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OSTP Basic Pump Selection Design ;,; <br /> likiiMinnesota Pollution Worksheet UNIVERSITY <br /> Control Agency OF MINNESOTA AS-S"." <br /> 1. PUMP CAPACITY Project ID: <br /> Pumping to Gravity or Pressure Distribution: 0 Gravity QQ Pressure Selection required <br /> 1. If pumping to gravity enter the gallon per minute of the pump: GPM (10-45 gpm) <br /> 2. If pumping to a pressurized distribution system: 38.0 GPM <br /> 3. Enter pump description: I <br /> -- <br /> tment <br /> stem. <br /> 2. HEAD REQUIREMENTS S&0ppointo discharge <br /> ht <br /> A. Elevation Difference 13 ft �- \'''q°5s,W N ttnc <br /> between pump and point of discharge: - <br /> nletpipe� ----- <br /> a Elevation <br /> B. Distribution Head Loss: 5 ft - differenceC. Additional Head Loss: ft(due to special equipment,etc.) I <br /> • <br /> _Table I.Friction Loss in Plastic Pipe per 100ft <br /> Distribution Head Loss Pi a Diameter(inches) <br /> Gravity Distribution = Oft Flow Rate P <br /> IGPMI 1 1.25 1.5 • 2 <br /> Pressure Distribution based on Minimum Average Head 10 9.1 3.1 1.3 0.3 <br /> Value on Pressure Distribution Worksheet: 12 I 12.8 4.3 1.8 1 0.4 <br /> Minimum Average Head Distribution Head Loss 14 17.0 5.7 2.4 I 0.6 <br /> 1ft 5ft 16 21.8 7.3 3.0 I 0.7 <br /> 2ft bft 18 9.1 3.8 I 0.9 <br /> 5ft 1 Oft 20 11.1 4.6 1.1 <br /> 25 16.8 6.9 1.7 <br /> D. 1.Supply Pipe Diameter: 2.0 in 30 23.5 9.7 2.4 <br /> 35 12.9 3.2 <br /> 2. Supply Pipe Length: 107 ft 40 16.5 4.1 <br /> E. Friction Loss in Plastic Pipe per 100ft from Table I: 45 20.5 5.0 <br /> 50 6.1 <br /> Friction Loss= 3.67 ft per 100ft of pipe 55 7.3 <br /> 60 8.6 <br /> F. Determine Equivalent Pipe Length from pump discharge to soil dispersal area discharge 65 I ' 10.0 <br /> point. Estimate by adding 25%to supply pipe length for fitting loss. Supply Pipe Length 70 11.4 <br /> (D.2) X 1.25=Equivalent Pipe Length 75 1 13.0 <br /> 85 107 ft X 1.25 = 133.8 ft 95 I I 20.� <br /> G. Calculate Supply Friction Loss by multiplying Friction Loss Per 100ft (Line E)by the Equivalent Pipe Length (Line F)and divide by 100. <br /> Supply Friction Loss= <br /> 3.67 ft per 100ft X 133.8 ft + 100 = 4.9 ft <br /> H. Total Head requirement is the sum of the Elevation Difference (Line A),the Distribution Head Loss (Line B),Additional Head Loss(Line C),and <br /> the Supply Friction Loss(Line G ) <br /> 13.0 ft + 5.0 ft + ft + 4.9 ft = 22.9 ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 38.0 GPM(Line 1 or Line 2)with at least 22.9 feet of total head. <br /> Comments: <br />