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discharge point located inside the bathroom of the on-site building The ABS pipe was connected to the <br /> existing sewer discharge line by a California licensed plumberduring the week of November 25, 2002 <br /> When the system is operated, groundwater is separated from the extracted vapor in a 50-gallon knockout <br /> ' tank located near the thermal oxidizingunit The knockout tank is equipped with water level sensors and <br /> when the knockout tank is approximately 80% full of groundwater, a transfer pump transfers the water <br /> ' from the knockout tank into a 1,000-gallon poly drop tank that is also located inside the remediation <br /> compound The drop tank is equipped with water level sensors and when the drop tank is approximately <br /> 80% full of groundwater, a second transfer pump transfers the water from the drop tank through the <br /> ' carbon filtration system The transfer-pump stops pumping when the drop tank is reduced to 55% <br /> capacity <br /> ' The aqueous-phase carbon filtration system originally consisted of three ASC200 200-pound carbon <br /> vessels containing liquid-phase granular activated carbon The three ASC200 carbon vessels were <br /> connected in series by a hose connection system These canisters were replaced in December of 2003 <br /> with two 2000-pound carbon canisters to reduce the frequency and number of carbon change-outs and the <br /> associated operation and maintenance (O&M) costs The two carbon vessels are setup in series with <br /> sampling ports before the lead vessel, in between the lead and lag vessels, and after the lag vessel <br /> ' AS Treatment System <br /> ' The AS system consists of a GAST 2567-P132-T908X rotary vane, 2- horsepower, air compressor This <br /> blower is capable of injecting at a maximum of 20 pounds per square inch (PSI) at low flow rates The <br /> maximum flow rate is approximately 21 SCFM <br /> There are two AS remediation wells (AS 1 and AS2), which are installed to 40 feet bgs with five feet of <br /> well screen Each AS wellhead connection includes a gate valve, pressure gauge and flow rate <br /> measurement port ATC started the AS system on February 13, 2003 <br /> ' REMEDIATION SYSTEM MONITORING <br /> ' Soil Vapor Extraction System Monitoring <br /> During the third quarter 2005 reporting period, ATC personnel monitored the SVE system on July 7, July <br /> ' 26,August 31, September 27, and October 7,2005 <br /> Parameters monitored in the field included vapor extraction flow rates, hydrocarbon vapor concentrations, <br /> groundwater extraction rate, total groundwater discharged to the City of Stockton sanitary sewer, and total <br /> ' hours of system operation Field monitoring data are contained in Attachment 3 <br /> ' On July 26, August 31, and October 7, 2005, ATC personnel collected vapor samples from VW 1, VW2, <br /> MW 1, and from the influent and effluent vapor streams of the vapor extraction system The samples were <br /> transported under chain-of-custody documentation to SunStar Laboratories, Inc (Environmental <br /> Laboratory Accreditation Program Certificate No 2250) in Golden, Colorado and were analyzed for <br /> ' VOCs by EPA Method TO-14 <br /> On July 26, August 31, September 27, and October 7, 2005, ATC personnel collected water samples from <br /> ' the groundwater treatment and discharge component of the vapor extraction system Water samples were <br /> collected from the system influent, system effluent, and vessel 1 (i e, the effluent of vessel 1 which is in <br /> between canisters) of the groundwater treatment system and transported under chain-of-custody <br /> documentation to Argon Labs for analyses The water samples were analyzed for TPHg by EPA Method <br /> s lenviro1625961quart1yl3gr-2005 doc 5 ATC ASSOCIATES INC <br />