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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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5/12/2004 3:16:01 PM
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Agenda Item Summary
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5/19/2004
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MWMC FACILITIES PLAN <br /> <br />the influent flow requirements. A biofilter is used to remove air odors at 13,000 ft3/min <br />e(City of Eugene, 2004). <br /> <br />The current capacity of the preliminary treatment facilities ranges from 175 to 210 mgd, and <br />is limited by the influent screening capacity (see "Peak Flow Management Alternatives" <br />technical memorandum in the appendix). <br /> <br />Primary Treatment. During primary treatment, solids and scum are removed through settling <br />and skimming (City of Eugene, 2004). Primary clarifiers thicken the sludge to 4 to 6 percent <br />solids. The thickened sludge is pushed by rake arms into a hopper, where the sludge is <br />transferred by air-operated diaphragm pumps to the primary (anaerobic) digesters <br />(Management Plan for a Dedicated Biosolids Land Application Site [CH2M HILL, 2003]). <br /> <br />The effective peak flow primary treatment capacity is approximately 90 mgd with all four <br />primary clarifiers in service, although the facility moves in excess of 200 mgd through the <br />clarifiers during peak flow events. <br /> <br />Secondary Treatment. Secondary treatment at the WPCF consists of aerating and recycling <br />bacteria, and converting fine particles and dissolved organic matter into settleable solids <br />(City of Eugene, 2004). Secondary treatment facilities consist of eight aeration basins and <br />eight secondary clarifiers. <br /> <br />During secondary treatment, sludge can be thickened in one of two ways, co-thickened by <br />mixing WAS with primary influent and settled in primary clarifiers or thickened directly at <br />the GBT. The activated sludge flow can be routed to the grit channels to be mixed with <br />primary influent or the WAS is combined with polymer and applied to the gravity filter <br />belts, then thickened to 4 percent dry solids. After thickening, the waste activated sludge is <br />pumped to the anaerobic digestion process. <br /> <br />During the anaerobic digestion process, sludge is inoculated with bacteria and heated to <br />approximately 36°C. Bacteria reduce the organic material to water, carbon dioxide, and <br />methane gas. The process takes 15 to 35 days, depending on the amount of sludge pumped <br />into the digesters. The methane gas is used to produce heat and electrical energy, which is <br />used in the operation of the Regional Treatment Facihty. <br /> <br />The current peak flow secondary treatment capacity is estimated at 103 mgd and is limited <br />by secondary clarification. PE flows over 103 mgd are diverted around secondary treatment <br />through a diversion conduit and recombined with the SE prior to disinfection. <br /> <br />Disinfection. Disinfection, the final wastewater treatment stage at the WPCF, consists of <br />disinfection by chlorine, followed by addition of sulfur dioxide to dechlorinate. Disinfection <br />facilities consist of gaseous chlorine, four chlorine contact basins, and gaseous sulfur <br />dioxide. <br /> <br />The peak flow disinfection capacity, estimated at 215 mgd, typically is limited by the <br />chlorinators, although hydraulic restrictions based on river level may limit capacity to <br />175 mgd. <br /> <br />2 The biofilter has a peak capacity of 18,000 cfm. <br /> <br />9-2 MWMC_9.0_REV14.DOC <br /> <br /> <br />
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