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' 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, specifically <br /> benzene, to groundwater standards without producing harmful byproducts. The reaction is <br /> ' produced with very low 03 concentrations--molar ratios—compared to volatile organic <br /> 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 <br /> reacts extremely rapidly to decompose the MTBE into simple products: alcohols, acetate and <br /> formate. The residual oxygen from the reaction encourages bioremediation, which consumes the <br /> ' breakdown products and converts them to carbon dioxide (CO2) and water (1120). 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>OZ+2H2O <br /> ' 4.2 General C-SpargeTM Remediation System Description <br /> 4.2.1 C-SpargeTM System Equipment Description <br /> The C-SpargeTM system became operational on June 17, 2004. Figure 11 shows the remediation <br /> system compound location as well as the injection and groundwater monitoring well network for <br /> the Jamar property. <br /> ' The C-SpargeTM remediation system at the Jamar property consists of a KVA C-SpargeTM System <br /> Series 5030 model. This includes a small profile Master Unit (43"w x 29.5% x 12"d, 120 lbs) <br /> which has a capacity of serving up to twelve (12) Spargepoints® sequentially but is currently <br /> ' serving 10 Spargepoints® (Attachment 4). Figure 12 is a general process and instrumentation <br /> (P&ID) diagram for the Jamar property remediation system. <br /> Two sparge points are installed in each of five injection wells (IWi through IW5) at the Jamar <br /> property. Each of the eight-sparge points in IW1 through IW4 is on separate injection intervals. <br /> The two-sparge points in IW5 are combined together. 03 is injected sequentially in each of the 8 <br /> separate sparge points at eight-minute intervals and for 16 minutes at the combined sparge point <br /> in IW5. This is 80 minutes for all sparge points combined with one shut-off period for 10 <br /> minutes after all intervals are completed or ninety minutes for a complete cycle including the <br /> ' S:1258231QM reports12004 3QR.doc 5 ATC Associates inc. <br /> 1 <br />