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2900 - Site Mitigation Program
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PR0508462
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Entry Properties
Last modified
1/30/2020 3:05:48 PM
Creation date
1/30/2020 11:03:42 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
WORK PLANS
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
Scanner
SJGOV\sballwahn
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EHD - Public
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' 2.1 Stoichiometry for Target Compounds and Intermediate Products <br /> The principal constituents of concern at the French Camp Grain Elevator site are carbon <br /> ' tetrachloride (CC14) and chloroform (CHC13). Chloroform is a daughter product formed from <br /> the partial molecular breakdown of carbon tetrachloride. Chloroform is further broken down <br /> anaerobically to methylene chloride (CH2C12), which ā in tum ā releases the final breakdown <br /> ' products, carbon dioxide, water and chloride iron. The presence of chloroform suggests that the <br /> groundwater contamination is degrading naturally, although the rate of natural attenuation has <br /> not been quantified and appears to be limited. <br /> The following reactions generally represent a dehalogenation process in the presence of reduced <br /> iron metal and water(Gilham and O'Hannesin, 1994): <br /> Considering only the presence of water, zero-valent iron and a chlorinated organic <br /> compound X-C 1, the following equations est <br /> ed: <br /> 2Fe° He 2++4e <br /> 3H2O 3H++ 30H- <br /> 211++2e H2 <br /> X-Cl +H++2eā> X-H+ Cl- <br /> 1 2Fe°+3H2O +X-C 1 --> 2Fe2++30H-+H2+X-H+Cl- <br /> . . . . (1) <br /> In this case, for each mole of Cl- released to the solution p ase, 2 moles of Fee+ <br /> should also appear in solution. On the other hand, if the dissociation of water is <br /> ' not included, the overall reaction can be written: <br /> Fe°+X-C 1 +H2O ā* Fe2++OH"+X-H+Cl" (2) <br /> tIn this case, only one mole of Fe 2+ would be released to the solution phase for <br /> each mole of Ct. Thus, the complete dechlorination of 1.0 mg/1 of CT would <br /> I result in a chloride concentration of 0.92 mg/l, and would contribute 2.8 or 1.4 <br /> mg/l of iron,based on equation(1) or(2),respectively. <br /> Depending on pH and Eh conditions, iron may occur as ferrous hydroxide Fe(OH)2 or as FeCO3. <br /> Chloride concentrations and iron concentrations may increase as a result of the degradation <br /> process. <br /> These constituents (chloride and iron) are included in the proposed monitoring of the pilot scale <br /> study. <br /> RACONTGRAMCCACargiIDFrench Camp\Waste Discharge Application\supp info 6-29-04.doc <br /> 5 <br />
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