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Kerfoot Technologies Technical Papers Page 1 of 3 <br /> i+ HtMEp�lE MbAB015'" ► C3t31; � Pif7LCY� �ti "' 4h1RL3�UCSxrTtCT��1 a� <br /> l �iSr�' ,.. ...tee <br /> Technical Papers <br /> C-SpargeTM Ozone Microspargeng for Raped Removal of MTBE and Benzene <br /> By William B Kerfoot, Ph D , LSP and Angus McGrath, Pty D <br /> A system called C-SpargingTM which uses ozone/air injected periodically in conjunction with a pulsing atAs xi orad, <br /> pump has been demonstrated to reduce MTBE from over 1000 ppb to less than 100 ppb in less than 40 �trr <br /> days The rate of decay was found to be a ten-fold reduction in monitoring wells located 3 to 7 meters <br /> from the injection point Monitoring was performed weekly during and after treatment alas <br /> 74= suza�ao>0 714L <br /> e=ve�c 4— Amew=1 <br /> What is C-SpargengTM "MFLIYE �. <br /> The KVA process of C-SpargingTM, in situ air stripping with micro-encapsulated ozone, combines three- <br /> unit operations offering a one-two-three punch to knockout MTBE Firstly, fine bubbles with a high ` <br /> xta�rt4si� <br /> surface-to-volume ratio are injected into the saturated zone to extract dissolved MT6E from ' <br /> contaminated groundwater Secondly, ozone contained within the bubble and thin film around the sqpzw i <br /> bubble reacts extremely rapidly to decompose the MTBE into simple products, alcohols, acetate and <br /> formate Thirdly, the residual oxygen from the reaction encourages bioremediation which consumes the <br /> breakdown products and converts them to carbon dioxide (CO2) and water (H2O) PUMP <br /> ne Microsparging is a Patented Technology for In Situ Treatment of Volatile Organic <br /> pounds (VOCs) in Groundwater <br /> The reaction detoxifies groundwater containing MTBE and BTEX compounds, specifically benzene, e i <br /> rapidly to groundwater standards without producing harmful byproducts The reaction is produced with <br /> very low ozone concentrations-molar ratios-compared to VOC concentrations in groundwater The SCREEN I ' <br /> technology combines the unit operations of air stripping and oxidative decomposition in a single ;i arxist <br /> i i <br /> process which can be catalytically accelerated In the C-SpargeTM process, air and ozone are injected I stIA> rTe'MYkLvs <br /> directly into groundwater through specially-designed spargers to create "microbubbles" that have very ..-.. C9r ,w <br /> high surface area-to-volume ratio The Henry's Constant which regulates the partitioning of MTBE from <br /> aqueous to gaseous state is about one-tenth that of benzene derivatives However, the surface-to- <br /> volume ratio increase of over 30-fold compensates to promote rapid in situ stripping of MTBE As the <br /> "microbubbles" rise within a saturated column of groundwater, they extract or "strip" the VOCs from °h <br /> aqueous to gas partitioning Upon entering the microbubbles, MTBE and BTEX compounds react with <br /> ozone in the gaseous state or in the aqueous "thin layer" surrounding the bubble to decompose MTBE <br /> is rapidly degraded with time The rate of decay is similar to that previously reported by Karpel vel Figure i Master Control Uni <br /> Leitner, et al (1994) In both bench-scale testing and field testing, ozone microbubbles appeared <br /> effective in reducing MTBE concentrations to beyond 90% of original levels (Kerfoot, 2000) The rate of removal has been sensitive to <br /> ozone concentration, pressure, and iron silicate content <br /> Site Specific System Set-up <br /> A single C-Spargero master unit with 6 Spargepointsg was installed upgradient of plume region The unit can be installed with a dual- <br /> screened recirculation spargewell which has a lower Spargepoint@ or with isolated SpargepointsO The depth to groundwater was 2 to <br /> meters The general construction of a C-Sparge6 consists of a 100 mm casing leading to a 1 S meter screen with 0 5 meter above the <br /> water table, a blank casing which was bentonite-sealed in the annular space to prevent short-circuiting, and a lower 1 5 meter screen <br /> (10 slot) Alongside this was a 1 5 cm diameter tubing leading from the wellhead region to a 50 mm macroporous Spargepointa 46 cm <br /> long with a compression fitting situated below the lower double screen <br /> The predominant soil type was gravelly sands Water table level occurred at 2 to 3 meters The predominant contaminated region <br /> 0ded vertically from 1 to 3 meters deep The Spargepoints® were installed at a depth of 10 meters <br /> http //www kva-equipment com/product php?14,2,28806,ker28806,,,Doc,page html 11/10/2004 <br />