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Ms Lori Duncan Project No 880-039 IA <br /> January 30, 2004 <br /> Page 3 <br /> indicate that TPHg were present in wells MW-4R-S, MW4R-D and VW-2, at concentrations <br /> ranging from 81 to 52,000 micrograms per liter (pg/L) Benzene was reported in wells MW-3R, <br /> MW-4R-S, MW-4R-D, VW-2 and VW-3 at concentrations ranging from 7 5 to 7,000 ug(L <br /> MTBE was not detected by USEPA Method 8260B in any of the seven wells sampled Copies of <br /> the chain-of-custody records and laboratory analytical report are presented in Appendix C <br /> The groundwater gradient was approximately 0 008 with groundwater flow to the north-east <br /> (Figure 2) Groundwater analytical data are summarized on Table 1 TPHg and benzene <br /> } concentrations are shown on Figure 3 <br /> E <br /> REMEDIATION SYSTEM STATUS: FOURTH QUARTER 2003 <br /> The remediation system consists of four shallow zone and three deep zone soil vapor extraction <br /> (SVE) wells, from which soil vapors are extracted using a Stealth Bobcat Catalytic Oxidizer <br /> rated at 100 cubic feet per minute (cfm) Startup of the remediation system occurred on <br /> February 3, 2000, under the supervision of regulatory personnel Subsequently, Shaw staff <br /> perform weekly system O&M, collect influent and effluent air samples monthly in accordance <br /> with air board permit requirements, and report quarterly to the air board <br /> Sampling Results <br /> On October 13, November 3, and December 8, 2003, vapor samples were collected from <br /> treatment system's influent and effluent Samples were submitted to Sierra Analytical (FLAP <br /> j #2320) for analysis of TPHg and BTEX using USEPA Methods 8015 and 8020/8021 TPHg and <br /> BTEX concentrations were below the detectable limits during each sampling event Laboratory <br /> analytical reports and chain-of-custody documentation are presented in Appendix D <br /> System Performance Status <br /> In the 91 days between September 30, 2003, and December 29, 2003, the treatment system ran <br /> approximately 80 days (88 percent operational), removing approximately 5 pounds of TPHg, as <br /> shown on Table 2 The system's TPHg emissions were maintained below 0 06 pounds per day, <br /> below the allowable TPHg emission rate of 6 1 pounds per day TPHg and benzene destruction <br /> efficiencies were maintained at approximately 97 percent The burn chamber temperature <br /> ranged from 750°F to 778°F, well above the minimum required burn temperature of 600°F <br /> N Isac)P120041PgW80W800391A 4aa doc Shaw Environmental,Inc <br />