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NEUTRALIZATION TANKS <br /> STRAINING AND <br /> STORM WATER FILTRA4mgd <br /> BACKWASH AND RINSING <br /> PUMP STATION SOLUTIONS <br /> 0.06 mgd` <br /> 0.86mgd <br /> 11.31mgd b 1.31 mgd b <br /> Zs' TORM WATER I <br /> INFLUENT, VARIES° <br /> BACKWASHED SOLIDS <br /> FUTURE FLOW EQUALIZATION <br /> GROUNDWATER BASIN 1.31 mgd° <br /> WELLS, 1.31 mgd It <br /> OUTFALL 001 <br /> SOLIDS TO STOCKTON DIVERTING <br /> TO LANDFILL CANAL AND CALAVERAS <br /> a. FLOW INTO PLANT WILL BE BALANCED DISPOSAL RIVER. <br /> BETWEEN STORM WATER AND GROUNDWATER <br /> SBE 1.31 mqd O THAT TOTAL FLOW THROUGH PLANT WILL SETTLED SOLIOSd DRYING BEDS <br /> AFTER MAX. EXPANSION. <br /> b. MINOR LOSES FROM BACKWASHING ARE NOT <br /> REFLECTED. <br /> C. 60,000 GAL. BATCH MAX. WILL BE DISCHARGED THE MARLEY COOLING TOWER <br /> AFTER NEUTRALIZATION AND SAMPLING APPROX. COMPANY <br /> EVERY 10 DAYS. <br /> STOCKTON, CALIFORNIA FACILITY <br /> d. FLOW QUANTITIES WILL BE VARIABLE AND <br /> DEPENDENT ON SOLIDS PRESENT IN INFLUENT. <br /> SCHEMATIC OF LIQUID <br /> TREATMENT FLOW <br /> - FIGURE 2 _-- <br /> i <br />