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3. EXISTING WASTEWATER FACILITIES <br /> <br />Effluent Bisposal <br />Current effluent disposal practices consist of discharging plant effluent into the Willamette <br />River. The WPCF has historically met all regulatory requirements for secondary effluent <br />disposal with one exception. On May 17, 1991 the daffy mass limit was exceeded for TSS and <br />BOD. Effluent is preferentially disposed of through a submerged diffuser in the Willamette <br />River. The NPDES permit requires the use of the submerged diffuser from May 22 through <br />October 31. Peak wet weather flows over 103 mgd consist of blended primary and <br />secondary disinfected effluent. The wet weather hydraulic capacity of the WPCF is <br />estimated at 175 mgd, although higher flow rates approaching 215 mgd have been achieved. <br />The current practice for discharging peak wet weather flows in excess of the submerged <br />diffuser outfall capacity is to overflow into a bankside outfall. These overflows occur at a <br />weir located at the outfall control structure. The current NPDES permit allows the bankside <br />outfall to be used from November 1 through May 21 to accommodate peak wet weather <br />flows. <br /> <br />Thickening <br />WAS is currently thickened at the WPCF with the use of GBTs. The GBT facility houses two <br />3-meter gravity belts, a polymer distribution system, and the thickened WAS pumps. WAS <br />flows either by gravity or pumped flow from the RAS control structure to the GBT facility. <br />The WAS flow rate is metered and controlled with flow control vanes at the RAS and/or <br />GBT control structure. Prior to thickening, the WAS is conditioned with a cationic polymer. <br />Thickened WAS is typically around 5 percent solids and is pumped directly to the digester <br />for anaerobic digestion. Table 3.2.2-5 summarizes the waste activated sludge unit process <br />and associated equipment. <br /> <br />TABLE 3.2.2-5 <br />WPCF Waste Activated Sludge Thickening Unit Processes and Equipment <br />MWMC Facilities Plan, Eugene-Springfield <br /> <br /> Capacity, (each/total <br /> Equipment Type Quantity firma/totalb) <br /> <br />Gravity Belt Thickeners 3-meter, 95% solids capture, 5% solids, 2 48,250/48,250/96,500 lb/day <br /> MWWW SLR= 2010 lb/hr, MWWW HLR = <br /> 120 gpm/m <br /> <br />WAS feed pumps Screw centrifugal with adjustable frequency 2 800/800/1,600 gpm <br /> drive (AFD), 15 hp <br /> <br />Thickened Waste Progressive cavity with AFD, 20 hp. 2 120/120/240 gpm <br />Activated Sludge Pumps <br /> <br />Polymer System Liquid tote polymer system, 17 lb/ton 2 i7/17/34 lb/ton <br /> capacity <br /> <br />Notes: <br />a Total firm capacity is with largest unit out of service. <br />bTotal capacity is with all units in service. <br /> <br />Anaerobic Digestion <br />Three primary anaerobic digesters located at the WPCF stabilize primary sludge and <br />secondary WAS. Each digester is 85 feet in diameter and contains a fixed cover. Table 3.2.2-6 <br />summarizes the anaerobic digestion unit processes and associated equipment. <br /> <br /> MWMC_3.0_REV11.DOC 3-13 <br /> <br /> <br />