Laserfiche WebLink
P <br /> I, <br /> The ground water has a contamination plume that extends horizontally from the station to the east. <br /> Well MW-11 is the most easterly well at this site. The vertical depth of the plume is from the <br /> water table to an unknown depth but boring B-4 found contamination at 160 feet bgs. <br /> In the past we had a Vapor Extractor System operating starting in July 1997 to October 2003. The <br /> system removed about 46,411 pounds of gasoline vapor from this site. <br /> On July 27 and 28 , 2005 we installed two monitoring wells (MW-14 and MW-16) to test the <br /> contamination . <br /> IV Contaminate Transport <br /> The Hydraulic Conductivity of the groundwater is 0. 07203 Feet/Day or 0. 00060 Feet/ Minute . The <br /> shallow ground water flows to the northeast. This shallow groundwater is retained from <br /> descending by clay layer located at 38 to 42 feet bgs on the west side to the station . The majority <br /> of the contamination originates near a line from MW-6 to MW-4. It flows to the east from that <br /> point. The highest point of contamination is in well MW-1 . To treat this contamination , we will <br /> have to treat the water along that line and near the highest source area around MW-1 . <br /> V Remedial Action Objectives and Processes <br /> The contamination plume could be treated with processes to destroy the contamination as it <br /> passes through the area. This can be performed by using a C-Sparger system or by treating the <br /> groundwater with a PulseOX 100 system or natural attenuation . <br /> Process 1 <br /> The C-Sparger wells will be placed in the area near the edge of the site plume. Our plan would be <br /> to place a C-Sparger System in the area close to the east edge of the plume at this site. The work <br /> plan will show the position of the wells and their depth . This will be accomplished by placing six <br /> (6) sparging wells in front of the plume. This work plan will control the majority to the plume. The <br /> estimated cost for this process , this includes the sparging wells, will be around $92 , 000. 00. <br /> Process 2 <br /> The treatment of the groundwater by use of a PulseOX system would obtain data to adjust the <br /> plume clean up. We discussed this with Applied Process Engineering and they recommended we <br /> do a pilot test for four month to see if the PulseOX system will operate properly. <br /> The cost to operate a recommended pilot test for this system for four months will cost <br /> approximately $26, 660. 00. We will have to install two extractor wells to a depth of 65 feet. The <br /> cost to install the wells will be about $5, 000. 00 plus 14 hours for the supervisor, which will cost <br /> about $1 ,600. 00. Four samples will cost around $2 , 000. 00. The water from the nearest <br /> monitoring well will be tested every three weeks to monitor the amount of contamination removed . <br /> Water samples taken during the PulseOX System testing will be six samples and the cost will be <br /> around $ 1 ,620.00. <br /> 5 <br />