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Item A-MWMC Facilities Plan
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Item A-MWMC Facilities Plan
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6/9/2010 1:11:10 PM
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Agenda Item Summary
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5/19/2004
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MWMC FACILITIES PLAN <br /> <br />TABLE 3,2.2-2 <br />WPCF Primary Clarification Unit Processes and Equipment <br />MWMC Facilities Plan, Eugene-Springfield <br /> <br /> Capacity, (each/total <br /> Equipment Type Quantity firma/totalb) <br /> <br />Primary Clarifier 135-foot-diameter, 12-foot side water depth, 4 21/64/86 <br /> with standard scraper mechanism, 44-inch <br /> influent column <br /> <br />Primary Sludge Pumps 4-inch air-operated diaphragm pumps 4 110/330/440 gpm <br />Primary Scum Pumps 4-inch air-operated diaphragm pumps 2 110/110/220 gpm <br /> <br />Notes: <br />a Total firm capacity is with largest unit out --of service. <br />b Total capacity is with all units in service. <br /> <br />Secondary Treatment <br />The MWMC WPCF currently has a total of eight activated sludge basins to provide <br />biological secondary treatment. The original design was intended to operate in complete <br />mix, plug flow, or contact stabilization mode. The original aeration system consisted of six <br />centrifugal blowers and coarse bubble aeration. In 1996 three of the eight aeration basins <br />were modified and the coarse bubble aeration systems were replaced with fine bubble <br />membrane diffusers. <br /> <br />The secondary treatment average dry weather capacity was estimated at 49 mgd prior to the <br />issuance of the new 2002 NPDES permit. This capacity was based on an adequate solids <br />retention time (SRT) to remove 5-day carbonaceous biological oxygen demand (CBODs) <br />only and does not account for any nitrification. At the same time, the peak hour wet weather <br />treatment capacity was estimated at 103 mgd, limited by secondary clarification capacity. <br />The introduction of nitrification in the 2002 NPDES permit stresses the facility's operation <br />during dry weather as a result of the high solids concentrations maintained in the aeration <br />basins to provide the SRT required for nitrification and the secondary clarifier's inability to <br />handle those additional solids. Historically for wet weather peak flows, primary effluents in <br />excess of 103 mgd are diverted around secondary treatment and blended with secondary <br />effluent and disinfected prior to disposal. <br /> <br />Secondary clarification takes place using the original eight secondary clarifiers constructed <br />in 1984. Mixed liquor is split to each secondary clarifier using sluice gates. Each secondary <br />clarifier is 130 feet in diameter, uses inboard launders, and contains a rapid sludge removal <br />(RSR) mechanism that draws return sludge from the clarifier floor with the use of PVC <br />suction tubes. Secondary scum is removed from the surface of the clarifier and flows by <br />gravity to the secondary scum pump station located in the secondary control complex. <br />Recent data indicate the wet weather peak hour capacity of the secondary clarifers to be <br />111 mgd, somewhat more than the 103 mgd estimated originally. Operations staff have been <br />able to pass these higher peak flows; however, flow management techniques are required <br />for the facility to stay within permit limits. <br /> <br />Return sludge is removed from each clarifier through the RSR mechanism. The return <br />sludge flow can be adjusted from each clarifier using electrically operated and controlled <br /> <br />3-10 MWMC_3.0_REV1 I.DOC <br /> <br /> <br />
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