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FIELD DOCUMENTS AND WORK PLANS 2000-2003
Environmental Health - Public
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FIELD DOCUMENTS AND WORK PLANS 2000-2003
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Last modified
2/22/2019 6:24:05 PM
Creation date
2/22/2019 2:58:44 PM
Metadata
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EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
AND WORK PLANS 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
01
SITE_LOCATION
200 N WAGNER AVE
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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WASTE DISCHARGE REQUOMENTS • 4 <br /> MARLEY COOLING TOWER COMPANY <br /> SAN JOAQUIN COUNTY <br /> TENTATIVE <br /> chromium in the aquifer and vadose zone to precipitate it out of solution. Sodium dithionite is <br /> proposed as research indicates it has the ability to alter the oxidation/reduction state of the <br /> groundwater,thereby immobilizing chromium. Ethanol is proposed as an organic carbon source to <br /> stimulate microbial growth and produce reducing conditions to precipitate chromium out of <br /> solution. Ethanol is highly soluble in water, and is easily obtained. Phase 1 is proposed to address <br /> the high concentrations of hexavalent chromium in the shallow groundwater adjacent to and <br /> downgradient of the former retort pit(range of 5,000 to 200,000 micrograms/liter(parts per <br /> billion)). Once these concentrations have been reduced,the residual chromium in the vadose zone <br /> is proposed to be addressed in Phase 2. The Discharger has provided information to indicate that <br /> in situ remediation research has shown that introduction of an organic carbon source into <br /> groundwater stimulated microbial activity that in tum used up dissolved oxygen and created <br /> strongly reducing conditions. Under these strongly reducing conditions hexavalent chromium was <br /> reduced to trivalent chromium and precipitated on the soil matrix. Furthermore,research also <br /> indicates that this reaction was not reversible under natural conditions(i.e. the absence of a strong <br /> oxidant)in groundwater. In effect,the precipitated trivalent chromium would not be re-oxidized to <br /> hexavalent chromium and re-mobilized under naturally occurring conditions. <br /> 15. During Phase 1,the Discharger proposes to inject up to 9 pounds of reagent grade sodium <br /> dithionite or 400 litres(about 105 gallons)of food grade ethanol in monitoring well MW-206 over <br /> a maximum of 40 days or until oxidation reduction potential(ORP)readings of-50 mV or less <br /> have been achieved for 30 days and chromium concentrations have declined. Field monitoring and <br /> groundwater sampling will be conducted to evaluate effectiveness of meeting the desired ORP. <br /> After results have been evaluated and it has been determined that chromium concentrations have <br /> declined and are relatively stable, slow release oxygen compounds(ORC)manufactured by <br /> Regenesis Bioremediation Products, San Clemente, California will be introduced into well MW- <br /> 206 to verify that trivalent chromium is not oxidized to hexavalent chromium and thereby increase <br /> chromium concentrations in groundwater. If the results indicate that the reducing conditions <br /> cannot be created in the shallow groundwater and the chromium concentrations are not declining, <br /> then this pilot test will be terminated. If the results indicate that chromium concentrations decline <br /> in response to the sodium dithionite or ethanol dosing,a larger scale pilot study in the shallow <br /> groundwater will be implemented. The lager study will include the introduction of ethanol into <br /> wells MW-6,MW-101,MW-105,MW-106,MW-206,MT-1,MT-2,MT-4,MT-8,P-228,P-229, <br /> and P-231. The amount and frequency of dosing will be based on the results of the initial phase of <br /> the pilot test using well MW-206. Sodium dithionite proposed for this pilot test is a powder 89 to <br /> 91 percent sodium dithionite(sodium hydrosulfite). The remainder is an alkali stabilizer. The <br /> product is essentially free of heavy metals. Ethanol is a liquid,highly soluble in water,and is <br /> easily obtained. <br /> 16. During Phase 2, the Discharger proposes to inject up to 31 pounds of reagent grade sodium <br /> dithionite or 43 litres (about 12 gallons) of food grade ethanol will be introduced into the <br /> flushing system injection wells (IW-1, IW-2, IW-3, IW-4, and IW-5)using a metering pump. <br /> If sodium dithionite is used, it will be injected at a rate to produce a concentration of <br /> approximately 50 mg/1 to achieve the desired ORP of-50 mV or less. If ethanol is used, it <br /> will be injected for 15 minutes every hour at a rate to produce a concentration ranging from <br /> 100 to 1000 mg/1 in the injected flow to achieve the desired ORP of-50 mV or less. If the <br /> evaluation of the results indicates that chromium concentrations have decreased but still <br /> 08/22/02 2:02 PM Marley Cooling <br />
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