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Resolution No. 4875
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2006 No. 4856-4897
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Resolution No. 4875
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Last modified
6/10/2010 4:50:03 PM
Creation date
6/14/2006 4:39:45 PM
Metadata
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Template:
City Recorder
CMO_Document_Type
Resolutions
Document_Date
6/12/2006
Document_Number
4875
CMO_Effective_Date
6/12/2006
Repeal_Date
5/7/2007
Author
Mary H. Feldman
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<br />Collection System Pump Stations . <br /> <br />The category collection system pump stations consist of pump stations ~at impart <br />, additional head or pressure to the wastewater so that the flow is conveyed to the WPCF. An <br />example of such a facility is the Willakenzie Pump Station. These r.egional pump stations <br />have the same functional and design criteria basis as the regional collection system <br />pipelines, arid, therefore, the allocations are: <br /> <br />. ' Average Flow - 1/4 <br />. Peak Flow - 3/4 <br /> <br />Preliminary Treatment <br /> <br />Preliminary treatment facilities are located between the, pump stations and primary <br />'treatment, consisting of screenings and grit removal facilities. Minimal organic matter <br />(BOD) is removed during preliminary treatment. Also, solid materials removed during <br />preliminary treatment tend to be large and heavy in nature; these materials are not typically <br />considered a U suspended" material (or TSS). Consequently, the loading parameters of BOD <br />and 1'55 generally do not apply to preliminary treatment, and the unit process category is <br />entirely flow based. The functional and design criteria basis for preliminary treatment are <br />very similar to that of the collection system facilities, and, therefore, the allocation is <br />identical to the preceding categories. The split between average and peak flow is as follows: <br /> <br />. Average Flow-1/4 <br />· Peak Flow-3/4 <br /> <br />Primary Treatment <br /> <br />Primary treatment consists of the four, large, circular concrete basins (primary clarifiers) and <br />the associated equipment used to remove solids that settle to the bottom of the basins. The <br />,purpose of primary treatment from a functional basis is to remove 1'5S and to a lesser <br />degree BOD. Typical percent removal across primary treatment for TSS and BOD are 60 and <br />30 percent, respectively. In other words, twi~e as much TSS is removed relative to BOD. <br /> <br />For the design criteria basis, typical primary clarifiers sizing is governed by both average <br />and peak flow, but for MWMC, where the parallel primary/secondary approach is <br />proposed for peak flow management, the peak flow will be split between primary treatment <br />and secondary treatment. Likewise, if the high-rate clarification peak flow management is <br />ultimately implemented (because regulatory approval is not obtained for the parallel <br />primary / secondary approach), the peak flow will be split between the primary treatment <br />and the high-rate clarification. Therefore, only average flow is considered in the cost <br />allocation~ <br /> <br />Combining the functional basis with the design criteria basis, the following allocation is for <br />primary treatment: <br /> <br />. Average Flow - 1/4 <br />. BOD - 1/4 <br />. TSS-l/2 <br /> <br />A-23 <br />
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