Laserfiche WebLink
X�f TI <br /> ' S E C O R <br /> ,� tl <br /> 3 1x <br /> 7 <br /> 1 l� <br /> ATTACHMENT A <br /> REMEDIAL SYSTEM PERFORMANCE EVALUATION � 1� <br /> ' A dual phase extraction (DPE) system, consisting of the application of combined soil vapor extraction <br /> (SVE) and groundwater extraction (GWE) technologies, was Initiated at the site on June 14, 2003 A <br /> brief description and a performance evaluation of the DPE system during the second quarter 2005 <br /> are presented below Certified laboratory analytical reports, chain-of-custody documentation, and field h. <br /> data sheets are included as Attachment A-A <br /> yds <br /> Soil Vapor Extraction N <br /> 1 � <br /> SVE was started on June 14, 2003 The SVE portion of the DPE system is comprised of 6 SVE wells d <br /> (SVE-1, SVE-2, MW-1, MW-2, MW-4, and EW-7) and a Thermtech VAC 50 thermal/catalytic oxidizer <br /> ' (Cat-Ox) as the abatement device The SVE system operates under San Joaquin Valley Air Pollution :y- <br /> Control District Permit to Operate N4826-1-0 <br /> r <br /> The SVE system was approximately 66% operational this quarter Approximately 53 pounds (lbs) of <br /> TPHg, 0 5 Ib of benzene, and 1 Ib of MtBE were removed this quarter An estimated 24,111 lbs of <br /> TPHg., 104 lbs of benzerie, and1.872 lbs of MtBE have been removed sine remediation was Initiated , <br /> at the site <br /> 4 <br /> ' SVE system performance data, including hours of operation, applied vacuum, flow rate, ambient <br /> dilution status, flame Ionization detector (FID) field measurements, influent TPHg and benzene <br /> concentrations, and estimated mass removal data are presented in Table A-1 Soil vapor emissions 3 <br /> ' data is provided In Table A-2 Graphic illustrations of soil vapor TPHg and benzene mass removal <br /> and concentration data are shown on Figures A-1 and A-2 l <br /> Groundwater Extraction System <br /> 4� <br /> The GWE portion of the DPE system is comprised of submersible pumps Installed In wells EW-1 and <br /> EW-6 and "slurp" tubes installed in wells MW-4 and EW-7, which are connected to an air stripper and <br /> ' three 2,000 Ib-granular activated carbon vessels Extracted groundwater is treated prior to discharge <br /> to a City of Stockton sanitary sewer line During the second quarter 2005, the GWE system pumped <br /> and treated approximately 145,000 gallons of groundwater, removing approximately 0 5 lbs of TPHg, <br /> 0 0 lbs of benzene, and 0 3 lbs of MtBE An n estimated 112 8 lbs of TPHg, 4 04 lbs of benzene and <br /> 139 9 lbs of MtBE have been removed by GWE since the DPE system began operating at the site <br /> WE system performance data Is included In Table A-3 Groundwater treatment effluent data Is <br /> included in Table A-4 Graphic Illustrations of TPHg and benzene mass removal from extracted <br /> ' groundwater and groundwater concentration data are shown on Figures A-3 and A-4 <br /> l <br /> r <br /> c y <br /> f <br /> IBP-ARC0149321QMRs1200512QMR05 doc ! <br /> r <br /> 1 <br />