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Groundwater Flow Direction: South-southeast <br /> Groundwater Gradient: 0.004 ft/ft <br /> SVE SYSTEM QUARTERLY OPERATION AND PERFORMANCE <br /> Equipment Inventory: _ Solleco 100 cfm electric catalytic oxidizer <br /> Operating Mode: Catalytic <br /> APCD Permit No.: N-4887-2-0 <br /> Influent TPHG Concentration End of Period: <15 milligrams per cubic meter (mg/m3 <br /> Influent Benzene Concentration End of Period: <0.15 m /m3 <br /> Flow Rate End of Period: 85.1 <br /> HC Destroyed this Period (tab): <4.88 lbs as TPHG <br /> Cumulative HC Destroyed: 4,095.14 lbs as TPHG <br /> Percent Time Operational: System operating in pulse mode <br /> DISCUSSION: <br /> At the time of the third quarter 2005 monitoring event, groundwater elevations had decreased between <br /> 0.40 and 1.63 feet in all wells since the previous monitoring event (April 7, 2005). Depth-to-water <br /> measurements were normalized to mean sea level (MSL), and were used to construct a groundwater <br /> elevation contour map (Figure 2). Wells S-1 and S-2 were dry. The groundwater flow direction on July <br /> 26, 2005, was generally to the south-southeast at an average gradient of 0.004 ft/ft, South-southeast <br /> groundwater flow direction has consistently been observed during previous monitoring events. <br /> TPHG (110 µg/L) was reported only in well MW-3. BTEX, MTBE, TBA, DIPS, ETBE, TAME, methanol, or <br /> ethanol were not reported in any of the wells. Analytical results are generally consistent with historical <br /> analytical data. TPHG, benzene, and MTBE data have been summarized on Figure 3. <br /> System Description <br /> Soil Vapor Extraction and Abatement(SVE) System <br /> The SVE system consists of a Solleco 100 cfm electric catalytic oxidizer (Model 100 SCAT) with a 5 <br /> horsepower (hp) blower. Upon system start-up (October 20, 2004), petroleum hydrocarbon laden soil <br /> vapors were extracted from wells VW-1, S-1, S-2, and MW-8 using the 5 hp blower package of the SVE <br /> system rated at 100 cfm at 14 inches of mercury. Figure 2 presents the locations of the vapor extraction <br /> wells, remediation system, and other pertinent site features. The extracted soil vapors were abated in the <br /> catalytic oxidizer prior to discharge to the atmosphere. The SVE system has an in-built hour meter and <br /> recordings are used to determine the operational uptime. Sample ports (influent, cat-influent, and effluent) <br /> are designated to collect air samples. The results of air samples are used to estimate the destruction <br /> efficiency of the system. <br /> Remedial activities at the site were initiated with a SVE system consisting of a 150 cfm Stealth Bobcat <br /> catalytic oxidizer (cat-ox) and was operated at the site between August 15, 2000 and August 15, 2002, <br /> under permit N-903-2-0. Due to low influent concentrations, the cat-ox system was replaced with a SVE <br /> system consisting of a 2.3 hp Fuji Blower and two 1,000 lbs vapor phase carbon units, which operated at <br /> the site between August 1, 2003 and March 12, 2004, under permit N-4887-1-0. The vapor phase carbon <br /> adsorption system was replaced with the currently operating Solleco 100 cfm electric cat-ox in October <br /> 2004. The 150 cfm Stealth Bobcat SVE system operated at the site for a total of 13,624 hours and <br /> removed approximately 3,467 pounds of TPHG and the carbon adsorption system has operated at the site <br /> KAUSA Gasolin600651QtrIy120051USA_65_3Q05.DOC 57RATU5 <br />