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<br />Collection System Pump Stations <br />The category collection system pump stations consist of pump stations that 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 Wilakenzie Pump Station. These regional pump stations <br />have the same functional and design criteria basis as the regional collection system <br />pipelines, and, therefore, the allocations are: <br />? <br />Average Flow - 1/4 <br /> <br />? <br />Peak Flow - 3/4 <br /> <br />Preliminary Treatment <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 “suspended” material (or TSS). Consequently, the loading parameters of BOD <br />and TSS 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 /> <br />? <br />Peak Flow - 3/4 <br /> <br />Primary Treatment <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 TSS 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, twice as much TSS is removed relative to BOD. <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 />Combining the functional basis with the design criteria basis, the following allocation is for <br />primary treatment: <br />? <br />Average Flow - 1/4 <br /> <br />? <br />BOD - 1/4 <br /> <br />? <br />TSS - 1/2 <br /> <br />Page 24 OF 39 <br /> <br /> <br />