Laserfiche WebLink
CLEARW___'�IATER %"0' <br /> G R O U P, I N C. <br /> E—iron—,.tat Ser ices <br /> technology, they also demonstrate the need for multiple extraction points. As <br /> you are aware, the greatest cost associated with remedial action falls into the <br /> categories of capital expense (for the actual treatment equipment) and time/labor <br /> costs for system operation and maintenance. There would likely be no increase <br /> in treatment equipment cost under a two well extraction scenario, as the <br /> water/vapor flow rates would fall within the tolerance (flow rates and <br /> contaminant concentrations) required for the equipment to be installed in a <br /> single well scenario. The savings associated with shortening the length of <br /> remedial action would be significant. Under best case conditions the length of <br /> remedial operations would be reduced by half. <br /> • Clearwater believes passive skimmers provide a limited response, given the <br /> concentration and extent of separate and dissolved phase contamination at this <br /> site and the larger-scale remedial attention necessary to address said <br /> contaminants. Skimmers would be useful if the PHS/EHD wanted to consider a <br /> non-aggressive approach that relies on natural forces for the attainment of <br /> project endpoints. The skimmers would then likely be the only device deployed <br /> at the site. <br /> Given the facts presented in the RAP, and reiterated above, Clearwater requests <br /> PHS/EHD reconsideration of the existing conceptual design. In accordance with <br /> USTCF guidelines, the next phase of project activity will be put to competitive bid. <br /> Clearwater recommends that Mrs. Ruiz and her attorney include the PHS/EHD May <br /> 23 letter and this response in the bidders package. It would be most helpful if the <br /> PHS/EHD specified more definitively specific ideas for an alternate remediation <br /> plan. <br /> Problem Assessment Report <br /> Several issues were raised by the PHS/EHD regarding the information presented in <br /> the Problem Assessment Report (PAR) section of the February 21 submittal. We <br /> have tried to address them in order of relative importance: <br /> • PHS/EHD staff recalculated the amount of hydrocarbon contamination using an <br /> oval footprint for the hydrocarbon plume and a maximum site hydrocarbon <br /> concentration of 28,000 ppm (detected in a sample apparently collected during <br /> underground tank removal in February, 1989). PHS/EHD calculations indicate <br /> that 137,200 lbs of hydrocarbons are present in the subsurface. Assuming that <br /> gasoline is 0.72 times the density of water, this equates to almost 30,000 gallons of <br /> gasoline. Given the chemical data collected during this project, we believe that <br /> this estimate is excessive. <br /> The estimation of the amount of product in the subsurface is difficult, at best. <br /> There is no dispute that significant levels of contaminant are present, as <br />