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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />certain parts of the pipe will flow as an open channel at atmospheric <br />pressure; without vents, air aCcumulation or vacuum problems will occur. <br />The need and location for vents will change with flows; i.e., a section <br />flowing full may flow at atm()spheric if flows drop and vice versa. It may <br />be better to oversize so the pipe always flows partially full under all flows. <br /> <br />b. C:q>acity bll'll'n on flattest slQpf> The flattest section in the profile selected <br />is used to calculate the minimum capacity of the pipeline. Under this <br />concept, there would be no surcharging; however, vertical air venting pipes <br />would be needed at locations along the pipeline to balance the air pressure <br />in the system. This approach. is the safest, but it may also require the <br />largest pipe diameter. <br /> <br />c. ~"" c.apacity on slQpes greatl'r than flattest slQpe. Under this concept, <br />some of the flattest slopes would flow full, and some water would have to <br />back up into a steeper section above. Thus, some surcharging would <br /><lCCur; however, this could be acceptable as long as their locations are <br />known and the vent pipes are properly located. <br /> <br />3. Limitations on Analyses. <br /> <br />Since calculations were based on slopes measured off of a USGS map, all flow <br />analyses must be considered approximate. During fmal design, a profile of the <br />pipeline will be made using an on-site survey and pipe diameter calculations <br />made at that time could differ from those shown herein. As a safety factor, it <br />was decided to base the preliminary design of pipe diameter on the flattest <br />probable slope; i.e., one that did not create any surcharging. <br /> <br />4. Calculation and Cost Estimates. <br /> <br />Since both the calculation and COst tabulation are relatively involved, detailed <br />data for both is included in the Appendix (part .J2.J, rather than the main text. <br />Results are summarized under each Alternative Analysis Section. <br /> <br />5. Pipeline Si71!S Reqllired to Meet Demand - Non-Pressure Flow. <br /> <br />a. Demand Scenarios. As discussed in Section B, there are four demand <br />scenarios being considered as follows: <br /> <br />Normal Operation <br />Palisade alone <br />Palisade & Ute <br /> <br />- 3.3 MGD (Scenario A) <br />- 3.3 MGD + 0.5 MGD - 3.8 MGD (Scenario B) <br /> <br />EmergenGy Operation <br />Palisade & Ute - 3.3 MGD + 4.0 MGD = 7.3 MGD (Scenario C) <br />- 3.3 MGD + 10.0 MGD = 13.3 MGD (Scenario D) <br /> <br />V-12 <br />