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FIELD DOCUMENTS_2000-2003
Environmental Health - Public
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EHD Program Facility Records by Street Name
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2900 - Site Mitigation Program
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PR0009002
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FIELD DOCUMENTS_2000-2003
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Last modified
6/17/2020 3:11:07 PM
Creation date
6/17/2020 1:43:21 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
2000-2003
RECORD_ID
PR0009002
PE
2960
FACILITY_ID
FA0004040
FACILITY_NAME
SPX COOLING TECHNOLOGIES INC
STREET_NUMBER
200
Direction
N
STREET_NAME
WAGNER
STREET_TYPE
AVE
City
STOCKTON
Zip
95215
APN
14331007
CURRENT_STATUS
02
SITE_LOCATION
200 N WAGNER AVE
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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EHD - Public
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WASTE DISCHARGE REQUOMENTS • 2 <br /> MARLEY COOLING TOWER COMPANY <br /> SAN JOAQUIN COUNTY <br /> TENTATIVE <br /> back into the facility treatment system. The treated water flow from the injection system beneath <br /> the retort pit is primarily vertical. <br /> 6. Approximately 5%of the treated water (effluent from the treatment system), defined as flushing <br /> water, is reinjected into shallow soils in the area of a closed retort pit at 37 degrees, 58 minutes, <br /> 11 seconds latitude and 121 degrees, 14 minutes, 00 seconds longitude, as shown on Attachment <br /> B, a part of this Order. The process flushes the wood-treating chemicals from the soil into the <br /> chromium and copper plume being captured by the above mentioned groundwater extraction <br /> system. <br /> 7. The groundwater treatment system consists of a treatment plant with an electrochemical unit <br /> operating in parallel to an ion exchange unit that removes waste constituents from the extracted <br /> water. <br /> 8. The ion exchange unit consists of two anion exchange vessels and a cation exchange vessel. In <br /> the anion exchange vessels,hexavalent chromium in the water is adsorbed onto the ion exchange <br /> resins. ht the cation exchange vessel, trivalent chromium and copper are adsorbed. The exchange <br /> process continues until the resin's exchange sites are filled and exchange capacity is exhausted. <br /> The adsorbed chromium and copper are stripped from the ion exchange resins and the resins are <br /> conditioned for additional water treatment in a process called regeneration. During regeneration, <br /> which occurs approximately every 2.5 days, 15,000 gallons of solution containing the stripped <br /> chemicals is removed from the ion exchange unit. <br /> 9. The electrochemical unit of the treatment plant is supported by processes consisting of <br /> electrochemical reduction(Andco) and precipitation which uses iron as the reducing agent for the <br /> hexavalent chromium followed by iron co-precipitation using pH adjustments. The addition of <br /> polymers and further pH adjustments are used to optimize settling. The effluent is then filtered <br /> prior to discharge. The solids from the clarifier are pumped and accumulated in a filter press. <br /> The filter press filtrate and mixed media filter backwash are returned to the electrochemical unit <br /> side of the treatment plant for further treatment. <br /> 10. The site is divided into two areas, the North Yard and the South Yard. All past wood treatment <br /> activities were conducted on the North Yard. Rain falling on the North Yard becomes polluted <br /> after contact with treated cooling tower components. This polluted rainwater is collected in a <br /> storm drain system and is passed through the treatment plant in the northeast portion of the site. <br /> Due to storage of treated wood products on the MCTC South Yard, some wood treating chemicals <br /> were once detected in the storm water runoff from the South Yard. The South Yard surface has <br /> been cleaned. The residual contamination in pipes and ditches has been removed as part of the <br /> remedial actions undertaken by the Discharger. MCTC is in the process of obtaining a general <br /> discharge permit for the South Yard. <br /> 11. The treatment facility is designed to treat flows to 0.94 mgd. Groundwater is extracted from a <br /> minimum of 17 extraction wells on and off-site. The groundwater extraction system can operate <br /> in a cyclical fashion with each of the two cycles lasting 56 hours or on a continuous basis with all <br /> extraction wells pumping at rates varying from 10-90 gallons per minute depending on effective <br /> 08/22/02 2:02 PM Marley Cooling <br />
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