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2900 - Site Mitigation Program
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PR0508462
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SITE INFORMATION AND CORRESPONDENCE
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Last modified
1/30/2020 12:22:14 PM
Creation date
1/30/2020 11:02:07 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
SITE INFORMATION AND CORRESPONDENCE
RECORD_ID
PR0508462
PE
2960
FACILITY_ID
FA0008093
FACILITY_NAME
CONTINENTAL GRAIN CO
STREET_NUMBER
9504
Direction
S
STREET_NAME
HARLAN
STREET_TYPE
RD
City
FRENCH CAMP
Zip
95231
CURRENT_STATUS
01
SITE_LOCATION
9504 S HARLAN RD
P_LOCATION
99
P_DISTRICT
001
QC Status
Approved
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EHD - Public
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r <br /> WASTE DISCHARGE REQUIREMENTS ORDER NO.R5-2004-0160 2 <br /> CONTIGROUP COMPANIES,INCORPORATED <br /> FRENCH CAMP GRAIN ELEVATOR <br /> ENHANCED REMEDIATION PILOT STUDY <br /> SAN JOAQUIN COUNTY <br /> PROPOSED REMEDIATION PROJECT <br /> 6. Based on review of other remedial technologies and case studies, the Discharger proposes a <br /> granular zero valent iron(GZVI) injection pilot study to reduce carbon tetrachloride and <br /> chloroform concentrations. This technology is well suited for slow moving groundwater <br /> plumes, such as is observed at the Site. The pilot study will evaluate the efficacy of the amount <br /> and spacing of the GZVI injections. The effectiveness of the pilot study will be determined by <br /> measuring the concentrations of carbon tetrachloride,chloroform, and breakdown products in <br /> perimeter monitoring wells. Groundwater monitoring of amendments,breakdown products, <br /> and byproducts will continue until concentrations return to baseline levels, which will conclude <br /> the pilot study. <br /> 7. GZVI is a strong reducing agent. Electrons released during GZVI oxidation reduce the <br /> chlorinated compounds whereby the chlorine atoms are replaced by hydrogen atoms. During <br /> the reductive dechlorination process, the carbon tetrachloride and chloroform act as electron <br /> acceptors. The hydrogen ion,which will affect pH, and chlorine are produced from the <br /> reductive dechlorination process. Case studies show that 70 percent of the carbon tetrachloride <br /> is expected to degrade to non-chlorinated end products (such as carbon dioxide) and 30 percent <br /> is expected to degrade to chloroform. The GZVI will further promote degradation of <br /> chloroform with about 60 percent expected to degrade to methylene chloride and about 40 <br /> percent expected to degrade to non-chlorinated end-products. The biological half-life of <br /> methylene chloride is about 10 days, so a buildup is not expected. The ultimate end products <br /> are carbon dioxide and chloride. <br /> 8. The Discharger will drill three borings, as shown on Attachment B,which is attached hereto <br /> and made part of this Order by reference,to about 85 feet bgs. The locations of the borings <br /> were determined based on groundwater flow direction and area with the highest concentrations <br /> of pollutants in the B water bearing zone. The pilot study is focusing on the B water bearing <br /> zone because the horizontal permeability is much greater than the vertical permeability so there <br /> should not be an influence on the C water bearing zone during the pilot study. Depths of <br /> injection will be about 77.5 feet bgs, 72.5 feet bgs, 67.5 feet bgs, and 62.5 feet bgs to create <br /> four iron fractures per boring. About 4 cubic meters of GZVI slurry will be injected into each <br /> fracture for a total of about 16 cubic meters per boring. The GZVI slurry consists of guar gum, <br /> which makes the slurry viscous and allows the GZVI to be suspended and pumped into the <br /> boring, cross-linker to make the slurry more viscous, and an enzyme breaker to reduce viscosity <br /> once the fracture is emplaced in the subsurface. Guar gum is a carbohydrate made up of <br /> carbon,hydrogen, and oxygen. The cross-linker,BX-1L, is made up of boric acid sodium salt <br /> and ethylene glycol. The enzyme breaker, LEB-H, is made up of sodium chloride. The <br /> mixture of slurry is 400 kilograms of iron, eight kilograms of guar gum, three quarters to two <br /> liters of cross-linker, and 0.02 liters of enzyme breaker per cubic meter of slurry. The amount <br /> injected may be less, but not exceed 4 cubic meters per fracture because the mass of GZVI <br /> injected is controlled by the amount that can be hydraulically fractured into the subsurface. <br />
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