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Stantec <br /> April 13, 2009 <br /> Page 10 of 13 <br /> Reference: Response to RWQCB March 11, 2009 Letter <br /> r fb <br /> Phydrostatic = 1 62.4 3) <br /> h(ft)l t <br /> Ib2 <br /> Phydrostatic= 62.4 3 110 ftt)+144 to =47.6 psi <br /> fi jt2 <br /> Pminimum Inlectlon Phydrosbtic 47.6 psi <br /> Because of the greater pressure than shallow applications and the approximate 2.5 <br /> cubic feet of casing volume that needs to be displaced, slightly lower oxygen volumes <br /> and weights will be delivered to the aquifer. On the other hand the greater pressure will <br /> allow higher concentrations of dissolved oxygen (DO) to be maintained. Overlying, fine- <br /> grained, low-permeability strata should minimize potential diffusion of DO to the surface <br /> as often occurs in unconfined aquifers. <br /> (2) stoichiometrically demonstrate that twice-monthly 13-Ib oxygen injections are sufficient <br /> to oxidize the petroleum hydrocarbon mass present in the target zone. <br /> As outlined in the January 27, 2009 Pilot Study Work Plan, the objective of the proposed <br /> oxygen injection was to facilitate enhanced biodegradation (not oxidation) and mitigate impacts <br /> near in the aquifer near well TS/MW-2D. Stoichiometric relationships between the mass of <br /> oxygen needed to metabolize petroleum hydrocarbons and the mass of hydrocarbons <br /> potentially degraded are available in the literature and typically vary between 3 and 3.5 pounds <br /> of oxygen to 1 pound of hydrocarbons. From the April 10, 1998, ASTM E 1943-98 Standard <br /> Guide for Remediation of Ground Water by Natural Attenuation at Petroleum Release Sites, <br /> Page 22, Appendix Section X5.3.2, A Quantitative Approach to Evaluating Indicators of <br /> Biodegradation; The equation that follows was used to determine that 3.1 mg/L of oxygen is <br /> necessary to completely metabolize 1 mg/L of toluene. <br /> Aerobic Respiration <br /> C6H5CH3 + 902 7CO2+ 4H2O <br /> As shown in Figure X5.1 of the above reference, the equation is balanced using toluene and <br /> would differ slightly for other BTEX constituents, TPH, and fuel oxygenates. The equations <br /> balanced for benzene can be found in Wiedemeier et al, 1995, Technical Protocol for <br /> Implementing Intrinsic Remediation with Long-Term Monitoring for Natural Attenuation of Fuel <br /> Contamination Dissolved in Groundwater. As is well understood, these are potential relations <br /> and depend on many other variables, the spatial distribution of adequate DO concentrations, <br /> the appropriate microbial communities, contaminant demands, and other variables. For <br /> example, biodegradation of MTBE is generally reduced or delayed until the much of the BTEX <br /> constituent mass has been degraded. <br /> I:\STTC-Stockton\Reports\Response to Comments\RWQCB Letter 3-11-09\STTC Response to RWQCB 3-11-09 Letter Final.doc <br />