bpump
Transcript of bpump
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2001 Goulds PumpsEffective August, 2001 www.goulds.com
ResidentialPump Fundamentals
Goulds Pumps and the ITT Engineered Blocks symbol areregistered trademarks and tradenames of ITT Industries.
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Sources of WaterA source of water or a well is often referred to as shallow or deep.These terms are referring to the depth of the water source or well.
A shallow well is one where the water is within 2 feet of the ground
surface. A deep well is where the static water level is more than 2 feet
down.
The standing water level in a well is called the static level. This is thewater level when the pump is not operating. !hen the pump comes on
and is running there often is a change in the water level. This is referredto as drawdown. The drawdown occurs and the water level reacheswhat is referred to as the pumping level. This is the operating level ofthe pump. The lowest level to which the water will drop is the level fromwhich it must "e pumped.
#riven !ell #rilled !ell #ug !ell $istern %pring, &a'e, or
%urface !ater
2 ft.
A Shallow Well(s an) source of water where the water is within 2 feet of ground level. !hen water is pumped from a well the
water level will draw down. The lowest level to which it will drop is the level from which it must "e pumped.
#riven !ell #rilled !ell #ug !ell
2 ft.
Draw
Down
Static Level
PumpingLevel
A Deep Well(s an) source of water where the low water level is more than 2 feet "elow the ground level.
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Pump
*
Typical Jet Pump Installations
SHALLOWWLL S!ST"
TWI# PIPDPWLLS!ST"
PA$%&DPWLLS!ST"
+se chec'valve hereor foot valveat end ofsuction pipe.
Shallow Well Jet Pump(n a shallow well et s)stem,
the et assem"l) is fastened
to the outside of the centrifu-
gal pump as illustrated. r
the et assem"l) can "e "uiltinto the centrifugal pumpcasing.
(n either case there is onl)
one pipe e/tending into the
well or source of water
the suction pipe.
Deep Well Jet PumpA deep well et s)stem is
"asicall) the same as a
shallow well s)stem withone maor difference
the et assem"l) is
separate from the
centrifugal pump,located in the well,
usuall) "elow the
pumping level of the
water, and piped to the
centrifugal pump withtwo pipes. A suctionpipe and a pressure ordrive water pipe.
AW '(ADAPT&
Typical )oul*s Jet Pump Installations
(+PIPPITLSSADAPT&
O,& TH WLL
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Pump Types
Typical Su-mersi-le Pump Installation
Goulds Pumps
Goulds 3su"mersi"lepump with alightning
protectedmotor. Twoorthree wiremodelsavaila"le.
Pressure Tan.ffers water storage forfewer pump c)cles.Provides air cushion tooperate against. Tan'should "e si4ed so thatdraw down is e5ual tocapacit) of pump.
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The / 0asic
1uestions
2 $apacity #ee*e*6ow "ig must the pump "e7
( Well $on*itions(s a shallow or deep well pump needed7
/ Discharge $on*itions6ow much pressure is needed7
The illustration a"ove poses a t)pical water s)stem pro"lem. The source of water is in nearl)all cases lower than the house or "uilding. This is wh) a pump is needed to raise the waterup
to the faucets and fi/tures. These are the three 5uestions to "e considered
2 $apacity #ee*e*6ow much water in gallons per hour or gallons per minute are needed7 This determines what si4e pump to use.
( Well $on*itions!hat is the total suction lift7 !hat is meant ") 8total suction97 !e learn from this what to e/pect from a
shallow well pump and when and wh) to use a deep well pump.
/ Discharge $on*itions6ow much pressure is needed at the pump7 6ow much pressure will result at the faucet7
!henever and wherever a pump is to "e used, the correct answers to these three 5uestions will tell the actual
pumping conditions or specificall) what is re5uired of the pump. !ith this information, )ou can alwa)sselect the right pump from the catalog.
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2 $apacity #ee*e*6ow much water is availa"le76ow much water is needed76ow large must the pump "e7
Limiting 3actors
6ow much water is
availa"le7 :efore we
select a pump "ased on
need we must determineif the suppl) is ade5uate.
;an) areas have what werefer to as low )ield wells,
!ell recover) rates ma) "e
as low as 1 GP; or less.
A t)pical low )ield
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2*?
Piping'itchen sin' to showerhead e5uivalent length 20?
Pipingpump tan' to 'itchensin', e5uivalentlength *0?
%taticwater level,pump notrunning
Pumpingwater level,pumprunning
Deman*
10?
*0?
20?
availa"le is used and
man) users are dissatisfied
with the results. The)eithercant ta'e a shower or fill a
tu" while sprin'ling the
lawn, or if a toilet is
flushed when ta'ing a
shower, the showerdiminishes to a dri""le, or
some similar interruption
occurs. The trou"le of
course is that the
The rate of flow from a
faucet or fi/ture dependson its t)pe and si4e, the
length and si4e of pipesuppl)ing it and the
difference in elevation
"etween it and the pumpor tan'. >urthermore,it is
impossi"le to determine ")sight the e/act rate of flow"eing delivered from a
This of course is not
alwa)s practical. Thecapacit) of pumpschanges with pumpingconditions such as
pumping level of the water
and the operating
pressure.Accordingl), it is
good practice to provide apump capacit) for the
average home of from 10
to 12 gpm when availa"le.
The capacit) re5uired ofthe pump is determined ")the num"er of continu-
ousl) flowing demands
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%hower in usesame time as'itchen sin'faucet on.
2 continuous uses re5uire G.P.;.minimumThe capacit) re5uired ofthe pump is determined ") the num"er of continuous useoutlets in use at the same time. Jou can?t use water at one or a num"er of outletsan) faster than the pump supplies it.
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( Well $on*itions
The level of the water to
"e pumped is practicall)
alwa)s "elow ground. (t
can "e onl) a few feet
as in a spring, shallow
well, pond, etc., or it can
"e man) feet as in a
deep well. (f we could
alwa)s locate thepumping mechanism in
the water, as we do with
su"mers- i"le pumps, our
pro"lem
e5ual to a"out 1.B l"s.
per s5uare inch at sea
level. !hen the pressure
of atmosphere is removed
from inside of a pump the
resulting condition is a
vacuum or partial
vacuum. (t is also called
suction.
The vacuum or suction
cham"er of a pump is
piped irst, lets consider terms
of measurement and theirrelation to each other.
Pressure is usuall) e/-
pressed in pounds pers5uare inch romthis we can
(;A7
,&TI$AL LI3TPL
,acuum)auge a"ove sea level. The total
suction lift would onl) "e2L.@ ft. not **.@ ft. li'e at
sea level.
1. The atmosphere allaround us has weight and
therefore e/erts pressure
AtmosphericPressure
AtmosphericPressure
2'78 L0S7
Water Level
Tr) to lift soda from a "ottle ")closing )our mouth over themouth of the "ottle. (t cant "edone. !hen )ou use a straw, itis eas) 0 )ou are creating apartial vacuum in )our mouth,e/posing the surface li5uid toatmospheric pressure, thedifference in pressure raises the
li5uid.
A reading of 203 on a vacuum
gauge placed on a suction sideof the pump would tell )outhat)ou had a vacuum orsuction lift of 22. ft.
203 / 1.1*? K 22. ft.
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TTA& &EIGT6 > %+$T(I P(PE (% 100 $APA$T(J > P+;P (%B GA&&I% PEM ;(I+TE
B ft.%TAT($ &EDE& > !ATEM
2* ft. DEMT($A& &(>T !ATEM
>M($T(I > B GP;(I 100 >T. > P(PE 13 K *.? 11/3K .@*?
TTA& %+$T(I &(>TK 2.? . . . . . . . . . 2?
:D(+%&J 11/3P(PE ;+%T :E +%E#.
Summing this up5 !henthe atmospheric pressureis1.B l"s. per s5. inch aperfect vacuumshould "e *0 inches andthis would lift water ")suctionto a height of **.@ ft.
;ost shallow well or suctionpumps are capa"le ofdeveloping a near perfectvacuum, and at sea levelthe) can lift water a"outthirt) feet. 6owever,suctionlifts of more than 2 ft.at sea level are notrecom-mended. %hallow welletpumps deliver inade5uatecapacit) on lifts over 2ft.
%uction conditions, ortotalsuction lift must include all
resistances to the flow of thewater through the suctionpipe up to the pump. 6eightor vertical lift is one resis-tance. >riction"etween thewater and the pipe walls isthe other resistance.
waste the least possi"leamount of wor'. Neepin mind that all wor'"eing done on thesuction side of the pumpis actuall)performed ") thepressure of atmosphere.%ince in
common practice weconsider this pressureissufficient to overcome onl)2 ft., the 2 ft. mustalwa)s include an) lossesdue tofriction.
!e dont have to "e tooconcerned with how or wh)friction loss is incurred, "ut itis essential that we accept itas occurring alwa)s whenwater flows through pipes. (tis, also, most essential thatwe understand how it ismeasured.(n our discussion of suctionlift, atmospheric pressureand the height thispressure will raise water,we esta"- lished the factthat 1.B l".
pressure will raise water to aheight of **.@ ft.Althoughthere is no relation "etweenatmospheric pressure andfriction loss, the relation"etween pounds pressureand feet elevation or headas we call it, is thesame whether the
pressure iscoming from atmosphere oran) other source. %o, asstated "efore, 1.B l"s.pressure from an) sourcewill raise water **.@ ft. andthis gives us the conversionfactor to change our termsfrom pressure to feet or thereverse of this. Therefore,1 l". of pressure is alwa)se5ual to 2.*1 ft.
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/ Discharge$on*itions
!hat are the conditionsunder which the waters)stem must discharge itscapacit)7
The capacit) of thepump has alread) "eenesta"- lished so we arenow concerned onl) withthe
!ould )ou rather haveat a faucet one gallonper minute at a hundredpounds pressure or tengallons per minute at tenpounds pressure7 !hichwill fill a tu" 5uic'er7
100 10
friction loss in feetcalculated and changed topounds pressure M($T(I &%%7
E&EDAT(I7
some e/planation is inorder. Ouite often it isstated that a particularpump is delivering suffi-cient capacit) "ut failsto
develop ade5uatepressure. (n most cases thisis a misstatement and theopposite condition is true.This complaint is generall)made when a particulars)stem fails to providesufficient flow throughseveral outlets at thesame
Iow as to the resistance toflow which will "e encoun-tered, there are threecauses. These are rictionPump capacit) is B gpmThis flow through 200 ft.of 13 pipe gives a frictionloss of *.0 l"s. .................. * l"s.
*0P%(
2*?
time. This is caused in mostcases ") the demand inrate of flow "eing greaterthan the capacit) of the
s)stem. (f the s)stem hassufficient capacit) to suppl)the ma/imum num"er ofoutlets which are li'el) to"e used at the sametime,our onl) concern withpressure is that wehave sufficient pressureto
overcome the resistanceto flow which will "eencountered. (f )ou havean) dou"ts a"out this,
consider )our answer
to this 5uestion installed at the house, andthe standard pressurerange of the s)stem issufficient to overcome
these resistances anddeliver its capacit) to thevarious outlets. An e/amplein which these computa-tions must "e made iswhen the pump or s)stemis located at considera"ledistance from the point ofuse and on a lowerelevation.
(n such a case the differ-ence in elevation must "edetermined
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200? 13 P(PE E&ED AT(I
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Jet SystemsThe first 5uestion with Cet Pumps is what is the suction
cham"er and how is the vacuum created.
The Cet Assem"l) itself forms the suction cham"er andthe vacuum is created ") the ver) high velocit) of a
stream of water passing through the et. :asicall), theetassem"l) is composed of two parts. >irst, a no44le which
produces the high velocit) stream of water. This highvelocit) stream of water is inected through a small
compartment which is the suction cham"er, there")causing the vacuum. "viousl), the suction pipe is
connected to this compartment or suction cham"er. Thevacuum caused ") the et permits the greater pressure ofatmosphere on the surface of a "od) of water to force
water into the suction cham"er.
The second "asic part of the Cet Assem"l) is the venturi
tu"e. (t is installed in the discharge of the suction
cham"er. (ts function is to convert the velocit) of the
water into pressure. This is accomplished ") the shape
of its water passage. Perhaps )ou can "est visuali4e this") thin'ing of a no44le in reverse. The no44le speeds up
the flow of the drive water converting pressure into
velocit) and when it has passed through the suction
cham"er,the venturi slows it down again converting the velocit)
"ac' into pressure.
8#rive water9 is that water which is piped under pres-
sure to the et assem"l) or suction cham"er. The dis-
charge from the suction cham"er or et assem"l) is
composed of "oth the drive water and that water
pumped from the well. The total amount pumped fromthe well can "e used as discharge from the s)stem and
is the output or capacit).
Shallow Well Jet Pump>romthe foregoing discussion it is o"vious that theoperation of the Cet s)stem is dependent on the com-
"ined functions of "oth the Cet Assem"l) or suctioncham"er and the centrifugal pump. Also, that these twomain components of the s)stem are entirel) separate
and their locations with respect to each other is a
matter of design.
Types of Pumps
(n shallow well et pumps the et assem"l) is "uilt intothe pump casing as in the Goulds Pumps C%. r, the
et assem"l), shallow well adapters, can "e "olted tothe centrifugal pump. (n either case there is onl) one
pipe e/tending into the well . . . the suction pipe.Deep Well Jet PumpThe onl) "asic or fundamental difference "etween
%hallow !ell and #eep !ell Cet Pumps is the location of
the CetAssem"l). (t must alwa)s "e located in such a
position that the total suction lift "etween it and thepumping level of the water to "e pumped does note/ceed that which can "e overcome ") the pressure of
atmosphere. This, ofcourse, means that when this pumping level is at a
distance lower than the ground level which cannot "eovercome ") atmospheric pressure, the Cet Assem"l) must
"e located at least five feet "elow the low water in thewell.
!e must have a closed compartment in which to installthe no44le and the venturi and to form the suction
cham"er. This part is called the et "od). (ts shape is suchthat it will fit into the casing of a drilled well and the pipe
connections
are located for accessi"ilit). There are two on the top side,
one for connection to the pressure pipe which supplies the
drive water, the other for connection to the suction pipe
which returns "oth the drive water and the water pumped
from the well. >orthis reason, this connection is one pipe
si4e larger than that for the pressure pipe. !ater from the
well enters through a third opening which is on the"ottom side of the et "od).
The last accessor) for the Cet %)stem is the pressure
control valve. (t is a valve installed in the discharge pipingfrom the centrifugal pump "etween the pump and the
tan' in the pump when the pump is mounted on a tan'.
+sed onl) in deep well s)stems, its purpose it to assure a
minimum operating pressure for theet.
Pressure$ontrolDalve
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I
o4
4
l
e
Denturi
TwinPipe#eep !ellCet Assem"l)
>oot Dalve
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Su-mersi-le Pump%u"mersi"le pumps are so named "ecause the whole
unit, pump and motor is designed to "e operated underwater. This means the pump does not have to "e primed.nce installed and turned on, water flows up the pipe.
The pump end is a multistage
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Accessories
!hen appl)ing a pump to an) specific pro"lem pertain-
ing to domestic water suppl), our o"ective in practicall)
ever) case should "e to provide automatic runningwater under pressure a water service compara"le to
that which might "e e/pected from connection to a cit)
water main. :ut, a pump alone can hardl) perform the
several necessar) functions. $ertain other accessories are
necessar), and the com"ination of them all forms what
we call a water s)stem.
alwa)s "e considered. The larger a motor is in horse-
power the more starting power re5uired therefore, the
less fre5uentl) it should "e started.
(t is good practice to si4e the tan' to re5uire the pumpto run at least one minute per c)cle when using frac-tional horsepower motors and two to three minutes forlarger motors.
There are three "asic t)pes of tan's in use toda).
"otorsThe first accessor) is the drive medium which on practi-
call) all water s)stems of toda) is an electric motor.
Jou should remem"er that some of our pumps, in
particular
A(M D&+;E$ITM&
A(M
!ATEM
$onventional or )alvaniBe* Type
Me5uires an air volume control device
to 'eep proper amount of air cushion
in the tan'.
theetpumpsinlarge motorsi4esandsu"mersi"le pumps, are furnished with motors of current characteris-
tics as specified. Therefore, when ordering these, we
must"e advised the electrical characteristics.
Pressure Switch
The ne/t accessor) re5uired is a pressure switch to startand stop the motor automaticall) at a predetermined
pressure.A tu"e connects the switch to some point inthe s)stem on the discharge side of the pump. The
pressure in the s)stem then acts directl) on a diaphragm
in the switch which in turn actuates the contacts in the
>&AT(IG#(%$
#(AP6MAG;
A(M
!ATEM
A(M
!ATEM
A(M DA&DE
3loating Disc Type
#isc helps in preventing water froma"sor"ing air "ut is not a"solute. (t
re5uires periodic replenishment of air
through air valve.
Seale* Diaphragm Type !aterand air are permanentl) separated
") sealed diaphragm therefore,
the amount of air never changes.
The amount of draw-off alsonever
changes.
switch.
Pressure Tan.sThe rate at which water can "e used in a home, school,
motel, or an) other place can "e as little as one gallon a
minute
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Summary
Iow lets summari4e
"riefl)the points weEve
covered. !e have shown
that in a water s)stem
application, there are three
factors to consider
1. !ater Ieeded or #eter-mination of $apacit)
2. %uction $onditions, and
*. #ischarge $onditions.
!e have concluded thatcapacit) re5uired is deter-
mined ") the ma/imum
num"er of outlets which
will "e in continuous use
at the same time with a
minimum flow of three
gallons per minute peroutlet.
!e have shown that allet
pumps, whether shallowwell or deep well, have a
water end in which there is
a suction cham"er that the
suction cham"er is actuall)
a closed container in which
a partial vacuum is created.
This allows atmosphericpressure to force in the
water. The suction cham"ermust "e located withina"out 2 feet verticaldistance a"ove the pump-
ing level of the water.
The main difference
"etween shallow well anddeep well pumps is that in
the former the water end is"uilt onto the power end.
The water end of deep well
et pumps is a separate
part. (t is installed in the
water and is used to pumpwater from levels "elow a
2 feet depth. !e have
shown that a su"mersi"le
should "e used when
source will allow. %ince the
su"mersi"le is su"merged
in water onl) dischargeconditions appl). !eve
esta"lished three distinctforms of resistance to flowencountered as #ischarge$onditions and shown thatthe) must "e considered"ut computed onl) in
special cases.Also, that the
pump is onl) part of the
s)stem necessar) to
provide an automatic
service. ther accessoriesare necessar) and weEveesta"lished the need and
function of each of these
accessories.
!e have mentioned *GP; as a minimum
accepta"le flow rate peroutlet. :ut a larger flow
rate is more desira"le and
the following ta"le should"e used as an average
suppl) re5uired when the
source of suppl) will allow
it.
!e would li'e to leave )ouwith one thought. That is,
capacit) and pressure areinversel) related. !hen one
goes up, the other goesdown. Alwa)s chec' the
rating chart or curve of apump to ma'e sure if )ou
raise the pressure )ou willstill receive the needed
suppl) of water at )ouroutlets.
+sing the rating chart
"elow, we would "e
getting L GP; from the
pump at 20 l"s. pressure.
(f we were tr)ing to
suppl) two outlets atonce, this would give us
appro/imatel) GP; at
each one. (f we increasethe pressure to *0 l"s.
pressure, we onl) get
GP; which will give us
appro/imatel) * GP; ateach outlet. :) raising the
pressure we have reduced
the amount of water ateach outlet ") appro/i-
matel) 2Q.
Alwa)s chec' the pumpperformance rating
"efore ma'ing a change.Performance &ating in
)allons per"inute
Seven "inute Pea. Deman* Perio* arm,irrigation and sprin'ling re5uirements are not shown. These values must"e added to the pea' demand figures if usage will occur during normal demand periods.
Pump Discharge Pressure
TotalSuctionLift
(; PSI /; PSI"a47Shut+Offin L-s7
feetL
GP;
GP;1 l"s.
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1uestions C
Answers
1. !hat well conditions might possi"l) limit the
capacit) of the pump7
2. 6ow does the diameter of a cased deep well and
pumping level of the water affect the capacit)7
*. (f there are no limiting factors, how is capacit)
determined7
. !hat is suction7
. !hat is atmospheric pressure7
. 6ow much is the pressure due to atmosphere7
B. !hat is ma/imum theoretical suction lift7
L. 6ow does friction loss affect suction conditions7
@. !hen and wh) do we use a deep well et pump7
Mate of flow from the source of suppl), the diameter ofa cased deep well and the pumping level of the water ina cased deep well.
&imits the si4e pumping e5uipment which can"e used.
;a/imum num"er of outlets or faucets li'el) to "e in
use at the same time.
A partial vacuum created in suction cham"er of pumpo"tained ") removing pressure due to atmosphere,
there") allowing greater pressure outside to forcesomething romthis, we o"tain the conversion factorof 1 l". per s5. in. of pressure e5uals 2.*1 ft. head.
The resistance of the suction pipe walls to the flow ofwater uses up part of the wor' which can "e done ")
atmospheric pressure. Therefore, the amount of loss dueto friction in the suction pipe must "e added to the
vertical elevation which must "e overcome and the total
of the two must not e/ceed 2 feet sea level. This 2feet must "e reduced 1 foot for ever) 1,000 feet eleva-
tion a"ove sea level which corrects for a lessened
atmospheric pressure with increased elevation.
!hen the water level is more than 2 feet "elow the
pump "ecause this is the ma/imum practical suctionlift which can "e o"tained with a shallow well pump atsea level.
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10. !hat do we mean ") water s)stem7
11. !hat is the purpose of a foot valve7
12. Iame the two "asic parts of a CetAssem"l).
1*. !hat is the function of the no44le7
1. !hat is the purpose of the venturi7
1. !hat do we mean ") 8drive water97
1. !hat is the source of the 8drive water97
1B. !hat is the purpose of the centrifugal pump7
1L. !here is the Cet Assem"l) usuall) located in a
%hallow !ell Cet %)stem7
1@. !hat is the principal factor which determines if a
shallow well et s)stem can "e used7
20. !hen is a deep well et s)stem used7
21. $an a foot valve "e omitted from a #eep !ell Cet
%)stem7 !h)7
22. !hat is the function of a chec' valve in the top ofa su"mersi"le pump7
2*. A su"mersi"le pump is made up of two "asic parts.
!hat are the)7
2. !h) did the name su"mersi"le pump come into"eing7
A pump with all necessar) accessories, fittings, etc.,
necessar) for its completel) automatic operation.
(t is used on the end of a suction pipe to prevent the
water in the s)stem from running "ac' into the source
of suppl) when the pump isnt operating.
Io44le and Denturi.
The no44le converts the pressure of the drive water intovelocit). The velocit) thus created causes a vacuum inthe Cet Assem"l) or suction cham"er.
The venturi converts the velocit) from the no44le "ac'into pressure.
That water which is supplied under pressure to drive the
et.
The drive water is continuousl) recirculated in a closed
s)stem.
The centrifugal pump provides the energ) to circulate
the drive water. (t also "oosts the pressure of the
discharged capacit).
:olted to the casing of the centrifugal pump.
A ma/imum suction lift of 2? at sea level.
!hen the total suction lift e/ceeds 2 ?.
Io, "ecause there are no valves in the Cet Assem"l) and
the foot valve is necessar) to hold water in the s)stem
when it is primed. Also, when the centrifugal pump isnEtrunning, the foot valve prevents the water from running"ac' into the well.
To hold the pressure in the line when the pumpisnEt running.
Pump end and motor.
:ecause the whole unit, pump and motor, is designed to
"e operated under water.
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2. A su"mersi"le pump can "e installed in a 23 well7
2. A stage in a su"mersi"le pump is made up of
three parts. !hat are the)7
2B. A su"mersi"le pump has onl) one pipe connection7
2L. !hat are two reasons we should alwa)s considerusing a su"mersi"le first7
2@. The amount of pressure a pump is capa"le ofma'ing is controlled ") what7
*0. The width of an impeller and guide vane controlwhat7
Io, the) re5uired a 3 well or larger for most domestic
use. &arger pumps with larger capacities re5uire 3
wells or larger.
(mpeller, diffuser and "owl.
True, for the discharge pipe.
(t will pump more water at higher pressure with lesshorsepower. Easier installation.
The diameter of the impeller.
The amount of water or capacit) the pump is capa"le ofpumping.
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Pro-lems
3riction of Water P& A$H 2;; 3T of #ew Steel Pipe
)P" )PH/?@APipe 2?(APipe /?'APipe 2 Pipe 22?'APipe 22?(APipe ( Pipe (2?(APipe / Pipe
3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3t7 L-s7 3
1 0 .*0 1.L 1.L .L1 0.2 0.11
2 120 1.00 .@ .BL 2.0B 1.21 0.2 0.*L 0.1
* 1L0 *1.L0 1*.BB 10.00 .** 2.0 1.0L 0.BB 0.**
20 .@0 2*.BB 1B.10 B.0 .21 1.L2 1.*0 0. 0.* 0.1
*00 L*.0 *. 2.L0 11.1B .*2 2.B 1.@* 0.L 0.1 0.22 0.2 0.10
*0 *.0 1.L0 L.LB *.L 2.L 1.1 0.B0 0.*0 0.** 0.1 0.10 0.0B 20 L.B0 21.0L 11.L0 .11 *. 1. 0.@* 0.0 0. 0.1@ 0.1* 0.0
L L0 2.B0 2B.1 1.00 .@ . 1.@B 1.1L 0.1 0. 0.2 0.1B 0.0B
@ 0 1L.L0 L.1 . 2. 1. 0.* 0.@ 0.*0 0.21 0.0@
10 00 2*.00 @.@ .L 2.@B 1.BB 0.BB 0.L* 0.* 0.2 0.11 0.11 0.0 0.0 0.02
12 B20 *2.0 1.11 @.2 .1 2.L 1.0B 1.1 0.0 0.* 0.1 0.1 0.0 0.0 0.02
1 @00 @.B0 21.2 1.B0 .* *.B 1.2 1.B 0.B 0.2 0.2* 0.22 0.10 0.0L 0.0*
20 1200 L.10 *B.2B 2.10 10.LB .* 2.B 2.@ 1.2B 0.LB 0.*L 0.* 0.1 0.1* 0.0
2 100 *L.0 1.B1 @. .1L .L 1.@ 1.*0 0. 0. 0.2* 0.1@ 0.0L
*0 1L00 .0 2*. 1*.0 .L@ .2 2.B1 1.L2 0.B@ 0.B 0.*2 0.2 0.11
* 2100 B*.0 *1.BB 1L.20 B.LL L.*B *.2 2.2 1.0 1.00 0.* 0.* 0.1
0 200 @.00 1.1* 2*.0 10.1B 10.B@ .B *.10 1.* 1.2L 0. 0. 0.1@
2B00 *0.B0 1*.2@ 1*. .L2 *.L 1.B 1.0 0.@ 0. 0.2
0 *000 *.00 1.L 1.0 B.10 .B 2.02 1.@ 0.L 0. 0.2@ .
B0 200 L.L0 [email protected] *1.*0 1*. L.L *.L *.* 1.B 1.22 0.* .100 000 2.20 2.@* 1B.0 B.* B.11 *.0L 2.*@ 1.0* .
10 @000 *L.00 1. 1.0 .B .1 2.2* 1
200 12000 .*0 2L.B0 2.B0 11. L.@0 *.L 2
20 1000 @0.B0 *@.2 2.L0 1L.* 1.10 .10 *
*00 1L000 L.0 2.*2 [email protected] L.*1
*0 21000 [email protected] *.2@ 2.@0 11.
>rom the ta"le, give the friction loss in ft. for the followingconditions
*H3 11H3 23
100 >eet of Pipe
0 >eet of Pipe
10 >eet of Pipe
L0 >eet of Pipe
1. *0 GP6 ................................. a " c
2. 00 GP6 ................................. a " c*H3 11H3 23
*. 20 GP6 ................................. a " c
. 00 GP6 ................................. a " c1H23 13 11H23
. 20 GP6 ................................. a " c
. L0 GP6 ................................. a " c*H3 13 11H3
B. *0 GP6 ................................. a " c
L. 00 GP6 ................................. a " c
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Pro-lems (continued)
27 (7
TotalE5uivalent &ength of %uctionPipe from Pump #own into !ell.
*0 ft. *H3 Pipe
TotalE5uivalent &ength of %uctionPipe from Pump #own into !ell.
10 ft. Pipe
%tanding level of water
Pumping level of water
1 ft. Dertical &ift %tanding level of water
Pumping level of water
1L ft. Dertical &ift
Pump $apacit) GP;
a.!hatisfrictionloss7
".!hatistotallift7
Pump $apacit) 10 GP;
a. !hat si4e suction pipe is re5uired to 'eep totallift within 2 feet7
".!hatisfrictionloss7
c.!hatistotallift7
/7
Pump $apacit)
GP; Elevation 2* ft.
>riction&oss l"s.
perating Pressure 20-0 l"s.
a. !hat is the %ervice Pressure7
>riction
%ervice Pressure
Elevation
!ell 6ouse Pump and Tan'
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Pro-lems (continued)
'7 7%ervice
Pressure
%ervicePressure
>riction Elevation >riction Elevation
!ell6ouse
Pump and Tan'
Pump $apacit) GP;
!ell6ouse
Pump and Tan'
Pump $apacit) 10 GP;
Elevation 2* ft.
perating Pressure 20-0 l"s.
200 ft. of *H3 #ischarge Pipe
a. 6ow much is friction loss7
". !hat is the %ervice Pressure7
c. !hat change would )ou ma'e in this s)stem
and what would the result "e7
Elevation L0 ft.
%ervice Pressure Me5uired 20-0 l"s.
&ength of #ischarge Pipe *00 ft.
a.!hatsi4epipetouse7
".6owmuchisfrictionloss7
c. !hat will the operating pressure of the pump
"e7d. 6ow man) continuous use outlets operating at
the same time will this capacit) suppl)7
Pump $apacit) is L GP;.
%ervice Pressure Me5uired at Tan' in:asement is *0 l"s.
a. !hat is the total length of pipe to "e considered
for friction loss7 >t.". !hat is the friction loss in feet7 >t.
c. !hat is the total feet the pump will have toovercome to get water to the tan'7 >t.
PME%%+ME%!(T$6
0? E&EDAT(I
120?
20?
P+;P(IG &EDE&
P+;P %ETT(IG
2001 Goulds Pumps
PM(ITE# (I +.%.A. SP$I3I$ATIO#S A& S
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Pro-lems (continued)
>ormLBA-!% :P+;P