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Manteca Bean Facility, 229 Moffat Boulevard, Manteca, California April 2, 1993 <br /> Golden Grain Company Page 3 <br /> in Table 3 During this quarter of system operation, analyses of discharge water indicated that the TPH- <br /> as-gasoline, BTEX, total and organic lead, and ethylene dibromide concentrations have been below <br /> permit limitations The air stripper was dismantled and cleaned on February 3 and March 4 during this <br /> quarter for normal maintenance in anter to keep the unit at peak operating efficiency, there was no <br /> discharge of system water during these maintenance events (See page 4 Treatment System Summary) <br /> During system operations for this quarter, 0 58 pounds of TPH-as-gasoline have been removed from <br /> groundwater extracted from beneath the sae <br /> The vapor extraction system was monitored each week during this reporting period The influent and <br /> effluent vapor concentrations were measured for TPH-as-gasoline using a flame ionization detector (FID) <br /> Values measured during site visits this quarter are shown in Table 4 The average destruction efficiency <br /> of 98 7 percent was calculated using weekly FID readings of the catalytic oxidizer effluent vapor stream <br /> for the operational period from December 29, 1992 through March 4, 1993 All effluent readings <br /> collected were below the 100 ppmv TPH-as-gasoline lima specified by the Unified Air Pollution Control <br /> District perms to operate <br /> Using the flowrates and TPH-G concentrations measured each week, the amount of TPH-as-gasoline <br /> removed from soils at the site can be estimated Based on the TPH-G concentrations and system flow <br /> rates obtained during field visas, approximately 843 pounds of TPH-as-gasoline were removed from the <br /> soil by the vapor extraction system during this quarter The cumulative amount of hydrocarbons <br /> removed by the VES since start-up is estimated 1613 pounds <br /> VAPOR EXTRACTION MONITORING <br /> On February 18 and 23, 1993, vapor extraction monitoring was conducted to evaluate the subsurface <br /> effects of the vapor extraction system (VES) and quantify the static vapor levels of TPH-G in the sods <br /> located within the VES treatment area On February 18, air samples were taken from the VES influent, <br /> the effluent of the lead scrubber, and the effluent of the catalytic scavenger unit for laboratory analysis <br /> The samples were analyzed for BTEX, TPH-G, total lead, and organic lead Results of laboratory <br /> analyses are shown on Table 5 Laboratory results indicate that effluent concentrations for toluene and f <br /> xylene are 0 6 and 1 part per billion respectively, while all other compounds or analytes that were V <br /> analyzed were non-detectable These effluent analysis results are wdhin the 100 ppmv TPH-as-gasoline <br /> limits as set by the Unified Air Pollution Control District permit to operate <br /> Following system sampling, the applied vacuum was measured at the two vapor extraction wells, and <br /> the induced vacuum was measured at the monitoring wells within the VES treatment area Readings <br /> were taken using a magnahelic gauge, in inches of water vacuum Readings were gathered to <br /> determine system efficiency and the radius of influence from the vapor extraction wells The values <br /> obtained are shown on Table 5B Results indicate a vacuum affect on the surrounding area, however, <br /> the applied vacuum at the extraction wells did not correspond with the system readings at the blower It <br /> GROUNDWATER <br /> QTR1 MCs TECHNOLOGY, INC <br />