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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