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KINETIC y V V <br /> the test spargewell (TW)to be able to m%e a 3-dimensional picture of the test results The larger <br /> diameter(2-inch ID) wells allowed ground%+ater flow as well as pressure change to be monitored <br /> during treatment A Nanety of physical and chemical measurements were performed during the <br /> test(Table 1) <br /> Table I. Ground Aater Monitoring during Pilot Test. <br /> Temperature,turbidity, pH,Fe;redox potential, dissolved oxygen (DO), <br /> static ttiater elevation, HVOCs including PCE,TCE,DCE, VC,TCA, <br /> groundwater flow, DCA; VOCs including benzene,toluene, <br /> • - _ -head pressure change ethylbenzerie,xylenes,ozone concentration <br /> C-SPARGE WELL WSTALLATION e 3 was installed <br /> The C-Spargenm double-screen well with lower SpargepomtR (Figur ) <br /> N%ith a recirculating water system and casing. A small flow (2 galtmin) was obtained from a <br /> shallow fire well for makeup water. Tlie lower Spargepoint R was set at a depth of 2 6 in (8.5 ft) <br /> A one-half inch tubing extended to the surface from <br /> a compression fitting on the Spargepoint R A 4-inch •'"' o <br /> ID triple-screened well extended from 23 m(75.5 ft) .ouffse,o a M` <br /> to .3 m (1 ft)above grade. The 2 m(6.6 R)long .9-26 <br /> screens were placed with bottom edges at 23 in (75 5 ft), <br /> 13 in (42.7 ft),and 2 5 m(8.2 ft). The middle casing <br /> between the two lower screens received 1 in(3 ft)of <br /> bentonite grout, I m(3 ft)of cement/bentomte, and .10 <br /> 1 in (3 ft) of bentonite, in that order,to seal the annular w8fters"04 M <br /> space to prevent"short-circuiting" of waxer. Water and '=° <br /> fine bubbles are injected into the formation from the is D <br /> lowest screen and retum water enters the middle screen. T ,s 0 <br /> The uppermost screen collects gases from just above the <br /> water(2.5 m [8 2 ftl)to assure vapor control. <br /> RADIUS OF INFLUENCE r° <br /> The C-Sparge'm system is designed to achieve ••o s �D 235 <br /> the injection and distribution of microbubbles into the WOMM <br /> aquifer to be treated. The pressure of the gas injection, s X35 ==0 <br /> use of microporous bubblers, and a recirculating well ."4W� ° :65 <br /> system all function to distribute fine bubbles,containing rM weii installation <br /> airlozone gas,through the fine sands under Darcian flow Figure C-Sparge <br /> approximating fluid flow The injection of the airiozone (TW), depth in meters <br /> approximates the injection of water, exhibiting mounding <br /> and outward mox ement until equihbirum is reached <br /> Despite numerous monitoring well corings depicting uniform fine sand formation ��-ith <br /> occasional graNel deposits,the immediate injection pressures and distribution suggested <br /> 4 <br />