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Design Requirements for Sewage Pumping Stations - The City of ...

Design Requirements for Sewage Pumping Stations - The City of ...

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<strong>City</strong> <strong>of</strong> Wentzville, MissouriEngineering <strong>Design</strong> Criteriad. Total Dynamic Head1) Static Head (H S )E h = Maximum <strong>for</strong>ce main elevationE 1 = Wet well low water elevation (Pump Off)H S (feet) = E h - E 12) Loss (L f ) due to friction in <strong>for</strong>ce mainLength = Total equivalent length <strong>of</strong> <strong>for</strong>ce main (feet)L f (feet) = Length x Friction Factor3) Loss (L s ) from friction in the station pipingLength = Equivalent length <strong>of</strong> station piping (feet)L s (feet) = Length x Friction Factor4) To Calculate the Friction Factors, use the Hazen andWilliams <strong>for</strong>mula with the following c-Factors:For the design pump operating point:Unlined iron or steel pipe: C=100All other pipe (including Plastic and lined DIP) C=120To insure pump motor does not overload after initialinstallation:Plastic Pipe and lined DIP C=150All other pipe C=140<strong>The</strong> operating point on submersible pump stations willbe evaluated at low water cut<strong>of</strong>f.Friction head loss per 100’ pipe:= 0.2083 x (100/C) 1.85 x Q 1.85 / d 4.86555) TDH (feet) = H s + L f + L sPlot a worst case TDH curve, using the lower C valuesabove, and a best case TDH curve, using the higher Cvalues above, on a manufacturer’s pump per<strong>for</strong>mancecurve sheet.<strong>The</strong> Constant Speed Rating (CSR) or the pump’soperating point is the point where the worst case TDHand the pump manufacturer’s pump per<strong>for</strong>mance curveintersect.Find where the best case TDH and the pumpmanufacturer’s pump per<strong>for</strong>mance curves intersect andcheck the pump is not in an overload condition.4 - 3 Approved 6/10/09

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