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1 <br /> ' significant. During the September 13, 2004 event, benzene was reported at 36 ug/L for a removal <br /> efficiency of 99.9% after approximately 3'/z months of operation. <br /> The successive decline of benzene in EW I from the 35,000 ug/L on June 3, 2004 in each of the <br /> monitoring events following was also significant. During the September 13, 2004 event, benzene <br /> ' was reported at 57 ug/L for a removal efficiency of 99.8% after approximately 3%months of <br /> operation. <br /> During the third quarter monitoring period, concentrations of benzene from MW3 and MW4 <br /> ' declined. The decline of benzene in MW3 does not appear to have accelerated after system start- <br /> up. It appears to have been ongoing at a similar or greater rate of decline. In addition, dissolved <br /> ' oxygen (DO) concentrations in MW3 appear to have been stable. <br /> MW4 is approximately 16 feet from the closest Spargepoint® (IW4). The decline of benzene in <br /> MW4 may have accelerated after system start-up from the 1500 ug/L on June 3, 2004 to later <br /> ' monitoring events (i.e., July 16, 2004, August 13, 2004 and September 13, 2004). During the <br /> September 13, 2004 event, benzene in MW4 was reported at a concentration of 3.0 ug/L. If this <br /> reduction was attributed solely to system activities this would equate to a removal efficiency of <br /> ' 99.8% after approximately 3V2 months of operation. (Note: In addition, DO concentrations may <br /> have increased very slightly in MW4. The slight increase in DO after system start-up may <br /> indicate influence by the C-SpargeTM process.) <br /> Benzene maps were plotted using data from March 17, 2004, June 3, 2004 and September 13, <br /> 2004. The March 17, 2004 and June 3, 2004 sampling data were obtained prior to system start- <br /> up. The September 13, 2004 sampling data was information obtained approximately 3 '/2 months <br /> after system operation start-up. Although there are not apparent reductions in the areal extent of <br /> benzene, significant reductions of benzene concentrations are apparent along the injection well <br /> ' corridor (Figure 21). <br /> 4.5.2 MTBE <br /> During this monitoring period, MTBE concentrations in most wells appeared to remain fairly <br /> consistent (i.e., MW2, MW3, MW5) or show fluctuating trends (MWI, MW4 and EW1) when <br /> compared with concentrations before system start-up on June 17, 2004. The MTBE <br /> concentrations appeared to decrease slightly, however, in MW8. <br /> ' Concentrations of MTBE in MWI, MW2, MW4 and EW 1 are significant and will be used to <br /> evaluate the remediation system effectiveness over time. MWI has the highest concentrations <br /> successively followed by E W 1, MW4 and MW2 (Table 2). <br /> Increases and decreases of MTBE in MWI may be related to periods of system operation and <br /> non-operation. However, the conditions need to be further evaluated over the duration of the <br /> remediation. One item that supports the analysis that the fluctuating concentrations for MTBE in <br /> MWI may be a result of system operation is that the DO also increased significantly after system <br /> start-up. The DO concentration in MWI increased from 0.36 mg/L on June 3, 2004 to 4.72 mg/L <br /> ' on September 13, 2004. <br /> S:126823%QM reports12004 3QR.doc 9 ATC Associates Inc, <br />