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Nestle USA, Inc., Ripon, California March 31, 2011 <br /> 2010 Annual Report <br /> In June 2009, Nestle submitted a proposa125 to the RWQCB to modify the pumping at EU-3 for a <br /> 60 day period following observed reduction in the extraction and treatment system mass <br /> removal rates. The purpose of the pumping modification was: <br /> • To assess the possibility of extracting additional mass within the stagnation zone, and <br /> • To evaluate future changes to the operation to optimize mass removal. <br /> ECM installed additional wells (M-50A and M-51A) in December 2009, in response to the <br /> RWQCB's request to verify the current extent of capture provided by the EU-3 and EU-4 wells. <br /> In May 2010, ECM shut down the Industrial Avenue extraction and treatment system for 72 <br /> hours to collect groundwater elevation data for the new and old monitoring wells and to estimate <br /> the hydraulic capture zone for extraction wells EU-3 and EU-4. ECM's capture analysis <br /> indicated that the actual capture zone is slightly larger in size than the capture zone predicted <br /> by the groundwater flow model, suggesting that the numeric groundwater flow model represents <br /> a conservative estimate of the hydraulic capture actually provided by wells EU-3 and EU-4 <br /> under in-field pumping condition S26. <br /> Field parameters including TDS, temperature, conductivity, and pH in the Industrial Avenue <br /> extraction and treatment system effluent are measured twice per month in accordance with <br /> MRP requirements (Appendix E). Metals concentrations in the influent samples were found in <br /> ranges similar to historical metals concentrations in groundwater (see Table 9.1). The TDS <br /> concentration for the system effluent in 2010 increased from 790 mg/L on January 7, 2010 to <br /> 1050 mg/L on December 28, 2010. The average TDS concentration in 2010 was 964 mg/L as <br /> compared to 943 mg/L in 2009. <br /> No COCs were detected in any of the effluent samples collected from the Industrial Avenue <br /> extraction and treatment system during the 2010 sampling events. The treatment system was <br /> 100% efficient in removing COCs from the extracted groundwater. No modification to the <br /> treatment system is warranted at this time. Nestle will continue to evaluate the groundwater <br /> extraction and treatment system in 2011 and adjust the system operation to maintain efficient <br /> and effective mass removal and hydraulic containment. <br /> 4.2 STOCKTON AVENUE EXTRACTION AND TREATMENT SYSTEM <br /> The Stockton Avenue groundwater extraction and treatment system was equipped with an air <br /> stripper to remove VOCs from the extracted water prior to discharge to the City of Ripon non- <br /> potable water system. VOCs in the off-gas from the air stripper are destroyed with a catalytic <br /> oxidizer prior to discharging the off-gas to the atmosphere. The system ceased operation in <br /> October 2010 as discussed below. <br /> 4.2.1 OPERATION AND MAINTENANCE <br /> The Stockton Avenue system extracted and treated a total of 57.4 MG of groundwater through <br /> the Third Quarter 2010, prior to shutdown in October, removing approximately 19.42 pounds of <br /> VOCs. This is equivalent to 0.34 pounds of VOCs removed per million gallons of water <br /> extracted (Table 10). The system discharged the treated groundwater to the City of Ripon non- <br /> potable water system during the first three quarters of 2010. The E-2 extraction well pumped at <br /> an average rate of 71 gpm, removing approximately 27.91 MG of groundwater from the Upper <br /> Aquifer in 2010. The E-6 extraction well pumped at an average of 76 gpm, removing <br /> approximately 29.88 MG of groundwater from the Intermediate Aquifer. <br /> Between January 1, 2010 and October 1, 2010, the system downtime was approximately <br /> 270.85 hours for maintenance, repairs, and system initiated shut-downs designed to protect the <br /> 22 <br />