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CLEARWA"-TER <br /> G R O U P ! \ C <br /> Environmental Services <br /> Based on the flow rates, vacuums, well screens, and radius of influence data, the soil <br /> air permeabilities were approximated according to Johnson, et al , (1990) using the <br /> software guidance system HyperVentilate© The results indicate that the <br /> permeability of the vadose zone soil around VW-2 and VW-3 are similar, and are <br /> approximately 3 to 4 darcies Vacuum, flow rate and permeability data is presented <br /> in Appendix E <br /> Soil vapors were tested from wells VW-1, VW-2, and VW-3 to evaluate volatile soil <br /> gas concentrations These samples were analyzed for TPHg and BTEX by Trace <br /> Analysis Laboratory, Inc The sample results from VW-1 revealed 27,000 mg/m3 <br /> TPHg and 6,840 mg/m3 total BTEX with the vapor extraction system operating The <br /> sample results from VW-2 revealed 150,000 mg/m3 TPHg and 35,900 mg/m3 total <br /> BTEX with the vapor extraction system operating The sample results from VW-3 <br /> revealed 130,000 mg/m3 TPHg and 29,200 mg/m3 total BTEX with the vapor <br /> extraction system operating Air sample analytical results are summarized on Table <br /> 5 Certified analytical reports are presented in Appendix B <br /> The sample results indicate that volatilization from the groundwater/air interface is <br />• significant, particularly in the vicinity of VW-2 and VW-3 At the flow rates <br /> induced during the test (12 cfm), hydrocarbon recovery rates from VW-2 and VW-3 <br /> were approximately 150 lbs/day (25 gal/day) each Although hydrocarbon <br /> concentrations were less in the sample from VW-1, the higher flowrates achieved <br /> from that well (60 cfm) produced hydrocarbon recovery rates of approximately 145 <br /> lbs/day (24 gal/day), comparable to wells VW-2 and VW-3 Again, it is worth noting <br /> that approximately a tenth of the contaminated soil pore volume was extracted <br /> when the air samples were collected Hydrocarbon recovery rates over a moderate <br /> period of time (several months) would likely be lower than those presented here <br /> However, if long term hydrocarbon recovery rates an order of magnitude lower <br /> than those presented here, they are still great enough to consider soil vapor <br /> extraction as a remedial alternative <br /> 5 3 4 Air S ar Test Results <br /> Following the soil vapor extraction test on VW-3, an air sparge test was conducted <br /> using sparge well SW-1 Vapor continued to be extracted from VW-3 during the <br /> sparge test An initially high pressure (15 psi) was required to overcome capillary <br /> pressures and induce flow into the sparge well Once flow was induced, pressures <br /> dropped to 7 psi and the flow stabilized around 13 cfm At the same time, a vacuum <br /> of 46 in w c column was applied to VW-3, which produced a flowrate of 8 cfm <br /> Pressures were observed in all observation wells, indicating that vapor extraction <br /> from VW-3 was unable to capture all sparge vapors In an attempt to control sparge <br /> vapors, flow into the sparge well was reduced to 10 cfm at 3 psi, and vacuum at VW- <br /> 3 was increased to 60 in w c , which produced a flowrate of 11 cfm (the limit of the <br /> test blower package) At these vacuums/pressures and flowrates, observation wells <br /> D-107, PAR/RAP 13 June 11, 1996 <br />