My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
1999-011223 - sewer & water - septic
Orono
>
Property Files
>
Street Address
>
B
>
Big Island
>
290 Big Island - PID: 23-117-23-32-0059
>
Septic
>
1999-011223 - sewer & water - septic
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
8/22/2023 4:13:24 PM
Creation date
4/18/2016 1:25:48 PM
Metadata
Fields
Template:
x Address Old
House Number
290
Street Name
Big Island
Address
290 Big Island
Document Type
Septic
PIN
2311723320059
Supplemental fields
ProcessedPID
Updated
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
20
PDF
Print
Pages to print
Enter page numbers and/or page ranges separated by commas. For example, 1,3,5-12.
After downloading, print the document using a PDF reader (e.g. Adobe Reader).
View images
View plain text
PUMP SELECTION PROCEDURE <br /> A. Determine pump capacity: <br /> Gravity Distribudon <br /> 1. Minimum suggested is 20 gpm <br /> 2. Maximum suggested is 45 gpm Perfontion Discharges in GPM <br /> Head Perforation diameter ' <br /> Pressure Distibution Eeet inches <br /> 3. a. Select number of perforated lateraLs . �/32 1/a <br /> b. Select perforation spacing= feet. . 1.Oa o.56 0.74 <br /> c. Subtract 2 ft. from the rock.layer length. ls 0.69 0.90 <br /> Rxk laya�en�th <br /> -2 ft.= feet. . 2ob o.so i.o� <br /> d. Determine the number of spaces between perforations. a Use 1.0 foot single homes. <br /> Length perf.spacing= ft.+ ft.= spaces b Use 20 feet for anything eLse. <br /> e. spaces+1 = � perforations/lateral <br /> f. Multiply perforations per lateral by number of laterals to <br /> get total number of perforations. y�s x .�= perforations. <br /> g. � x �T�= gpm. <br /> SELECTED PUMP CAPACTTY � gpm <br /> B.Determine head requirements: <br /> 1. Elevation difference between ump and point of dischazge. <br /> ��, feet <br /> 2. If pumping to a pressure distribution system,five feet for pressure � �°`'`�"a""`s`�""' <br /> required at manifold if gravity system,zero. °"'"``�°' <br /> _��feet T°nl p'p�1°`�t!' <br /> 3. Friction loss <br /> a. Enter friction loss table with gpm and pipe diameter. �N„o„�� <br /> Read friction loss in feet per 100 feet from table(F-14). �'�' <br /> F.L.= I 5 5 ft./100 ft of pipe ._ <br /> b. Determine total pipe length from pump to discharge� ._._ _ ------------------------------------- <br /> point. Estimate by adding 25 percent to pipe length for fitting <br /> loss,or use a fitting loss chart(F-15 feet). <br /> Equivalent pipe length-1.25 times pi�e length= � <br /> �.S- x 1.25= 9 `� feet Friction Loss in Plastic Pipe <br /> c Calculate total friction loss by multiplying <br /> friction loss in ft/100 ft by equivalent pipe length. Nominal <br /> Total friction loss= I� S r x + � pipe dia. <br /> �_ 100= feet Flow Rate <br /> 4. Total head re quired is the sum of elevation difference, �m 1.5" 2" 3" <br /> special head requirements,and total friction loss. <br /> 20 2.47 0.73 0.11 <br /> �+ a + � 25 3.73 0.16 <br /> (1) (2) (3c) 30 5.23 1.55 0.23 <br /> 35 6.96 2 6 0.30 <br /> 40 8.91 264 0.39 <br /> TOTAL HEAD /�_feet 45 11.07 3.28 0.48 <br /> 50 13.46 3.99 0.58 <br /> C, Pump selection 60 5 bo o s2 <br /> 65 6.48 0.95 <br /> 70 7.44 1.09 <br /> 1. A pump must be selected to deliver at least <br /> 3v gpm (Step A) with at least �_feet of total hea�i (Step B). <br />
The URL can be used to link to this page
Your browser does not support the video tag.