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1 <br /> I First Quarter 1996 Groundwater Monitoring& Remediation Status Report <br /> ' Moore Petroleum, 14800 W Frontage Rd,Manteca,CA <br /> April 24, 1996 <br /> Page 3 <br /> ' Vapor Extraction Remediation System Status <br /> In early 1995, Emcon installed a soil vapor extraction system consisting of a Remediation Service, <br /> Int'1 Spray Aeration Vapor Extraction (S A V E) system at the subject site The vapor extraction <br /> system was installed per San Joaquin Valley Unified Air Pollution Control District (SJVUAPCD) <br /> permit conditions The vapor extraction system consists of an internal combustion engine with <br /> catalytic converters mounted on the exhaust pipe During this reporting penod, soil vapor flow to <br /> the system has ranged from 35 standard cubic feet per minute (scfm) on February 22, 1996, to 47 <br /> ' scfm on January 23, 1996 <br /> Vapor samples were collected from the system influent and effluent on January 23, February 8, and <br /> ' on March 6, 1996 to demonstrate compliance with SJVUAPCD permit <br /> ' On January 23, 1996, the vapor extraction rate was 47 standard cubic feet per minute (SCFM) <br /> Based on the vapor sample analytical results for this date, the system extraction rate was 3 3 <br /> pounds per day (lb /day) of TPH, as gasoline, and 0 002 lb /day of benzene On February 8, 1996, <br /> the vapor extraction rate was 37 SCFM Based on the vapor sample analytical results for this date, <br /> the system extraction rate was below laboratory detection limits for both TPH, as gasoline and <br /> benzene On March 6, 1996, the vapor extraction rate was 43 SCFM Based on the vapor sample <br /> ' analytical results for this date the system extraction rate was 1 9 lb /day of TPH, as gasoline <br /> Benzene was not detected in the influent to the vapor extraction system on March 6, 1996 Air <br /> analytical results and chain-of-custody forms are contained in Attachment 3 As of March 6, 1996, <br /> ' the vapor extraction system has extracted approximately 2,300 lbs of TPH, as gasoline, and 7 6 <br /> lbs of benzene <br /> ' System operating data are contained in Table 3 Mass extraction rates to date, based on laboratory <br /> analytical results, are contained in Table 4 Example calculations are contained in Attachment 4 <br /> ' <br /> Groundwater Remediation tem <br /> On January 23, 1995, Emcon started a groundwater treatment system at the subject site The <br /> groundwater treatment system is pneumatically operated via compressed air supplied from the <br /> ' R S I unit and extracts groundwater from monitoring wells MW-1, MW-2, MW-3 and MW-4 <br /> Once the groundwater arrives in the remediation compound via I" diameter PVC piping, it is <br /> filtered through two in-line particulate filters and then through two in-line, 400 lb carbon vessels <br /> ' Upon discharging from the carbon vessels, it is reinjected through two reinjection wells, RWA and <br /> RW-2, located to the west of the remediation compound (Figure 2) <br /> ' During this reporting period, water flow through the treatment system has ranged from 1 0 gallon <br /> �1 <br /> M <br />