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LFR Inc. <br /> LFR has routinely monitored the performance of the system by measuring vacuums, <br /> flow rates, and VOC levels using a PID at the wellheads of SVE and soil-vapor <br /> monitoring wells. A typical iso-vacuum contour map generated using vacuum data <br /> measured at SVE and monitoring wellheads during operation of the SVETS is depicted <br /> on Figure 13. <br /> Figure 14 presents a time versus concentration graph of the SVE mass removal rate <br /> since start-up. This figure graphically displays the initial rapid Hazardous Substance <br /> removal rates (represented by PCE concentrations), which have declined asymptotically <br /> with time and which are currently at de minimis rates of generally less than <br /> approximately 0.2 pound per day. The mass removal rate of the SVETS increased <br /> temporarily upon activation of the Phase IV air sparging system in March 2007. This <br /> occurred as the Hazardous Substances present within groundwater were volatilized into <br /> the overlying vadose zone by sparging air into the underlying Hazardous Substance- <br /> affected groundwater. The sparged air and any Hazardous Substances within the air <br /> were captured and removed by the overlying SVE system. Operation of the sparging <br /> system initially consisted of sparging air(April to August 2007), with ozone being <br /> added in September 2007. <br /> 1.3 Phase IV IRA (Air and Ozone Sparging) <br /> The air and ozone sparging system was started up in May 2007 in accordance with the <br /> "Proposed Phase IV Interim Remedial Action Detailed Plan," dated July 3, 2006 <br /> (LFR 2006). System construction and start-up activities are summarized in LFR's <br /> "Construction Completion and System Startup Report, Phase IV Interim Remedial <br /> Action," dated October 5, 2007 (LFR 2007). <br /> Figure 15 is a histogram that graphically displays the concentration of Hazardous <br /> Substances in samples collected from groundwater monitoring wells located within the <br /> area of the sparge system. This figure shows the average Hazardous Substance <br /> concentrations before sparging was initiated (April 2007), and the rapid Hazardous <br /> Substance reductions over time to the present. In all cases, post-sparging values are at <br /> least one order of magnitude lower than the pre-sparging average; in many cases, the <br /> reduction is two orders of magnitude. These results showed that the system was <br /> effectively remediating Hazardous Substances in the Historical Source Area with only <br /> air. Ozone sparging was started on November 5, 2007, after the October 2007 sampling <br /> event, when the levels of Hazardous Substances in all wells were below 1,000 <br /> micrograms per liter (µg/L). The wells were most recently sampled in January 2009, <br /> and results indicate that all wells contained the lowest concentrations of Hazardous <br /> Substances detected since sparging began. PCE concentrations reported in treatment <br /> system wells during the most recent monitoring event ranged from not detected to 19 <br /> µg/L in well PT-8 (Figures 4 and 15). <br /> pla losu Phll_IV_IRA-Aug09-06750.dm:deh Pap 3 <br />