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r • <br /> . yc <br /> v 1' <br /> - <br /> - <br /> n; <br /> TABLE 2 <br /> SOIL VAPOR EXTRACTION PILOT TEST RESULTS <br /> EXTRACTED VAPOR CONCENTRATIONS (in µgli) <br /> MANTECA BEAN FACILITY, MANTECA, CALIFORNIA <br /> MAY 8-14, 1990 <br /> - SAMPLE FLOW RATE ELAPSED TIME BENZENE TPH-G <br /> POINT (CFM) (HOURS) (µI 11) (µ91I) <br /> MW-2A 130 0.33 5,800 170,000 <br /> MWI 130 22.75 1,200 82,000 <br /> MW-2C 130 45.25 1,200 83,000 <br /> MW-2D 130 64.75 750 56,000 <br /> MW-2E 130 -,135.25 220 20.000.,,..- <br /> MW-3A <br /> 0.0001MW-3A 130 0.95 3,100 110,000 <br /> MW-5A 130 0.88 510 26,000 <br /> MW-6A 130 1.00 59 3,400 <br /> The highest soil vapor concentrations were measured in wells near the former underground tank <br /> (MW-2 and MW-3), as expected from the results of the soil gas survey. li and MW-6 exhibited one <br /> and two orders of magnitude lower benzene concentrations, respectively. <br /> Soil vapor was extracted from MW-2 at a rate of 130 cfm for 135 hours to determine the rate at <br /> 9 which hydrocarbon concentrations decrease with time. A graph of benzene and TPH-G concentration <br /> versus gime is included in Appendix I. At the start of the test,0.04 feet of separate phase petroleum was <br /> measured in MW-2. No separate phase petroleum was detected on the second day. The water table had <br /> mounded up approximately 0.79 feet due to the negative pressure exerted by the vacuum blower. The <br /> blower was off due to an electrical failure between hours 40 and 44,hence samples MI and MW-2C <br /> have similar concentrations of TPH-G and benzene. The p&oleum�hydrocarbon mass extraction rate: <br /> fldm MW-2 at the'end of the test was 233 lbs(day <br /> The pilot test was successful in providing data with which to design an extraction and treatment <br /> system. The radius of influence was evaluated for different tiuw ,aces to allow selection of the proper <br /> vacuum blower. Hydrocarbon concentrations.were evaluated from several candidate extraction wells to <br /> allow extraction well selection. Finally, a hydrocarbon dissipation curve was calculated for predicting <br /> concentrations to be treated after prolonged operation of the system. <br /> 3.3.3 Soil Vapor Extraction and Emission Control System Design <br /> - remove rale from W 2 after 135 hours or•. <br /> of vapextractlan-was,233jbs/day�. ----- <br /> The San Joaquin County Air Pollution Control District uses risk based criteria to evaluate allowable <br /> L .GROUNIAVATEIZ <br /> Twisol.oc)`,INC. <br />