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f <br /> KLEINFELDER <br /> in NP-70' and NP-80' appears to be from a lifting effect as seen in the past caused by.the air <br /> sparging and soil vapor extraction remedial action on the source area of the plume as evidenced <br /> by the decreasing concentrations in NP-90'. <br /> Most downgradient wells (MW-DIS-9, MW-DIS-I ls, MW-DIS-1 ld, MW-DIS-12, MW-DIS-13, <br /> MW-DIS-14s, MW-DIS-14d and MW-DIS-15) all showed decreasing concentrations of 1,2- <br /> DCA and non-detectable concentrations of BTEX compounds, EDB, and oxygenates. Only <br /> i MW-DIS-lls showed an increased concentration of TPH-g and 1,2-DCA. The 1,2-DCA <br /> I <br /> concentration in MW-DIS-14s continued to show a decreasing trend during the 2004 monitoring <br /> period (down to 2.0 ug/l from 3.4 ug/1). It should be noted that the concentration of 1,2-DCA <br /> reported for MW-DIS-15 Glacier Court was the lowest since monitoring this location began (2.1 <br /> ug/1). <br /> Based upon the screened depth intervals of the monitoring wells, which range from as shallow as <br /> 65 feet to 85 feet and as deep as 154 feet to 164 bgs, compared to the depths of the ozone and air <br /> sparging wells at 140 feet bgs, it appears that the sparging continues to lift deeper contamination <br /> into the shallower screened zones of the monitoring wells during the treatment process. The 1,2- <br /> DCA increases are anticipated as the lifting effect, and consequential resonation in <br /> concentrations, that is occurring at the front of the plume (downgradient of the source area) <br /> continues until the deep contamination at the source area is more significantly mitigated. <br /> GROUNDWATER TREATMENT SYSTEM OPERATION <br /> The soil vapor extraction system installed by CH2M Hill was replaced by Kleinfelder during <br /> 2003 with an air sparging (AS)/high vacuum soil vapor extraction (SVE)/ozone injection system. <br /> The AS/SVE system consists of a network of two air sparging wells (shallow/deep) and a vapor <br /> extraction well positioned at five distinct locations, totaling fifteen wells. The ozone injection <br /> system consists of a horizontally directional drilled conduit for ozone/air transmitted to a system <br /> of wells triple-nested at three different depths below groundwater, at five separate locations, <br /> equaling fifteen wells. Active remediation began in May 2003 in the source area (actual Disco <br /> site) by means of AS/SVE utilizing a thermal oxidizer unit. Continual operation of the thermal <br /> oxidizer began in June 2003, In July 2003, the AS/SVE unit was converted from a thermal <br /> oxidizer to catalytic oxidizer thereby optimizing the efficiency through fuel uptake. The ozone <br /> injection system began consistent operation within the downgradient portion of the plume in <br /> September 2003. The system has only been inoperable during periods of system maintenance <br /> and enhancements. <br /> c <br /> 1 Photo Ionization Detector (PID) samples were taken from the five vapor extraction wells (VE-1 <br /> through VE-5) each month in during the Third Quarter 2004. Extraction wells VE-2 through <br /> VE-5 averaged approximately 35 ppm for the three months during the Third Quarter. VE-1 <br /> (located in the former tank area) ranged from approximately 950 to 1100 ppm (before PID <br /> termination). Air inlet sampling was conducted at the main manifold of the catalytic oxidizer on <br /> June 2, 2004. TPH-G was detected at a concentration of 460 ppm, showing an increase from the <br /> i previous (March 22, 2004) sampling event of 28 ppm, still below the 1,400 ppm detected during <br /> ++ the September 2003 sampling event. <br /> 1 <br /> 12280.M0N/ST04R1610/JZ:Iv Page 2 of 13 <br /> 0 2004,Kleinfelder,Inc. December 10,2004 <br />