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., NVES N ;390 EASTvEAArMR MEET <br /> GE-C.-ET'-LT rE \EEERS j�700DL.4ND, C-4,95776-16003 <br /> CA-LIF. CONTRACTOR 4!513857 (530) 668-5300 <br /> . IREGISTF-RED GEOLOGIS'T'S F-4X (530)662-0273 <br /> �r e,e�cal.�et <br /> May 23, 2005 <br /> Mr. Richard Stiffler <br /> Environmental Control Section, Department of Municipal Utilities <br /> City of Stockton <br /> 2500 Navy Drive <br /> Stockton, CA 95206-1191 <br /> (209) 937-8740 Fax (209) 937-8708 <br /> RE: Request for modification to treatment system for Discharge of treated groundwater <br /> to City of Stockton at Sanchez Property, 1876 Country Club BIvd, Stockton, California. <br /> Dear Mr. Stiffler: <br /> As per our phone conversation on Friday, May 20, 2005, the following discusses the <br /> changes to the treatment system to alleviate TBA (tert Butyl Alcohol) from being <br /> discharged to the sanitary sewer. <br /> Revision to treatment system. A revised schematic <br /> reatment system is shown <br /> on Figures I and 2. The treatment system is designed toe remove contaminants of <br /> concern (COC) from groundwater extracted from excavation well MWIO. Maximum <br /> pump rates from MW10 are not to exceed 10 gallons per minute. We wish to modify <br /> the treatment system by adding a fifth water carbon unit in series to the pre-existing <br /> four and placing an aeration tank between carbon units 42 and #3. The existing <br /> treatment system was able to remove all of the COCs with the exception of tert <br /> Butanol (TBA). The aeration tank will allow for the further oxidation of TBA <br /> followed by three water carbon units, prior to discharge. The majority of petroleum <br /> hydrocarbons are removed in the initial water carbon unit with further removal <br /> occurring in the second water carbon unit. Placing the aeration tank after the second <br /> carbon unit will aIIow the oxidation to be concentrated on MtBE and TBA. <br /> Summary of operation and maintenance (O&M) practices for the treatment system. <br /> Operation: Groundwater is extracted from well MWIO by electrical submersible pump_ <br /> This pump is capable of pumping 12 gallons per minute. A valve at the influent of the 41 <br /> water carbo in used to adjust the flow rate to the permit condition of 10 gpm or less. <br /> The pumped water travels to the two in series water carbon units 41 and #2, prior to be <br /> sprayed into the newly added aeration tank (poly tank). A centrifugal pump (capable of <br /> Pumping the treated water at 20 gpm) attached to the bottom bung of the aeration tank, <br /> Pumps the water from the tank to a manifold that will allow IO gallons per minute <br /> 1 WATER TREATMENT modification May 2005 <br />