Laserfiche WebLink
1 <br /> maintained through the air stripper to trunimize scale formation on the tower packing. Pump P9 <br /> and flow control valve FCV 1 have been selected to deliver a constant flow rate of 20 gpm to the <br /> iair stnpper <br /> The air stripper is designed conservatively, and even under severe operating conditions (air <br /> temperature 30 F, water temperature 60 F) it should remove at least 99.9 percent of the gasoline <br /> from the groundwater Water not recirculated back to tank T3 flows by gravity into holding tank <br /> T4 Pump P10 pumps the air stripper effluent from tank T4 through two activated carbon vessels <br /> (CV 1, CV2) plumbed in series. The carbon will be used to remove any detectable residual gaso- <br /> line remaining in the air stripper effluent so that a portion of the treated water may safely be <br /> reinfected into the uppermost saturated zone <br /> The effluent from the carbon absorbers is transferred to monitoring tank T5 The headspace of <br /> this tank is monitored for the percentage of the lower explosive limit (LEL) of gasoline If <br /> hydrocarbon vapors are detected above one percent of the LEL in this tank, a ball valve is <br />' automatically closed, and the entire groundwater extraction and treatment system is shut down to <br /> prevent untreated water from being discharged from the system Before fluid discharge, the <br /> treated water goes through sterilizer UV2 <br /> The entire system, including piping, hose, and equipment,uipment, will be secondarily contained Four- <br /> inch piping will be trenched from the recovery wells and reinfection wells to the base of the <br /> treatment system to act as ducting and secondary containment for the well pump hoses The <br /> treatment system itself will be placed on a bermed concrete pad The treatment area will be <br /> appropriately marked with the necessary Uniform Fire Code (UFC} and National Fire Protection <br /> Association (NFPA) approved hazardous materials storage signs <br /> t2.6 TASK V - SYSTEM STARTUP, OPERATION,MAINTENANCE, AND REPORT- <br /> ING <br />' After the treatment system is installed, the system will be brought online over a three-day period <br /> This startup will include the adjustment of the recovery pumps, measurement of water and air <br /> flows, and measurement of treated effluent quality. <br /> - After the treatment system is brought online, the influent and effluent will be sampled and ana- <br /> lyzed to ensure that treatment equipment is functioning properly and meeting discharge stand- <br /> ards. The extraction and treatment system operation and maintenance manual is provided as <br /> Appendix D The effects that the pumping and percolation system have on the aquifer will be <br /> closely monitored to ensure that the system is not overpumping and that the hydraulic barrier is <br /> sufficient to isolate the site hydraulically from any adjacent sites <br /> 06W-s6 n3%2rJ 191/m 16 <br />