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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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6/10/2010 4:49:14 PM
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7/7/2004 4:37:39 PM
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City Recorder
CMO_Document_Type
Resolutions
Document_Date
6/28/2004
Document_Number
4793
CMO_Effective_Date
6/28/2004
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DEVELOPMENT AND EVALUATION OF ALTERNAllVES <br /> <br />System alternative 1 does not increase treatment capacity or alter existing operations to <br /> system efficiency. Although cost is zero, the ability to meet future NPDES <br />increase <br /> the <br />permits and EPA requirements for projected plant capacities is unlikely, if not impossible, <br />without substantial upgrades or improvements to existing facilities. Therefore, this <br />alternative was eliminated for further consideration. <br /> <br />Figure 6.6.3-1 shows a potential site layout for system alternative 2. In addition to those <br />facilities required for all alternatives, this alternative includes the construction of four new <br />primary clarifiers, a new aeration basin, and six additional new secondary clarifiers. This <br />system alternative would result in the highest capital investment and requires the most site <br />space. This is significant because the only available site space that could be used is reserved <br />for future build-out of secondary treatment capacity. Additionally, the primary clarifiers <br />would be located a long distance from the existing primary clarifiers, requiring separate <br />primary sludge handling and odor control facilities. Thickening of primary sludge outside <br />the primary darifier would not be required with this alternative; however, it is <br />recommended. This system alternative would be capable of treating 100 percent of the <br />projected PWWF thi'ough primary and secondary treatment and no blending would be <br />required. However, all these additional new facilities would be constructed to mitigate <br />PWWF that only occurs on a relatively infrequent basis. It is therefore recommended that <br />this alternative be removed from further consideration because of its extremely high capital <br />cost. <br /> <br />Figure 6.6.3-2 shows a potential site layout for system alternative 3. In addition to those <br />facilities required for all alternatives, this alternative includes the construction of four new <br />primary clarifiers. Less costly than system alternative 2, this system alternative has the <br />benefit of providing primary treatment for 100 percent of the PWWF. As in system <br />alternative 2, this alternative provides redundant primary treatment capacity, because a <br />total of eight prLmary clarifiers would be available. The new primary clarifiers will occupy <br />excessive site space allocated to future expansion of secondary treatment facilities. <br />Additionally, if these clanfiers were constructed they would be located a long distance from <br />the existing primary clarifiers, further complicating primary sludge handling and odor <br />control facilities. Thickening of primary sludge outside theprimary clarifier would not be <br />required with this alternative; however, it is recommended. Blending would be required for <br />this alternative to meet the anticipated NPDES permit requirements. This alternative is <br />feasible cost-wise, and should be considered further for permit compliance. <br /> <br />Figure 6.6.3-3 shows a potential site layout for system alternative 4. In addition to those <br />facilities required for all alternatives, this alternative includes the construction of a new <br />high-rate clarification pump station and new high-rate clarification facilities. System <br />alternative 4 offers the greatest operational flexibility as it would allow the HRC to function <br />as primary clarifiers and would allow the existing primaries to be taken off line if necessary. <br />Thickening of primary sludge outside the existing primary clarifiers would be required with <br />this alternative to reduce the overall HRC needs. HRC can function in multiple modes, <br />either to treat base dry season flows or to treat WWPH flows. The HRC system would <br />reqttire more extensive O&M than either system alternatives 1, 2, 3, and 5 because the <br />monthly exercising of the system would be significantly more involved. This system would <br />also experience higher operational costs because of chemical requirements and electrical <br />costs associated with the would be for this alternative <br /> system. <br /> Blending <br /> required <br /> to <br /> meet <br /> the <br /> <br />MWMC_60_REV11.DOC 6-55 <br /> <br /> <br />
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