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' 20 March 2015 <br /> AGE Project No. 00-0769 <br /> ' Page 18 of 19 <br /> ' been 1,100 pg/I in December 2012 and 640 pg/I in October 2011. Trend graphs <br /> illustrating dissolved TPH-g, concentrations versus time for HU-1 through HU-5 <br /> are presented in Appendix F. <br /> ' • TPH-g concentrations in wells MW-5(B-C), MW-6(B-D), and MW-10 decreased <br /> moderately (37-70% reduction) at the conclusion of the pilot test. However, BTEX <br /> ' concentrations in all the above-mentioned wells either increased slightly or <br /> remained stable; and TAME and 1,2-DCA concentrations remained stable. Trend <br /> graphs illustrating dissolved TPH-g, concentrations versus time for HU-1 through <br /> ' HU-5 are presented in Appendix F. <br /> • TPH-g and various BTEX concentrations in wells MW-2A, MW-7A, MW-8A, and <br /> MW-9A increased slightly at the conclusion of the pilot test. However, <br /> ' concentrations were all very low and may demonstrate the influence of the ozone <br /> injection. <br /> ' The injection of ozone over the 183 day period reduced petroleum hydrocarbon <br /> concentrations significantly in wells that were in close proximity (5-15 feet) to ozone <br /> injection wells and had corresponding well screen intervals (MW-5A and OZ-4 through <br /> ' OZ-8); and in wells where ozone injection was capable of dispersing upwards through <br /> well screens (MW-3B and OZ-1 through OZ-3); while, at the same time increasing the <br /> DO and ORP concentrations in surrounding monitoring points. Additionally, ozone <br /> ' injection reduced petroleum hydrocarbon concentrations moderately in wells that had <br /> corresponding well screen intervals (MW-2B and OZ-4 through OZ-8; MW-10 and OZ-1 <br /> through OZ-3) but were not located in close proximity to an ozone injection point. <br /> ' The results of the ozone injection pilot test indicate that ozone can be a feasible <br /> J p e <br /> remedial technology at the site. However, additional ozone injection points, with depth- <br /> discreet well diffusers (deeper than long screened monitoring wells [e.g. MW-1]), <br /> installed in specific locations at the site would be necessary. Additionally, due to the <br /> ' high concentrations, large area and volume, and depth of impacted soil and <br /> groundwater at the site, AGE believes ozone remediation would need to be <br /> supplemented with an additional solute base ISCO/remediation technology (peroxide). <br /> t An additional ISCO technology (liquid: hydrogen peroxide or equivalent) would be <br /> capable of targeting impacted soil and groundwater in the deeper HU2 zone. <br /> ' Based on the results of the semi-annual groundwater monitoring and sampling event <br /> performed in August 2014, AGE presents the following brief conclusions: <br /> • On 04 August 2014, groundwater on-site was generally inferred to be flowing <br /> ttowards the northeast at an average gradient of 0.0008 ft/ft in HU-1; towards the <br /> south at an average gradient of 0.002 ft/ft in HU-2; towards the west-northwest at <br /> an average gradient of 0.001 ft/ft in HU-3; and towards the northwest at an <br /> ' average gradient of 0.002 ft/ft in HU-4 (Figures 3-6). <br /> Advanced GcoEnvironmental Inc. <br /> 1 <br />