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4 <br /> based on 24-hour maximum design flows of 50, 000 GPD. With a <br /> calculated BODS loading of 171. 19 lbs BODS/day and a maximum daily <br /> BODS and a maximum daily BODS loading capacity of 108. 0 lbs, the <br /> aerated buffer tank will pretreat the incoming waste, thus lowering <br /> the BOD to a level less than 280 mg/L prior to its entering the <br /> main plant aeration chamber. The Bio-Pure process is not subject <br /> to upset by flow variations because a constant quantity waste is <br /> treated in each batch. <br /> For this project, the basic Bio-Pure 500EFO-1 has a hydraulic-flow <br /> oversize capacity of 4 , 900 gallons per day. Adding the 11, 655 <br /> gallon reserve (safety) capacity, which is designed into the <br /> aeration chamber, and the 4 , 900 gallon oversizing effectively gives <br /> the system an internal flow equalization and safety factor of <br /> 16, 555 gallons per day, which equals 36 . 71% of calculated daily <br /> flows, or 33 . 11% of system design flow capacity. <br /> Since the system feed pump is located near the bottom of the 20, 000 <br /> gallon front-end buffer tank, at least 18, 000 gallons of additional <br /> volume are available as flow-equalization capacity. Adding this <br /> 18 , 000 gallons to the above 16, 555 gallon safety factor raises the <br /> total reserve capacity to 34 , 555 gallons, or 76 . 62% of the <br /> calculated daily flows, or 69 . 11% of the system design flow <br /> capacity. <br /> Under normal sequence of operations, the collection system will <br /> deliver the wastewater from the generating facilities to the <br /> aerated buffer tank. From the buffer tank, the wastewater is <br /> lifted in the aeration chamber. Float controls are used to start <br /> and stop the system feed pump in the buffer tank. A major concern <br /> is to prevent wastewater from remaining in the buffer tank in an <br /> anaerobic state for a long period of time and it is for this reason <br /> that the buffer tank is aerated. Under maximum daily flow <br /> conditions, the system batch sequencing processes a batch from the <br /> aeration chamber at least once every 97 minutes, and the fill rate <br /> of the total reserve capacity during the twice-daily peak flows is, <br /> on average, less than 111 GPM. The maximum amount of incoming <br /> waste over the 97 minute batch in period would total 10, 777 <br /> gallons; subtracting that from the total reserve/safety capacity <br /> _ leaves a 23 , 778 gallon reserve capacity. Under peak flow <br /> conditions, the entire 201000 gallons (400 of daily flows) could be <br /> stored in the buffer tank should the aeration chamber be at its <br /> . maximum standby level . This arrangement assures that the system <br /> cannot overflow. <br /> The digestion process in the aeration chamber is carried out with <br /> the introduction of air into the incoming wastewater. The soluble <br /> material, oxidized material, settleable solids and suspended solids <br /> form a mixed liquor. Aeration. chamber residence time for the <br /> digestible materials a minimum of 16 hours of combined time and is <br /> dependent on the final system timing, which is based on effluent <br /> testing. This reduced mean-cell-retention-time is possible due to <br />