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r <br /> LFR Inc. <br /> • Nitrogen as nitrate <br /> • Sulfate concentration <br /> • Estimates of the competing hydrogen to form ferric iron, manganese (Mn"), <br /> and methane <br /> Processes other than reductive dechlorination compete for the hydrogen created by <br /> substrate injection. Nitrate reduction, ferric iron reduction, sulfate reduction, and the <br /> creation of methane all use hydrogen. Analytical data from the Site suggest that sulfate <br /> reduction may represent the largest competitive demand for hydrogen due to the <br /> relatively high (78 mg/1) sulfate concentration. The model predicts that sulfate reduction <br /> will take up an order of magnitude more hydrogen than any other competing process. <br /> When these demands of competing processes are accounted for, the required substrate <br /> load is increased to accommodate them and still provide sufficient hydrogen for the <br /> anaerobic dechlorination of targeted Hazardous Substances. LFR used a Hydrogen <br /> Demand/Groundwater Flux model spreadsheet provided by EOS Remediation, Inc., to <br /> perform this evaluation. The spreadsheet is presented as Appendix D in this report. Site <br /> data were put into the model and yielded an emulsified edible oil substrate requirement <br /> of 138 drums (7,590 gallons). <br /> Proposed Substrate Loading <br /> The two methods yielded similar recommended substrate loading, 8,580 and 7,690 <br /> gallons for the Empirical TOC approach and the Hydrogen Demand/Groundwater Flux <br /> model, respectively. To introduce a factor of safety for unforeseen competing processes <br /> and/or dispersion or transport of substrate away from the target area, and to minimize <br /> the likelihood that re-injection will be necessary, LFR proposes to roughly double the <br /> amount of substrate injected to approximately 15,000 gallons. <br /> 4.2.2 ERD Well Installation <br /> The proposed ERD injection wells will be installed using a hollow-stem auger drill rig. <br /> Eleven injection wells will be screened in the upper A zone and 11 injection wells will <br /> be screened in the lower A zone. Locations of the wells are shown on Figure 5. Based <br /> on historical site lithology data presented in Section 2.2 and shown on Figure 7, it is <br /> anticipated that the upper A-zone wells will be screened at approximately 45 to 60 feet <br /> bgs and the lower A-zone wells will be screened at approximately 65 to 80 feet bgs. An <br /> LFR geologist will record a description of the lithology as drilling progresses, based on <br /> drill cuttings, and the boring will be continuously cored and logged from approximately <br /> 40 feet bgs to 80 feet bgs for the deeper lower A-zone wells. Upper A-zone wells will <br /> not be continuously cored; these wells will be installed based on the lithology <br /> encountered in the adjacent lower A-zone wells. The ultimate depth of the injection <br /> well and screen interval will be determined in the field, based on lithologic and head- <br /> Page 22 wp-PhV IRA-Sep07-F1m1-06750.dx:IR <br />