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• <br /> Pump Selection for a Pressurized System•Single Family Residence Project <br /> Evergreen Plumbing f Advanlex to Shallow OraveNess D.P. . i'.'- <br /> 4 <br /> lee <br /> Parameters <br /> Discharge Assembly Size 1.25 inches • <br /> _ — — —' OrenCO <br /> Transport PipeLengthC 40 teat �_ <br /> Transport Pipe Glass 40 <br /> • Transport Line Size 1.25 inches T„ — _ <br /> • Distributing Valve Model None <br /> . Max Elevation Litt 10 feet --.,-• -. -.- <br /> Manifold Length 20 feet <br /> • Manifold Pipe Claw 40 250 --• <br /> .� <br /> • Manifold Pipe Size 1.00 i thes E IC L`, _ `J "1 <br /> • Number of Laterals per Cell 3 — W , '—' `J <br /> Lateral Length 41.5 feat _ _ <br /> • Enteral Pipe bless 40 1 , 1 , , „ - I. DEC 1 102`I <br /> • Lateral Pipe size 1.00 inches <br /> • <br /> • <br /> Orifice Size 1r8 irlrhes <br /> Orifice SOWN! 2 feel -- . Mi'�PSON COUNTY <br /> . Residual Head 5 feetIll <br /> Flow Meter None Inches 200 ' il.-�il\!C� INSPECTION ' <br /> . 'Add-on'Friction Losses 0 feet U <br /> Calculations ' ,I -II , ' <br /> Minimum Flow Nate per Orifice 0.43 gpm <br /> • Number of Orifices per Zone 63 <br /> • <br /> Thief Flow Rate perZone 27.7 N gpm <br /> • <br /> Number of Laterals per zone 3 I r F <br /> • <br /> • <br /> • Flow Differential 1s:Lasi Orifice f1.3 1ao • (ATE CERTIFIED <br /> Transport Velocity 5.9 fps u <br /> E I nvironmental Health Specialist <br /> Frictional Head Losses - - - zp " J2O ' <br /> 'I� -i 40 <br /> i Loss through Discharge 5A flint I PF20in y l <br /> '� <br /> Loss In Transport 1.9 feel 4 I <br /> • <br /> • k <br /> Loss through Valve 0.0 feel _• Loss in Manifold 2.0 teat <br /> • <br /> 1_ Robert Goodwin <br /> Loss In Laterals 0.7 tenet 100 ~mm9 <br /> • Loss through Flowmoler 0.0 fee / <br /> 'Add-on'Friction Losses 0.0 feet _— — — — `�(�'� <br /> - - 1 _ �. 1 ` <br /> Pipe Volumes __ 1 1_101Val of Transport Une 1.6 gelsVol of Manifeld 0.9 gale — — <br /> Vol of Laterals per Zona 5,6 eats I <br /> Ill <br /> I — <br /> • Total Volume 8.0 gals 50 <br /> _ BYjle�n Curve: <br /> . Minimum Pump Re uirements i <br /> Design Flow Rale 27.7 gam II <br /> 111111 1 1 �"�.. �_�� w� <br /> IIIPump Own. <br /> Total Dynamic Heed 25.1 feel 1 1 1 � 1!,!!; ■.. I h Pump OFisrOK1ngx - <br /> -I01 11 •��� fie• 11___H_ opuasmgpaPl �+ <br /> MIII <br /> • 0u13n Riot a <br /> e0 5 to , 15 20 25 10 30 So <br /> Net Discharge(gpm) <br />