/hour yields <br /> Q=(37 WImin)-(60 mm/hour)•(0 0283168&/ft3)—62 86&/hour <br /> M=C• Q• t=(0 000150 kg/m3) •(62 86 m3/hour) • (528 hours) =4 98 kg of gasoline <br /> Converting kg of gasoline to pounds of gasoline yields <br /> 4 98 kg of gas• 2 2046 lbs of gas/kg of gas= 10 97 lbs of gasoline <br /> Converting pounds of gasoline to gallons of gasoline yields <br /> 10 97 lbs of gas • 0 16 gal of gas/lbs of gas =1 76 gallons of gasoline <br /> I• <br /> I <br /> I <br /> I <br /> i <br /> i <br /> i <br /> i <br /> i <br /> i <br />