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INTRODUCTION <br /> The following report describes a pilot test of the C-SpargeTm process for remediation of <br /> dissolved chlorinated solvents from ground%%ater The test was conducted b} Mateboer <br /> Milieutechniek B V for the Provincial Government of Utrecht at Rembrandt Street in Bilthoven, <br /> The Netherlands,from March 27, 1997 through April 4, 1997 The test involved installation of a <br /> C-Spargel well (TW), some additional monitoring wells (four 2-inch ID),the use of previously <br /> existing miniwells, and a fire well across the site <br /> THE C-SPARGETm PROCESS where <br /> The C-SpargeTm process consists of a combination of in-situ air stripping, <br /> dissolved chlorinated solvents(like PCE,TCE,DCE or vinyl chlonde) are extracted from <br /> tee:..—�� 4L _ in <br /> 1�'►^ - — - - -' <br /> trichloroethene(TCE),-then reacts with encapsulated ozone in gas/gas reaction described by the <br /> Criegee mechanism as a pnmary ozonide The ozonide is very unstable,decomposing to form a <br /> carbo 1 oxide which reacts with water(hydrol as it exits the bubble to eld reaction end _ <br /> products Cl-,H2O, and CO2(Masten, 1996) <br /> This is a very clean reaction sequence since the TCE is concentrated in the fine bubbles <br /> to react with ozone on a mole-to-mole basis The concentration of ozone in the bubbles is <br /> matched to the expected TCE concentration The process focuses ozone reaction selectively to <br /> air-stnppable compounds which invade the bubbles. As a result, Othe encapsulatedaditional ozone <br /> concentration is maintained at a low multiplier of the stnppab <br /> is available for side reactions with other dissolved organic compounds which have low Henry's <br /> numbers Primary reactions do not create any intermediate products because the reactions <br /> proceed so rapidly and bubble rise times are quite long. As of yet,the only identified end <br /> products have been inorganic(chloride, carbon dioxide,bicarbonate,nitrate,sulfate, and <br /> dissolved oxygen) Other organics may be produced,but at levels below normal detection- <br /> SM DESCRIPTION lume of <br /> The field test site is positioned in a small park area midway on a long p <br /> predominantly trichloroethene(TCE)onginaung at a commercial building and traveling over <br /> 244 m(800 ft) across a predominantly commerceal� residentialbdeposits iGroundwaThe ter�xists at a <br /> on lies <br /> in a thick fine sand deposit which contains gra <br /> depth of 2.5 m(8 2 ft)below grade. About one-half of the area of groundwater overlying the <br /> TCE plume is contaminated with dissolved hydrocarbon (BTEX)from a nearby commercial fuel <br /> spill. <br /> Soil borings taken by Tauw Engineering in the vicinity of the plumeshowed over mlow <br /> (19.7 <br /> surface loam extending to 3 m ells to(6 6 ft)deep Fine sand occurred in many A thick cla <br /> ft) deep Often gravel layers were intercepted at 4 m(13 ft)to 6 m(19 7 ft) deep Y <br /> layer,which probably serves as a bottom confining layer,was found at 38 m to 40 m(124 7 ft to <br /> 131 2 ft)deep. A hydraulic conductivity(K)of 7 5 x 10-2 cm/sec has been estimated for the <br /> sand deposits. <br /> Previous groundwater sarnpling had identified a narrow, long HVOC plume on two <br /> transects (A-A' and BB") extending from a source near A(wells 120 and 121) at a commercial <br /> facility to under Rembrandt Street, and ending under another commercial comptex The Bowe f <br /> 140)near Rembrandt Street(Figure 1) The distance was about 225 m(738 ft)Ict P <br /> 2 <br />