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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />This condition deserves careful consideration, since the first taps on the system are adjacent to <br />the treatment plant and can receive water in about I minute. A preliminary assessment <br />indicates that this condition cannot be corrected by modifications to the existing clearwell <br />structure or changing current operations. <br /> <br />CWorine feed equipment appeared to be operating normally; operators report that the feed rate <br />can be visually observed. However, due to the hazardous nature of cWorine, we recommend <br />that chlorine gas warning signs be placed in prominent locations within and around the <br />building. <br /> <br />In summary, addition of tankage, or its equivalent, for chlorine contact is required, external to <br />the existing plant. The correction scheme will also require piping modifications. Note that <br />cWorine residual data and chlorine feed rate data are not available. Without this data, a log <br />reduction analysis for Giardia cysts cannot be performed in this preliminary evaluation. <br />Operators report, however, that annual tests have been performed on treated water for Giardia <br />cysts by a certified laboratory. All tests have been negative. <br /> <br />High Service Pumps to Storalle/Distribution <br /> <br />The high service pumps are rated as follows by name-plate data: <br /> <br />Pump No.1 Worthington 75 HP 12M90-4 <br />Pump NO.2 Worthington 40 HP 12LF4 <br /> <br />900 g.p.m. @ 240 TDH <br />500 g.p.m. @ 240 TDH <br /> <br />On the peak day of 1993, Pump No.1 pumped at 1043 g.p.m. for 15.6 hours. Using these <br />data, the plant capacity with Pump No. lon-line, and adjusting for 3 backwash cycles under <br />existing filter operations, is 1.32 MG in 24 hours. <br /> <br />Production with the use of two pumps in parallel is now unknown. Such an estimate would <br />require the analysis of piping, pump curves, and system curve characteristics. However, a <br />conservative estimate, factored by 0.75, is about 1.46 MGD. Because all finished water must <br />be pumped into the system for use, these pumps remain the primary hydraulic constraint on <br />capacity. At the same time, no standby power source is available to the plant. With a full <br />storage tank of treated water, at the average usage rate for the peak month of 0.68 MGD, the <br />system has (1.0/0.68) x 24 = 35 hours of water available, should a pump breakdown or power <br />failure occur. Considering this conclusion and the aforementioned lack of clearwell contact <br />time for disinfection, it appears that consideration of a new, external clearwell with standby <br />pumping capability and an emergency power supply is appropriate for the existing water <br />treatment plant. <br /> <br />Solids Handlinll <br /> <br />22 <br />