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i <br /> Pump Selection for a Pressurized System-Single Family Residence Project <br /> Humbug <br /> Parameters <br /> Discharge Assembly Size 1.25 inches 110 : I 1 1 i. . 1 1 1 1 , 1 1 • 1 i 1 i i 1 , i : ; I <br /> LengthI <br /> Transport Pipe C 20 feel -i_I i i _ -. --.-- , - <br /> Transport Pipe Class 40 + I Ii, • i : ' ; i i 1 f ; i <br /> Transport Line Size. 1.50 inches 100 I I I I I <br /> , <br /> Distributing Valve Model None 11 I ( ! j j ; i 1 1 ' 1 I 1 ! 1 ! I , 1 1 1 <br /> Max Elevation Lilt 15 feell i IYi 1 i j I j i i 1 i <br /> Mandold Length 16 feet I i i <br /> I • I i I I I ; <br /> Manifold Pipe Class 40 90 1 I I ! I i i •+ 11 <br /> Manifold Pipe Size 1.50 inches I I I 1 . ' 1 1 I_ 1 L-i <br /> 1 i <br /> Number of Laterals per Cell 5 11 1 j I i t 1 1 1 1 i ' i <br /> Lateral Length 28 feet 80 I I I ' I ' ! i 11 + - i I i + <br /> i f 1 i 1 .I 1 <br /> I I I <br /> Lateral Pipe Class 40 { I I I i j ! 1 1 I II 1 <br /> Lateral Pipe Size 1.50 inches I -�-�-I -) - I-• _ __._ <br /> Orifice Size 1/8 Inches 70 1 1 I r I 1 1 I 1 I I . 1 : i 1 I <br /> Orifice Spacing 2 feet tv Residual Head 5 feet X _I 1 1 I <br /> I 1- III <br /> i-._1_i_._J._ i L + - I_I 1 ! i_Lt._ <br /> Flow Meter None inches ! 1 ! III f + I i ; ; I : + i <br /> 'Add-on'Friction Losses 0 feet - 60 + \. <br /> co do <br /> 1111 ( 1 1 i_l_I 1 ' III 1 , : i `\ i I l ,: l <br /> Calculations x 11 1 ,—I i j - - <br /> 50 f ill I i t i l 1 1 1 1 , 1 I T M \ I i 1 , i <br /> Minimum Flow Rate per Orifice 0.43 gpmto <br /> 1 1 1 1 I j III <br /> I I I i l l 1 <br /> Number of Orifices per Zone 75 j� (__1-y 1 I I - I l i _1 i <br /> Total Flow Rate per Zone 32.5 gpm O 1 i I-j- I_T'-_i! _I I i 1 _I , ' <br /> Number of Laterals per Zone 5 3 40 ( I I i I i i i ! , , , <br /> Flow Differential lsut.as1 Orifice 0.3 °5 12 • 11 I 1 i i 1 l I I + I I I { 1 i• <br /> 1 i t <br /> Transport Velocity 5.1 fps l -1 I_ { t__'_ �_ _l_+_.i?-j--=-"-I-+ <br /> 1. li 1111 i111 j1i1 .flat l i i, . , <br /> Frictional Head Losses 30 — IfI _ <br /> Loss through Discharge 7.4 feel III <br /> �� 1 Ijf <br /> I I I ! I 11 f 1-• 11 1 11ti I I i 11 I • I !LossthroughValve 0.0 feet 20 1Loss In Manifold 0.3 feet + ' _ _ _ +1 I , i Li l { I I I II' i ' I <br /> Loss in Laterals 0.0 feet I I 1 <br /> Loss through Flowmeter 0.0 feel 10 I l I 1 i l 1 I l i t I 1 1 11-:-1-; <br /> 1 ! i i I I I ! . <br /> 'Add-on'Friction Losses 0.0 feet 1 I I i j . i <br /> 1 1_._!_ _i , 111 1 1_ ,.. 1 1 1 _1 _�_,_1� , 1 i_ i _I.- ! �_ <br /> Pipe Volumes I I I 11 -FM i I i I 1 1 I 1 I ! ; i l i 1 i ;_ <br /> Vol of Transport Line 2.1 gals 00 5 10 15 20 25 30 35 40 <br /> Vol of Manifold 1.7 gals Net Discharge(gpm) <br /> Vol of Laterals per Zone 14.8 gals <br /> Total Volume 18.6 gals <br /> Minimum Pump Requirements PumpData Legend <br /> Design Flow Rate 32.5 gpm P3005 HH Effluent System Curve: <br /> Pump Data <br /> Total Dynamic Head 28.9 feel P3005 High Hoad Effluent Pump <br /> 30 GPM 112HP Pump Curve:..._ <br /> 115V 10 <br /> Pump Optimal Range: <br /> — <br /> Operating Operating Point:`1 <br /> STATE CERfl . /f b <br /> edatt5t J Design Point O <br /> I Environmental Health Sp LL <br /> ,ror EH-S-i 0 06540 <br /> Loote0/ii- __:: .\ <br /> Robert G <br /> ood <br /> win <br /> 6 <br /> . <br />