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Woodhill Avenue
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1245 Woodhill Avenue - 02-117-23-24-0012
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Last modified
8/22/2023 4:07:47 PM
Creation date
2/25/2020 8:07:29 AM
Metadata
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Template:
x Address Old
House Number
1245
Street Name
Woodhill
Street Type
Avenue
Address
1245 Woodhill Ave
Document Type
Septic
PIN
0211723240012
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" ', . ' FUMP SELEC1'.tON• 'R©LtiA/RB , <br /> • <br /> L. Determine pump capacity: ' <br /> k. Gravity disttibufion . • • <br /> •• <br /> 1. Minimum required discharge is 10 gpn • <br /> . <br /> M <br /> 2. axisnw�n suggested'dischar.g ;45,gpm. For other <br /> . establishments at least 10%ge is regter tilt=the water supply rate, <br /> • <br /> but ncitaster than the rate at which efflhent will flow out of the • <br /> diditi'bution device.• . . , . .• <br /> . Pressure distribution . - <br /> See pressure.distribution work sheet <br /> rom'A or B Selecfed'pump.capacitp: y 0'• gpm • <br /> • <br /> Determine pump'head•requirements: , . • <br /> Elevation difference between pump and point of discharge? ' • • soil treatment syst <br /> &p•I • •Ischar <br /> /0 feet o:k.9.-.1.kd;,.. 0 <br /> Special head requirement?(See Figure at right-Special Head Requirements) , total •Ipe <br /> Tenet <br /> 5 feet • 2A.elevation <br /> • ' Inlet i,""'''"""'"'"''„ ' '" difference <br /> Calculate Friction loss . pipe. � • <br /> 1. Select pipe diameter Z •• 111111K1,1111 <br /> re o2. Enter Figure E-9 with gpm(7A o•r B)aiid pipe diameter(• C1) ••.-�~' ^""'•' <br /> Read friction loss lrrfeet per 100feet from FigureE-9" • ' ' . Special Head Requirements <br /> Friction Loss = 3, - / ,ft/• .00ft of pipe ' • •. Gravity Distribution 0 ft <br /> 3. Determine total pipe length from pump dscharge to soil treatment ,Pressure DlstrIb,itlon 5 ft <br /> discharge point.Estimate by adding 25.percent to pipe length•for '• <br /> fitting loss. Total pipe length times 1.25:equivalent pipe length -9• Friction Loss in Plastic Pipe - <br /> ( '0• feet x 1.25 : ' feet • • • . • Per 100 feet <br /> . Calculate total friction loss by multiplying friction loss (C2)' •' Hominy! <br /> in•ft/100 ft by.the equivalent pipe!length(C3)•and divide by 100. pIpe diameter <br /> 3.Z-- ft/,100ft x, 1 S . +100= ft flow rat. 1.5" 2" 3" <br /> ;pm <br /> Total head required is the.sum of elevation difference(A),special" 20 ' 2.47 . 0.73 • 0.11 <br /> head requirepnents.(13),and total friction Ioss (C4) 25 . , 373 1.11 0.16 <br /> 10• ft+ 5' . Z ft- . . , 30 5.23 1.55 0,23 • <br /> 19 '�eet 35 6.96 2.06 0.30 <br /> Total head: � <br /> 40 • 8,91 2.64 0,39 <br /> 'ulzlp selection45 50 11.07 3,28 0.48 <br /> 13.46 3.99 0.58 <br /> 55 4.76 0.70 <br /> .pump must be selected to deliver at least . 4 r) ' •gpm 60 5.60 0.82 <br /> :A or B) with at least_.LZ.,_feet of total head(2D) • ' 65 6.48 0.95 <br /> 70 7.44 • 1.09 <br /> ereby certify that I ve completed this work in accordance with applicable ordinances,,rules and laws. <br />
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