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�.,Y..��a u,x.�. Pump Selection Design � Minnesota Pollution W��-k$heet � Control A enc �,.'-•�'y;- Equivalent Length Factors(ft.)for PVG Pipe 10. Equivalent length of pipe fittings. Fittings Section 9 is for Collection Systems ONLY and dces NOT need to be Pipe Diameter(in.) comp/eted for individual subsurface sewage treatment systems. Fitting Type �� 2 3 Quanity X Equivalent Length Factor=Equivalent Length Gate vatve 1.07 1.38 2.04 90 Deg Elbaw 4.03 5.17 7.67 45 Deg Elbow 2.15 2.76 4.09 Fittin T Equivalent Equivalent g ype Quantity Length Fador Length(ft) � g�a�Thra,y g.p5 0430 5 30 X Swing Check Vatve 73.40 17.20 25,50 Gate Valve - Angle valve 20.10 25.80 38.40 90 Deg Etbow X = Globe Valve 45.60 58.60 86.gp Butterfly Valve - 7.75 17.50 45 Deg Elbow X = Tee-Flow Thru X = Tee-Branch F(ow X - NOTE: Equivatent tength values for PVC pipe X = fittings are based on calcutations using the Hazen- Swing Check Valve Williams Equation. See Advanced Designs for SSfS Mgle Vatve X = for equation. Other pipe materiat may require different equivatent length factors. Verify other Globe Valve X - equivalent length factors with pipe material X manufacturer. Butterfly Valve = Valve 10 X = NOTE:System installer should contact system designer if the number of fittings varies from the Valve 11 X = design to the adual installation. A. Sum of Equivalent Length due to pipe fittings: ��ft B. Total Pipe Length =Supply Pipe Length(5.6)+Equivalent Pipe Length(9.A.) Hazen-Williams E uation for h �� ft + �� ft - ��ft 1�.5 *L *��-C)1.852 Qingpm hf T1 4.8655 L in feet C. Hazen-Williams friction loss due to pipe fittings and supply pipe(h): 1l D in inches 10.5 X Total Pipe Length (9.B) X (Ftow Rate =Constant)'��Z - Pipe Diameter°��ss 10.5 X ��ft X (��9Pm = 130)�esz _ ��ft4.8655 _ �ft l�.�l �1• Total Head requirement is the sum of the Etevation Difference (Line 3),the Distribution Head Loss(Line 4),Additional Head Loss(Line 5), and either Supply Friction Loss(Line 9),or Friction Loss from the Supply Pipe and Pipe Fittings for collection systems(Line tO.C} NOTE:Supp/y Friction Loss(Line 8)need ONLY be used if NOT a co(lection system. NOTE:Friction Loss from the Supply Pipe and Pipe Fittings(Line 9.C)need ONLY be used if system is a coUection system. 10.0 fc + 5.0 rc + C�rc + 1.3 ft = 16.3 fc 3. PUMP SELECTION A pump must be setected to deliver at least Z9 GPM(Line 1 or Line 2)with at least �7 feet of totat head. I hereby certify that i have completed this work in accordance with all applicable ordinances,rules and laws. Joseph J Olson 810 08/10/09 (Designer) (Signature) (License#) (Date)