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Resolution No. 4793
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2004 No. 4782-4819
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Resolution No. 4793
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Last modified
6/10/2010 4:49:14 PM
Creation date
7/7/2004 4:37:39 PM
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Template:
City Recorder
CMO_Document_Type
Resolutions
Document_Date
6/28/2004
Document_Number
4793
CMO_Effective_Date
6/28/2004
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MWMC FACILITIES PLAN <br /> <br />Reliabil~ Class I Requirements <br />MWMC Facility Plan, Eugene-Springfield <br /> <br /> Plant <br />Component Requirement <br />Filtration 75% of design flow capacity with largest unit out of service. Design flow is defined as <br /> the flow used as the design basis of the component. <br />Ef/luent Pumps Peak flow with largest umt out of service. Peak flow is defined as the maximum <br /> wastewater flow expected during the design pedod of the treatment works. <br />Electrical Power Two separate and independent soumes of electrical power shall be provided, e~ther <br /> from two separate utihty substations or from a single substation and a works-based <br /> generator. Designated backup source shall have sufficient capacih/to operate all <br /> vital components, critical lighting, and ventilation during peak flow conditions <br /> <br />The reliability criteria for sludge processes presented in Table 5.1.6-2 are also based on the <br />guidance offered in EPA's Works Design Criteria. <br /> <br />TABLE 5.1.6-2 <br />Studge Handling System Reliability <br />MWMC Faciltty Plan, Eugene. Springlfeld <br /> <br /> System <br /> Component Requirement <br /> <br /> Sludge Holding The volume of the holding tank shall be based on the expected time necessary to <br /> Tanks perform maintenance and repair of the component in question. <br /> Anaerobic Sludge At least two digestion tanks shall be provided. At least two of the digestion tanks <br /> Digestion provided shall be designed to permit processing of all types of sludges normally <br /> digested. <br /> Sludge Pumping Pumps sized to pump peak sludge quantity and maintain velocities above 2 fps. Prowde <br /> a minimum of 2 pumps. <br /> <br />5.2 Basis for Cost Estimate <br />Unit process and system alternative cost comparisons are to be based on total project or <br />relative project costs. Project costs are calculated to include legal costs, administrative costs, <br />contingency costs, and engineering costs in addition to the construction and axmual <br />operation and maintenance costs. End-of-life salvage value will not be considered in the cost <br />evaluations. <br /> <br /> Relative cost estimates are typically used to compare alternatives in which rmany of the <br /> facilities in each alternative are identical. Only those costs that are unique to each alternative <br /> are estimated and used for comparison purposes. This approach is useful when considering <br /> systemwide alternatives in which many of the facilities are the same and the relative costs of <br /> each alternative can be narrowed down to selected facilities. Costs for the selected <br /> <br /> 5-22 k~WMC_5.O_REVS_VKS,DOC <br /> <br /> <br />
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