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FROM <br /> STORM WATER NEUTRALIZATION <br /> INFLUENT, TANKS, S gpm (AVG.)5 <br /> VARIES 2 STORM HOLDIN H <br /> pq% HOLDING <br /> NC <br /> TANK <br /> STATION I -_ <br /> NORTH YARD 5 <br /> GROUNDWATER, gpm I 4 <br /> VARIESI (AVO. it FAND HLLARIF IEBK 300 gpm MIXED <br /> II \f\IL1RgTE <br /> ILTER PRF <br /> EEDIA <br /> SS [300 gpmM FILTERS <br /> F <br /> VARIESI INFLUENT 300 EREDUCTEMICRL <br /> HOLDING gpm EULT IDN/ 300 gpm DEGASSING 300 gpm4 <br /> TANK PRECIPITATI TANK <br /> UNIT <br /> FLOW <br /> GROUNDWATER VARIESI EQUALIZATION ---- <br /> BASIN SETTLED <br /> SOLIDS 3 <br /> 200 gpml STRAINING 200 gpm4 ION 200m4 <br /> "N0 EXCHANGE gp <br /> – FILTRATION UNIT <br /> NOTES: _ _ <br /> 1. GROUNDWATER IS TREATED AT AN EFFECTIVE BRCKNRSHEO _ I <br /> FLOW RATE OF 500 gpm THROUGH THE ION SETTLED I SOLIDS 3 I 500 gpm4 <br /> EXCHANGE AND ELECTROCHEMICAL REDUCTION/ SOLIDS 3 BRCKWRSH AND <br /> PRECIPITATION TREATMENT UNITS. FLOW I <br /> CONSISTS OF NORTH YARD GROUNDWATER [PUMPED RINSING SOLUTIONS <br /> DIRECTLY TO INFLUENT HOLDING TANK) <br /> AND GROUNDWATER PUMPED FROM EXTRACTION <br /> SYSTEM TO FLOW EQUALIZATION BASIN. SLUDGE HOLDING <br /> FLOW RATES FROM EACH SOURCE VARY. <br /> MAXIMUM FLOWS TO EACH TREATMENT UNIT TANKS <br /> VARY. <br /> 2. STORM WATER TREATMENT OCCURS THROUGH ---- <br /> m THE ELECTROCHEMICAL REDUCTION/PRECIPITATION <br /> L4 UNIT AT A MAX FLOW OF 300 ggppm. STORM DISCHARGE 002 <br /> DI ONSITE DISCHARGE 001 <br /> o WATER TREANENT INTERRUPTS GROUNONATER TO STOCK TON <br /> K TREATMENT THROUGH THIS UNIT. FORMER SOIL FLUSHING DIVERTING CANAL <br /> NEUTRALIZATION $YSTEM <br /> i 3. FLOW QUANTITIES TIES ARE VARIABLE DEPENDING NOING ON - <br /> u <br /> SOLIDS PRESENT IN INFLUENT. TANKS <br /> FILTER PRESS (USED FOR INJECTION WELLS <br /> s 4. MINOR LOSSES FROM SOLIDS REMOVAL. ARE NOT EQUALIZATION) <br /> 0 REFLECTED. <br /> S. UP TO 180.000 GALLONS OF NEUTRALIZATION <br /> TANK LIQUIDS ARE PRODUCED PER MONTH AND FILTRR IE S gpmIAVG IS <br /> N TREATED THROUGH THE ELECTROCHEMICAL TO <br /> REDUCTION/PRECIPITATION UNIT UP TO A RATE BACKWASH <br /> c�.. OF 10 gpm. THIS VOLUME IS NOT ACCOUNTED FOR HOLDING <br /> ua,^ IN THE WATER BALANCE. TANK 1 I THE MARLEY COOLING TOWER <br /> omW 2 REVISED JUNE 2, 1993 ` COMPANY <br /> FILTER CAKE i0 OFFSITE� STOCKTON, CALIFORNIA FACILITY�a 1 REVISED JULY I8. 1991 DISPOSAL <br /> 0 ISSUED AUGUST 18.1990 TO ANOCO SYSTEM INFLUENT WATER TREATMENT PLANT <br /> r <br /> Me — HOLDING TANK FOR TREATMENT WATER BALANCE <br /> ATTACHMENT C <br />