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�` .�-. } �a-t,^�t ' � � Y! .'��a �YF � �r�- � r �r�✓�' ,,� „b�b.. '� - v�k":*,y�rrx i- �f sr. �K <br /> a <br /> per: <br /> i <br /> p <br /> REGAL 603 8/16/91 <br /> were derived from the Bouwer and Rice Slug test. <br /> 6, The gasoline range contaminated ground water <br /> plumhas <br /> migrated past monitor well MW8 and is approaching eW; <br /> 7. Soil contamination is limited to the area directly <br /> earby <br /> beneatwell <br /> h the <br /> extendskfromathe�25 foot on and ndepth totop monitoring <br /> of ground <br /> MW10 an <br /> water. <br /> 8. A vapor extraction source test performed on MW10 show a <br /> steady flow rate of 50 scfpm can be achieved from this <br /> well with an average concentration of 37,867 ppm <br /> gasoline vapor and 14% methane. <br /> RECOMMENDATIONS <br /> 1. Proceed with the permitting "Authority to Construct" and <br /> "Permit to operate" for the "Hirtz" incinerator. <br /> 2. Finalize the permit to place treated ground water to the <br /> City of Stockton's sewer. <br /> 3. Recover contaminated ground water from monitor wells MW1 <br /> and MW3, using a gasoline rated air and <br /> pimps at a <br /> combined rate of 2000 gallons per day. <br /> 4. Place data logger transducers in monitor wells MW2, MW4, <br /> MW 7 and MW8 and record depth to water for one week; <br /> then obtain weekly depth to water measurements on all <br /> wells, after the data loggers have been removed, for one <br /> month and then monthly depth to water for one year, to <br /> show the radius of influence the pumping is providing. <br /> The data obtained should be calculated upon receipt, to <br /> justify the pump rate at monitor well MW3. <br /> 5, Pretreat the recovered ground water by removing <br /> svispended solids in a solids trap. This trap is vented <br /> to the incinerator and is heated/a:i.rstripped using a <br /> portion of the air supplied to the ,c:onvault" stripper. <br /> 6. Treat the recovered ground water by heated air <br /> stripping. <br /> 7. Sample the influent prior to the stripper and the <br /> effluent after the stripper to determine percent <br /> destruction and flow rates that will be needed for <br /> ongoing treatment. <br /> PAGE 2 <br />