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10 <br /> ( "%TC <br /> . A S S O C I A T E S I N C . <br /> ■ GHH Engineering Inc.'s Interim Groundwater Treatment System, Jamar Service, 4075 <br /> East Main, Stockton, California, dated October 2003. <br /> ■ ATC's Remediation System Installation Report for Jamar Property, 4075 East Main <br /> Street, Stockton, California dated 27 May 2003. <br /> ' KVA's C-Sparge System- Model 5030 Installation, Operation, and Safety Manual dated <br /> January 2004. <br /> The operation and monitoring of the C-SpargeTM system was conducted in accordance with these <br /> documents except where specifically noted herein. Remediation system field data is contained in <br /> Attachment 1. <br /> 4.1 C-SpargeTM Chemical Process Description <br /> MTBE and BTEX are the analytes of concern at the Jamar Property. In the C-SpargeTM process, <br /> air and 03 are injected directly into the saturated zone to extract dissolved BTEX and MTBE <br /> from contaminated groundwater. The system at the Jamar property has specially designed <br /> spargers to create "microbubbles" that have very high surface area-to-volume ratio. As the <br /> "microbubbles" rise within a saturated column of groundwater, they extract or "strip" the VOCs <br /> from the aqueous phase. Upon entering the microbubbles, MTBE and BTEX compounds react <br /> with 03 in the gaseous state or in the aqueous "thin layer" surrounding the bubble to decompose <br /> contaminants. Because of the high solubility of 03, over 10 times that of oxygen (CRC, 1972), <br /> the decomposed 03 leaves behind elevated dissolved oxygen. In general the rate of removal has <br /> been sensitive to 03 concentration, pressure, and iron silicate content although the iron silicate <br /> content is not a major concern at the Jamar property due to initial groundwater chemistry. The <br /> reaction rapidly detoxifies groundwater containing MTBE and BTEX compounds without <br /> producing harmful byproducts. Reduction of concentrations is extremely rapid.for benzene. The <br /> reaction is produced with very low 03 concentrations—molar ratios—compared to volatile <br /> organic compounds (VOC) concentrations in groundwater. <br /> The Henry's Constant which regulates the partitioning of MTBE from aqueous to gaseous state is <br /> about one-tenth that of benzene derivatives. However, according to the manufacturer of the C- <br /> Sparge system the surface-to-volume ratio increase of over 30-fold compensates to promote rapid <br /> in situ stripping of MTBE. 03 contained within the bubble and thin film around the bubble reacts <br /> extremely rapidly to decompose the MTBE into simple products: alcohols, acetate and formate. <br /> The residual oxygen from the reaction encourages bioremediation, which consumes the <br /> breakdown products and converts them to carbon dioxide (CO2) and water(H2O). In both bench- <br /> scale testing and field-testing; 03 microbubbles appeared effective in reducing MTBE - <br /> concentrations to beyond 90% of original levels (Kerfoot, 2000). <br /> C-SpargeTM (microbubble 03) <br /> 03 + 2H+ + 2e-_...> 02 +2142O <br /> SA268231QM reports12044 4QR.doc 5 <br />