Laserfiche WebLink
� v <br /> a <br /> i � <br /> A S S o C I A T E S I N C <br /> groundwater being generated during extraction of vapor from the vapor wells Subsequent system <br /> modifications were made as described in Section 5 3 <br /> ' During the week of Feb 10, 2003 ATC personnel installed a Gast 2567-P1 - <br /> ��rY � p 32 T908X rotary <br /> vane compressor to operate the air sparge component of the system The compressor is capable <br /> 1 of creating a maximum of 20 pounds per square inch pressure and a maximum airflow rate of 18 <br /> standard cubic feet per minute <br />' 5.3 Groundwater Treatment and Discharge Equipment <br /> During initial start up of the vapor extraction system, approximately 25 gallons of groundwater <br /> per hour was extracted from the four vapor wells ATC closed the valves on vapor extraction <br /> wells V W 1 and V W2 and only extracted vapors from vapor wells V W3 and V W4, which are <br /> 1 screened approximately two feet above the current water level Seven gallons of groundwater <br /> per hour was extracted from vapor wells V W3 and V W4 <br /> 1 ATC contacted the City of Stockton Department of Municipal Utilities (DMU) and submitted the <br /> necessary permit application information for the discharge of treated groundwater The DMU <br /> issued the Groundwater Discharge Permit (GDP) on November 6, 2002 Following the issuing of <br /> the GDP, approximately 50 feet of 3-inch diameter, ABS pipe was placed on the surface of the <br /> site from the remediation compound to a discharge point Iocated inside the bathroom of the on- <br /> site building The ABS pipe was connected to the existing sewer discharge line by a California <br /> 1 Licensed Plumber during the week of November 25, 2002 <br /> To operate the vapor extraction system, ATC modified the vapor extraction system to include the <br /> treatment and discharge of the groundwater during operation of the vapor extraction system to the <br /> City of Stockton sewer system The extracted groundwater is separated from the extracted vapor in <br /> a 50-gallon knockout tank located on the thermal oxidizing unit The knockout tank is equipped <br /> with water level sensors and when the knockout tank is approximately 80% full of groundwater, a <br /> transfer pump pumps the water from the knockout tank into a 1,000-gallon poly drop tank that is <br /> also located inside the remediation compound The drop tank is equipped with water level sensors <br /> and when the drop tank is approximately 80% full of groundwater, a second transfer pump pumps <br /> the water from the drop tank through the carbon filtration system The transfer pump stops <br />' pumping when the drop tank is reduced to 55% capacity <br /> The carbon filtration system includes three 200-pound ASC200 carbon vessels containing liquid- <br /> phase granular activated carbon The three ASC200 carbon vessels are connected in series by a <br /> hose connection system The activated carbon has an efficiency of 99% The three carbon vessels <br />' are setup in series with sampling ports before the first carbon vessel, in between each vessel, and <br /> after the third vessel <br /> 1 Components of the groundwater treatment system located in the remediation compound include the <br /> knockout tank on the thermal oxidizer from the vapor extraction system, one 1,000-gallon drop <br /> w lwordpro1625961reponshrp doe 6 <br />