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F <br />4) <br />ATTACHMENT A <br />REMEDIAL SYSTEM PERFORMANCE EVALUATION <br />Soil vapor extraction (SVE) and groundwater extraction were initiated on June 14, 2003 A brief <br />description and performance evaluation of the remedial system during the third quarter 2003 is <br />presented below Certified laboratory analytical reports, chain -of -custody documentation, and field <br />data sheets are included as Attachment A -A <br />SVE System <br />The SVE system was started on June 14, 2003, and is comprised of 6-SVE wells (SVE-1, SVE-2, <br />MW -1, MW -2, MW -4, and EW -7) The SVE system utilized a Thermtech VAC 50 thermal/catalytic <br />oxidizer (Cat -Ox) as the abatement device The SVE system operates under San Joaquin Valley Air <br />Pollution Control District Permit to Operate N-4826-1-0 <br />The SVE system was approximately 66% operational this quarter Downtime was due to high <br />temperature shut -offs and a car crashing into the remedial compound Approximately 16,230 pounds <br />(lbs) of TPHg, 894 Ib of benzene, and 1,753 lb of MtBE were removed this quarter An estimated <br />16,698 lbs of TPHg, 94 lbs of benzene, and 1,809 lbs of MtBE have been removed since remediation <br />was initiated at the site <br />SVE system operational and analytical data, including hours of operation, applied vacuum, flow rate, <br />ambient dilution status, field FID measurements, influent TPHg and benzene concentrations, and <br />mass removal data are presented in Table A-1 Emissions data is provided in Table A-2 Graphical <br />illustrations of TPHg and benzene mass removal and concentration data are shown on Figures A-1 <br />and A-2 <br />Groundwater Extraction System <br />The GWE system is comprised of submersible pumps installed in 2 GWE wells (EW -1 and EW -6) and <br />connected to an air stripper and three 2,000 -granular activated carbon vessels Extracted <br />groundwater is treated by the air stripper and carbon vessels prior to discharge to the City of Stockton <br />sanitary sewer During the third quarter of 2003, the GWE system pumped 67,200 gallon of <br />groundwater at a pumping rate of 1 2 gpm Approximately 47 5 pounds (lbs) of TPHg, 1 53 Ib of <br />benzene, and 615 lb of MtBE were removed this quarter An estimated 47 5 lbs of TPHg, 1 53 lbs of <br />benzene, and 615 lbs of MtBE have been removed since remediation was initiated at the site GWE <br />system operational data is included in Table A-3 <br />Groundwater Batch Extraction <br />Batch groundwater extraction was initiated in March 2002 and consisted of extracting groundwater from <br />onsite wells MW -1, MW -4, MW -6, and EW -1 with a vacuum truck Batch extraction was performed twice <br />a month until the construction of the permanent remedial system began in November 2002 Batch <br />extraction was re -started in September 2003 as an interim remedial approach to reduce petroleum <br />hydrocarbon concentrations in offsite extraction wells and for offsite plume control pending connection of <br />