ahmed abdalghani pump presentation
TRANSCRIPT
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PUMPING & HYDRONICBALANCING
AHMED ABD EL GHANI
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Contents of This Lecture
Pump Curve
Net Positive Suction Head
System Curve
Pressure Gradient Diagrams
Pumping Arrangement
Parallel Series
Why alancing alancing !alves
Static alancing
Dynamic alancing
"lo# Con$guration Direct %eturn
%everse %eturn
Pumping Con$guration
Primary Secondary
!aria&le Primary Primary Distri&uted Secondary
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WHAT 'S TH( D'""(%(NC(?
Same "lo# %ate Same Pipe Si)e
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WHAT 'S TH( D'""(%(NC(?
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Head Capacity Curve
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"lat !ersus Steep PumpCurve
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Pump Head*Capacity Curve
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Pumping (nergy
Water horsepower The energy re+uired &y a pump, as indicated &y the a-nity
la#s, depends on its speed and the diameter of its impeller.
Where / 0 1o#, in gal2min.h 0 head, in ft
s 0 speci$c gravity
Pump brae horsepower
The energy re+uired to operate a pump is determined in&ra3e horsepo#er &hp4 the di5erence &et#een #aterhorsepo#er and pump &ra3e horsepo#er is the energy lostin the pump.
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Pumping (nergy
Where 0 pump e-ciency as a decimal
Pump Motor Power !" #!$owatts
The electrical energy, pump 3ilo#atts, for a motor*driven pump must ta3e in consideration the e-ciencyof the motor on constant*speed pumps and the #ire*to*
shaft e-ciency of the motor and varia&le* speed driveon varia&le*speed pumps.
Where is the e-ciency of the electric motor or themotor and varia&le*speed drive as a decimal
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Total HP %e+uirementCurve
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Pump Curves at GivenSpeed
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'mpeller Pressures Causing %adial Thrust
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%adial Thrust !ersusPumping %ate
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Pump (-ciency
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Pump Head*Capacity Curve
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Pumping Po#er 'ncrease 7 Pump "lo#
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Pump Curve Sho#ingNPSH%
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NPSHA in Proposed'nstallation
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NPSH %e+uired
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!apor Pressure 7 Speci$c Weight forWater, 89 to 9:9o"
!apor pressure is the a&solute pressure,psia, at #hich #ater #ill change fromli+uid to steam at a speci$c
temperature. "or each temperature of#ater, there is an a&solute pressure at#hich #ater #ill change from a li+uid toa gas
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Water !apor Pressure
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H!AC Pumps 7 Performance
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H!AC Pump Performance
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H!AC Pump Performance
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System Curve Plot
i
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(+uations "rom PumpA-nity La#s
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System Curve
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System Curve
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System Curve 7 Pump head*Capacity Curve
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System Curve 7 Pump Head*CapacityCurve
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Parallel 7 Series Pump Application
P ll l P Pi i
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Parallel Pumps PipingSchematic
P ll l P S t
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Parallel Pump System;peration
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Single Pump ;peration*Paralleled'nstallation
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uilt*up Pump Curves
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Pump Curve (nd Point
P ll l d P ( d
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Paralleled Pumps < (ndPoint Curve
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Pump Curve (nd Point
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Paralleled => Pump Curve
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System Curve
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Single Pump ;peration
Typical uilt up Pump
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Typical uilt*up PumpCurves
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Paralleled Pump Curve
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Single Pump ;peration
Series Pumps? Piping
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Series Pumps PipingSchematic
asic Series Pump
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asic Series Pump;peration
Seriesed Pump Curve
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Seriesed Pump CurveConstruction
Seriesed Pump System
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Seriesed Pump < System;peration
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Single Pump ;peration*Seriesed 'nstallation
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Design %e+uirement
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Seriesed Pump Curve
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Single Pump ;peration
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Design %e+uirement
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Seriesed Pump Curve
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Com&ination Parallel 7 Series Pump Curves
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System ;perational Time
Pump Curve@ Po#er %eduction !ersus
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Pump Curve@ Po#er %eduction !ersusPump Speed
Load Pro$le 7 WH Bsage Calculation for C2S
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Load Pro$le 7 WH Bsage Calculation for C2S(ample
Potential HP Saving as A5ected &y
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Potential HP Saving as A5ected &yaintaining a Constant Head
Ad ; Si l C2S L
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Advantage ;ver Single C2S at Lo#"lo#
est pp cat on rea or ara e +ua ySi)ed C2S
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Si)ed C2SPumps in Comparison #ith !2S ;ccurs WhenSystem !aria&le Head Loss in Lo#
!aria&le "re+uency Drive Control
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!aria&le "re+uency Drive Control(-ciency
!aria&le "re+uency Drive Control
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!aria&le "re+uency Drive Control(-ciency
!aria&le Speed ;perational Points
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!aria&le Speed ;perational PointsA, , (, etc
ustrat on o ontro urve
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Change*overPoint for Parallel C2S Pump
!2S Pump in Parallel #ith
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!2S Pump in Parallel #ithC2S
;peration of Paralleled !2S pump at Lo#
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;peration of Paralleled !2S pump at Lo#"lo#, Bp to Change*over Point
Small Lo#er HD Pump*>Humps> is "lo#*
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Small Lo#er HD Pump* Humps is "lo#*Head Curve onto Larger Pump
High "lo# Need4 !2S Pump =Humps>
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High "lo# Need4 !2S Pump Humpsonto C2S Pump Curve
Capacity
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Capacity(ceeds Curve (nd at ;ver EF
Speed
(nergy Wasting Solution to ParallelP
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Pump=(nd of Curve> Pro&lem4
'ncrease aintained Constant HeadDi5erence
est Solution to Parallel pump =(nd
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est Solution to Parallel pump (ndof Curve>
Parallel Pump Application of
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Parallel Pump Application of!aria&le !olume (ample
odel uilding for System Head Area
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odel uilding for System Head Area(valuation
odel uilding for
system head areaevaluation
Bniform system headcurve for model&uilding of A
d l ildi L di
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odel uilding Loading
a. Bniformly loaded&uilding F load on each
&. Non*uniformlyloaded &uilding, AHBs
close to pumping
odel uilding Loading
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odel uilding Loading
c. Non*uniformly loaded &uilding, AHBs far
from pumping source fully loaded
Con$guring an H!AC Water System
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Con$guring an H!AC Water SystemSystem Head area
C T Chill d H t W t S t
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Campus Type Chilled or Hot Water System
a. Load los variation incentral plant
&. System head area caused&y non*uniform 1o# in&uilding => 7 other
Point of Selection
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Point of Selection
The &asic rule that has &een o5ered in theindustry is to select the pump as closelyas possi&le to its &est e-ciency point.
Points of Pump Selection 7 ;peration
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Points of Pump Selection 7 ;peration
Points of Pump Selection 7 ;peration
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Points of Pump Selection 7 ;peration
Selecting Constant Speed Pumps
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Selecting Constant*Speed Pumps
Constant*speed pumps should operate at no greater1o# range than I9J percent of the 1o# at the &este-ciency point.
Normally, pumps for constant*speed operation #ould
&e selected Kust to the left of the of the &este-ciency point.
A dangerous point to operate a pump is at :FFF gal 2min and :8F ft of head, as sho#n in "ig. :F.:a. Thisis an unaccepta&le selection &ecause of the poore-ciency and the high radial thrust eisting at thispoint. Additional #ear may occur due to hydraulicim&alance #ithin the pump.
Sometimes H!AC #ater systems are designed #ith
more estimated pump head than actually eists in
Selecting Constant Speed Pumps
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'n an attempt to avoid poor pumpoperation, and recogni)ing theina&ility to compute system head
accurately, the usual practice #ithconstant*speed pumps has &een toadd a pump head conservation
factor and then pic3 the pump to theleft of the &est e-ciency point toensure that the pump #ill operate#ithout damage at the higher 1o#s
Selecting Constant*Speed Pumps
Steep !ersus "lat Head Capacity Curves
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Steep !ersus "lat Head*Capacity Curves
With the advent of varia&le*volume #ater systems utili)ingvaria&le*speed pumps and system di5erential pressurecontrols, there is very little need to &e concerned a&outthe shape of the pump curve.
"lat*curved pumps are desired.
Pumps #ith 1at*curved head*capacity characteristicsshould &e sought for varia&le*speed pumping applications,provided there is no loss in pump e-ciency.
's less speed reduction #ith a 1at*curved pump than #ith asteep*curved pump.
Less speed reduction, the #ire*to*shaft e-ciency of thevaria&le speed drive and motor is greater &ecause thespeed reduction is less.
T#o*Pipe Source*Load
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pConcept
Airside 7 Waterside "lo# 7 Temperature
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pConditions
Control Se+uence
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Control Se+uence
The si component elements of the control loop interact#ith each other
T#o*Way Control Calve ody
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Single 7 Dou&le Seat
Terminal Control #ith Thermostat 7 Three*
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Way iing !alve
Terminal Control #ith Thermostat 7 To#*
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Way !alve
Three*Way Control !alves
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iing 7 Diverting Types
Three*#ay !alve 'nstallation Controlling
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System Water Temperature
Three*Way valve installation controlling
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unit 1o# rate
T#o*Pipe Systems, Direct %eturn, Bn&alanced &MP Di t i& ti Di
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Pressure Distri&ution Diagram
T#o*Pipe Systems, %everse %eturn aM "lo#
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Diagram Pressure Distri&ution Diagram
Coil ;utput !ersus Temperature "lo#
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Change
Water Coil (mission
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Water Coil (mission
(5ects of "lo# !ariation on Heat Transfer "or' d D i T D
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'ncreased Design Temperature Drops
(5ects of "lo# !ariation on Heat Transfer "or9FD i T D
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9FDesign Temperature Drop
Chilled Water Coil (mission
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Chilled Water Coil (mission
Control !alve "lo# Characteristics
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(+ual percentage !alve and Coil (mission
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(+ual percentage !alve and Coil (mission
Non*Linearity of The Terminal Bnit Characteristic isCompensated &y Adoption of an 'nverse Non*Linear
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p y pCharacteristic "or The Control !alve
Distortion of (+ual PercentageCh t i ti
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Characteristic
Direct and %everse %eturn System
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Direct and %everse %eturn System
a. Direct %eturnPiping
&. %everse %eturn
Piping
Direct and %everse %eturn System
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Direct and %everse %eturn System
C. Pressure Gradient fora direct %eturn System
d. Pressure Gradient fora direct %eturn System
Pressuri)ation of Closed Hydronic System
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y y
Primary circuit pressuri)ed at PumpSuction aM "lo# Diagram &M
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Suc o aM o ag a &MPressure Distri&ution Diagram
!aria&le*volume*"lo# System, Control of%everse %eturn aM "lo# Diagram &M Pressure
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gDistri&ution Diagram
* ,of alancing aM "lo# Diagram &M PressureDistri&ution Diagram eM %esistance Splitting at
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Distri&ution Diagram eM %esistance Splitting atPartial "lo#
to The Control !alve on 'ts
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Degree of ;pening
Applied Control !alve; ti
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;peration
Correct !alve Shut*;5Pressure %ating
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Pressure %ating
Distri&ution SystemDi
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Diagram
Pressure Gradient Diagram for aDistri&ution System at "ull Load
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Distri&ution System at "ull Load
Direct %eturn Pressure Gradient at PartLoad ;perating
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Load ;perating
Note@ Pump is not %iding the Curve
Ne# Pressure Gradient 7 Pump %iding
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Ne# pressure gradient#ithpump riding the curve