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Y) l <br /> Canepa s Car Wash <br /> 6230 Pamfic Avenue,Stockton,CA <br /> First Quarter Groundwater Monitonng Report,January 2005 <br /> Page 5 of S <br /> • TREATMENT SYSTEM STATUS UPDATE <br /> Sampling of the Soil Vapor Extraction (SVE) system was suspended during the first quarter of 2004 and <br /> shut down on January 31, 2004, to allow for modifications to the system and property development In a <br /> letter dated October 17, 2003, the SJCEHD approved the Remedial Action Plan (RAP) submitted by <br /> Condor, dated March 3, 2003, for upgrade of the SVE system and installation of a groundwater pump and <br /> treat system to operate in tandem with the upgraded SVE system Installation of the pump and treat <br /> system and upgraded SVE system was completed in September 2004 <br /> The groundwater pump and treat and upgraded SVE system was constructed such that petroleum <br /> hydrocarbons that are removed from the liquid phase treatment stream are fed as a vapor phase into the <br /> catalytic oxidizer as part of the total vapor phase influent Groundwater from MW-I and/or MW-1 I is <br /> pumped into the SVE liquid/vapor separator Accumulated liquid is pumped to the air-stnpper storage <br /> tank and through a heat-exchanger that is integrated into the SVE effluent stack prior to entering the air- <br /> stripper The air-stnpper removes BTEX and MTBE constituents with a removal efficiency of <br /> approximately 99% and 32%, respectively Liquid phase effluent from the air-stripper is pumped through <br /> two tanks, plumbed in series and loaded with 1000# of coconut-derived virgin activated carbon The <br /> carbon tanks are intended to adsorb residual MTBE, TBA, and other oxygenates Treated water is <br /> discharged to the sanitary sewer Vapor phase influent is drawn from the 9-well array through the <br /> liquid/vapor separator, and then into the catalytic oxidizer The catalytic oxidizer is operationally <br /> controlled to maintain temperature at 600-700 degrees F with a vapor flow rate of 100-300 SCFM The <br /> destructive efficiency of the catalytic oxidizer ranges from 95% to 99% Operational and efficiency data <br /> are included in Attachment D Laboratory certificates of analyses and chain-of-custody records are <br /> • included in Attachment F <br /> Initial inspection of the SVE system was conducted on September 30, 2004, and a follow-up inspection <br /> was conducted on October 7, 2004 In a letter report, Soil Vapor Extraction System, submitted to Karen <br /> DeGroot of the San Joaquin Valley Air Pollution Control District(SJVAPCD), dated November 30, 2004, <br /> Condor provided data required in the SJVAPCD Authority to Construct document to obtain a SJCAPCD <br /> Permit to Operate <br /> The City of Stockton Municipal Utilities District (MUD) authorized the initiation of discharge of treated <br /> groundwater on October 2$, 2004 Groundwater extraction and treatment, with subsequent discharge to <br /> the sanitary sewer began November 1, 2004 Monthly sampling and reporting of the final discharge of <br /> treated groundwater is required in the MUD groundwater discharge permit Those reports document the <br /> analytical results of the treated groundwater being discharged into the City of Stockton sanitary sewer <br /> system The laboratory analytical data for final discharge samples collected during October, November, <br /> and December 2004, and January 2005 indicated that none of the contaminants of concern were detected <br /> at or above the laboratory reported detection limits The laboratory analytical data for the final discharge <br /> sample collected on February 16, 2005 indicated that none of the contaminants of concern were detected <br /> at or above the lahnratnry rPnnrtPrl d�tPrhnn limitg event fnr X4 RP xxThin1k ;xiao :1_f__+_A 't <br /> I r Y evve .. �. <br /> concentration of 120 µg/l This concentration of MTBE exceeded the discharge limit set forth in the MUD <br /> groundwater discharge permit, and the system was shut down Corrective action is being undertaken The <br /> anticipated restart date is April 6, 2005 <br /> MASS REMOVAL AND DESTRUCTION CALCULATIONS <br /> The system was operational 1,430 hours between November I, 2004 and March 1, 2005, or 50% of the <br /> • time The groundwater treatment system has removed petroleum hydrocarbons from 299,216 gallons of <br /> groundwater during the dates and hours of operation indicated above Groundwater treatment system <br /> �1� CONDOR <br />