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' Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> • SIERRA LUMBER-375 West Hazelton Avenue, Stockton, CA <br /> 1 <br />' 3. 26 February 2003 to 20 March 2003 <br /> The average analytical TPH-g concentration for this time interval was determtned to be 84,ug/l(02-26-03=27,ug/1 and <br /> 03-20-03= 140,ug/l,avg =84#g/1) The average flow rates during this time was calculated at 0 35 inches of water or <br />' approximately 33 cubic feet per minute(table 6), the operational period was equal to 528 hours of running time <br /> C z 84 µg/1=0 000084 kg/m' <br />' Q = 0 35 inches water = 33 ft'/min <br /> t=528 hours <br /> Converting Q to rn3/hour yields <br />' Q=(33 ft:/tnin)-(60 nun/hour) -(0 0283168rn'/ft)=56 1 m3/hour <br />' M=C- Q- t=(0 000084 kg/m3) -(56 1 m3/hour)- (528 hours)=2 50 kg of gasoline <br /> Converting kg of gasoline to pounds of gasoline yields <br /> 2 50 kg of gas - 2 2046 lbs of gas/kg of gas=5 51 lbs of gasoline <br /> Converting pounds of gasoline to gallons of gasoline yields <br /> 5 51 lbs of gas - 0 16 gal of gas/lbs of gas =0 88 gallons of gasoline <br /> 1 <br /> 1 <br /> 1 <br /> 1 <br />