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1 <br /> Free product has been observed in well MW-3 intermittently since Fourth Quarter 2003 <br /> Approximately one-half inch of free product was observed in well MW-3 at the time of the Fourth <br /> IQuarter 2004 sample event No free product was observed during the First and Second Quarters 2005 <br /> sample event, however, a product sheen was observed on the purge water and the water in the sample <br /> Icontainers during both of these sampling events <br /> 33 Remediation System Operation and Maintenance and Performance Summary <br />' Operation and maintenance (O&M) of the remediation system is performed monthly (or as needed) <br /> Photo ionization detector (PID) readings from the SVE effluent and influent is performed monthly as <br />' required by the San Joaquin Unified Air Pollution Control District (SJUAPCD) As required by <br /> SJUAPCD, a chart recorder provides a continuous chart of the catalytic oxidizer temperature The <br /> chart paper is changed out on a weekly basis A brief description and performance evaluation of the <br />' remedial system for the reporting period is presented below <br />' 3 3 1 SVE System <br /> The SVE system is comprised of a skid-mounted 250-cfm blower and catalytic oxidizer (SCAT-250) <br />' with knockout pot manifolded to ten SVE wells (V-1 through V-10) During the reporting period, the <br /> SVE system was approximately 100% operational <br /> On February 3, 11, 18, and 25, March 4, 14, 21, and 28, and April 4, 11, and 19, the chart paper was <br /> changed out <br /> On March 7, Geocon mobilized to the site to collect the SVE influent and effluent samples for <br /> laboratory analysis and to adjust flows and vacuums on various wells to maximize contaminant <br />' removal The contaminant concentration, flow, and vacuum were monitored in extraction wells V2, <br /> V3, and V6 Based on vacuum readings, flows, and PID readings no adjustments were necessary <br /> On April 6, Geocon mobilized to the site to collect the SVE influent and effluent samples for <br /> laboratory analysis and to adjust flows and vacuums on operating wells to maximize contaminant <br />' removal The contaminant concentration, flow, and vacuum were monitored in extraction wells V2, <br /> V3, and VE-6 Vacuum pressures were adjusted by changing valve openings on VE-2 and VE-3 <br /> IThe approximate vacuum for the SVE system during the reporting period was 97 5 inches of water, <br /> and the approximate flow rate was 201 cfm The average SVE system influent TPHg concentration <br /> 1 during the reporting period was 90 5 parts per million volume (ppmv) <br />' Project No 58643-06-01 -6- <br /> May 5 2005 <br /> 1 <br />