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Efficient Pump Selec/on & Control

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  • EfficientPumpSelec/on&Control

  • GrundfosTechnicalIns2tutewww.grundfos.us/training

    •  VirtualClassroom–  Self-Paced–  Over50courses–  Cer2ficatesofComple2on

    •  Webinars–  LiveandRecorded

    •  Face-to-FaceTraining

  • PointsonaPumpPerformanceCurveShut-Off Head/Dead Head

    Shut-OffHeadNoflowperformance,don’trunhereformorethanafewminutes(Damagefromheatbuildupcanoccur)

    Duty Point DutyPointThedesignflowandhead,thisiswhatisrequired,usuallybasedoncalcula2ons

    Run-Out/End of Curve

    RunOut/EndofCurveThisisthemaximumallowableflowrateforthepump.Flowsexceedingthisshouldbeavoided(Damagecanoccur) Pump Efficiency

    PumpEfficiencyThisisthepumphydraulicefficiency,doesnottypicallyincludemotorefficiency

    Brake Horsepower

    BrakeHorsepowerThisisthehorsepowerrequiredbythepump.Anypointonthiscurveshouldbelowerthanthemotornameplatehorsepower

    NPSHR

    NPSHNetPosi2veSuc2onHead,theactualsuc2onheadofthesystemmustbehigherthanthisvalue.Veryimportantinboilerfeedsystemsandsystemswithfloodedsuc2on.Notsoimportantforcoldwaterfromapressurizedsourceorhydronichea2ng/coolsystems

    Operating Point Opera/ngPointThisiswherethepumpisactuallyrunning,wherethesystemcurveintersectstheperformancecurve

  • Twocommonvariableflowpumpapplica2ons

    HVACCircula2on–Hotand/orChilledWaterWaterSupply–PressureBoos2ng

  • dP

    SUPPLY

    RETURN

    HVACCircula2onDifferen2alPressuremeasuredremotely

  • dP

    SUPPLY

    RETURN

    HVACCircula2onDifferen2alPressuremeasuredacrosspumps

  • Suc2onPiping–CityWaterConnec2on

    Control

    DischargePiping

    PressureBoos2ng

    PackageMountedSensor

    RemoteMountedSensor

    WaterSupplyRisers

  • PumpHead/CapacityCurve

    H

    Q

    Q

    HP

    Eff

    BEP

  • PumpHead/CapacityCurve

    H

    Q

    DesignCondi2on

    Headrequiredincreases

    withflow

  • PumpHead/CapacityCurve

    H

    Q

    DesignCondi2on

  • TheAffinityLawsforcentrifugalpumps

    1

    212 TDHTDHRPMRPM =

    When TDH1, RPM1 and TDH2 are known:

    2

    1

    2

    1RPMRPM

    GPMGPM

    = ⎟⎟⎠

    ⎞⎜⎜⎝

    ⎛=

    1

    212 RPMRPMGPMGPM> > Flow varies linearly with pump speed

    2

    2

    1

    2

    1RPMRPM

    TDHTDH

    ⎟⎟⎠

    ⎞⎜⎜⎝

    ⎛=

    2

    1

    212 RPMRPMTDHTDH ⎟⎟

    ⎞⎜⎜⎝

    ⎛=> > Head varies with the square of the pump

    speed

    3

    2

    1

    2

    1RPMRPM

    BHPBHP

    ⎟⎟⎠

    ⎞⎜⎜⎝

    ⎛=

    3

    1

    212 RPMRPMBHPBHP ⎟⎟

    ⎞⎜⎜⎝

    ⎛=> >

    Brake Horsepower varies with the cube of the pump speed

    1=Originalcondi2on(fullspeed)2=Newcondi2on(reducedspeed)

    Whataboutefficiency?

  • H

    Q

    60Hz 55Hz

    50Hz 45Hz

    40Hz 35Hz

    30Hz

    35% 42% 55%

    62%

    67%

    65%

    60%

    54%

    Curvesofconstantefficiencywithspeedreduc2onsRemember…..theaffinitylawsassumeconstantpumpefficiency.Thepumpcanonlyruncon2nuouslyatitsBestEfficiencyPointalongasystemorcontrolcurvethatfollowsacurveofconstantefficiency

  • H

    Q

    60Hz 55Hz

    50Hz 45Hz

    40Hz 35Hz

    30Hz

    35% 42% 55%

    62%

    67%

    65%

    60%

    54%

    ConstantPressure:Asflowreducessodoespumpefficiency!

    Curvesofconstantefficiencywithspeedreduc2ons

  • H

    Q

    60Hz 55Hz

    50Hz 45Hz

    40Hz 35Hz

    30Hz

    35% 42% 55%

    62%

    67%

    65%

    60%

    54%

    SimilarlywithHVACCircula2onEfficiencyalsoreduceswithreducingflow

    Curvesofconstantefficiencywithspeedreduc2ons

  • H

    Q

    60Hz 55Hz

    50Hz 45Hz

    40Hz 35Hz

    30Hz

    35% 42% 55%

    62%

    67%

    65%

    60%

    54%

    Whenselec2ngpumpsforvariableflowSelectpumpsbasedonadesignflowthatistotheRIGHTofthepumpsbestefficiencypoint.

    Curvesofconstantefficiencywithspeedreduc2ons

  • DesignFlow:1000gpmDesignHead:75feet

    PumpSelec2onExample

  • Option 1 1750 83.16 9.25 26.7 97.60 6 x 5Option 2 1750 82.94 8.39 25.5 81.24 6 x 5Option 3 1750 80.03 12.7 24.7 81.24 5 x 4Option 4 1750 78.09 27.2 24.2 92.69 5 x 4Option 5 1750 83.71 10.1 24.8 89.80 6 x 5

    Pump Speed [rpm]Pump

    Size [Suc/Dis]

    % Max. Diameter

    Max. Power [bhp]NPSHr

    Pump Efficiency

    [%]

    DesignFlow:1000gpmDesignHead:75feet

    Selec2onToolResults:

    PumpSelec2onExample

  • Option 1 1750 83.16 9.25 26.7 97.60 6 x 5Option 2 1750 82.94 8.39 25.5 81.24 6 x 5Option 3 1750 80.03 12.7 24.7 81.24 5 x 4Option 4 1750 78.09 27.2 24.2 92.69 5 x 4Option 5 1750 83.71 10.1 24.8 89.80 6 x 5

    Pump Speed [rpm]Pump

    Size [Suc/Dis]

    % Max. Diameter

    Max. Power [bhp]NPSHr

    Pump Efficiency

    [%]

    DesignFlow:1000gpmDesignHead:75feet

    Selec2onToolResults:

    Op2on5=Highestefficiency,butisitthebestchoiceforvariableflow?Youmustlookatthepumpcurvesaswellasthecontrolcurve!

    PumpSelec2onExample

  • 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 0 0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    110

    120

    130

    140

    Head (ft.)

    Flow (gpm)

    1000 gpm / 75 feet

  • 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 0 0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    110

    120

    130

    140

    Head (ft.)

    Flow (gpm)

    65% 75%

    80% 84.5% 85%

    83.5% 78%

    70%

    Option 5

  • 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 0 0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    110

    120

    130

    140

    Head (ft.)

    Flow (gpm)

    65% 75%

    80%

    83% 83.5%

    82%

    78%

    70%

    65% 75%

    80% 84.5% 85%

    83.5% 78%

    70%

    Option 4

    Option 5

  • 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 0 0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    110

    120

    130

    140

    Head (ft.)

    Flow (gpm)

    Op/on4Hydraulic(Pump)efficiencyrangesbetween75-83%alongcontrolcurve

    65% 75%

    80%

    83% 83.5%

    82%

    78%

    70%

    65% 75%

    80% 84.5% 85%

    83.5% 78%

    70%

    Option 4

    Option 5

  • Option 1 1750 83.16 9.25 26.7 97.60 6 x 5Option 2 1750 82.94 8.39 25.5 81.24 6 x 5Option 3 1750 80.03 12.7 24.7 81.24 5 x 4Option 4 1750 78.09 27.2 24.2 92.69 5 x 4Option 5 1750 83.71 10.1 24.8 89.80 6 x 5

    Pump Speed [rpm]Pump

    Size [Suc/Dis]

    % Max. Diameter

    Max. Power [bhp]NPSHr

    Pump Efficiency

    [%]

    Op2on4hasthelowestenergyconsump2on,yetthelowestefficiencyatthedesignflow.Howmanyhoursdoyoureallyrunatdesignflow,ifever…..

  • Example:BasicRequirementsDesignFlow:350gpmDesignTDH:90feet

    Mul2plePumpOpera2on-Parallel

  • Ques2on:Dowejustselecta350gpmpumpwithaheadcapacityof90feetandbedonewithit?

  • LoadProfile

  • Two50%pumps:

    DesignFlow:350gpm

    DesignTDH:90feet

    Pumps:2x7.5HP

    BHPatDesign:11.9

  • One100%Pump:

    DesignFlow:350gpm

    DesignTDH:90feet

    Pumps:1x15HP

    BHPatDesign:10.5

  • (1)CR64-115HP

    (2)CR32-2-17.5HP

    EnergyConsump2on

    Total=20,877kWh/Year

    Total=24,856kWh/Year

    At75-100%flowthesinglepumphasalowerkWrequirement(higherpump/motorefficiency).Butpumpsgenerallyhavehigherrunninghoursatlowerflowratesthereforethetwopumpsolu/onisabeberchoiceoverallduetothehigherpumpefficiencyatflowslessthan50%.

    1x15HPPump

    2x7.5HPPumps

  • Methods:>Flow>Current[Amps]>Speed>Demand[set-pointnotbeingreached]>Efficiency

    ParallelConnectedPumps-PumpSequencing

    Whichisbest?Itdepends……..……onalotoffactors

  • ParallelConnectedPumps-FlowSequencing

  • ParallelConnectedPumps-FlowSequencing

  • ParallelConnectedPumps-FlowSequencing

  • ParallelConnectedPumps-FlowSequencing

    Flowsequencing,needtostartbefore400gpm

  • ParallelConnectedPumps-FlowSequencing

    Flowsequencing,needtostartbefore400gpm

    Flowsequencing,approx.820-830gpm

  • ParallelConnectedPumps-FlowSequencing

    Flowsequencing,needtostartbefore400gpm

    Flowsequencing,approx.820-840gpm

  • ParallelConnectedPumps–SpeedSequencing

  • ParallelConnectedPumps–SpeedSequencing

  • ParallelConnectedPumps–SpeedSequencing

    SpeedSequencing,needtostartbefore91%speed.Cavita2oncanhappenif2ndpumpisnotstarted.

  • ParallelConnectedPumps–SpeedSequencing

    SpeedSequencing,canstartbetween95-99%

  • ParallelConnectedPumps–SpeedSequencing

  • ParallelConnectedPumps–DemandSequencing

    DemandSequencing,headwilldropoffatapprox.91%speed.2ndpumpwillbestartedwhenthisoccursasset-pointisnotbeingmaintained.

  • ParallelConnectedPumps–DemandSequencing

    DemandSequencing,headwilldropoffwhenbothpumpsreachfullspeed,3rdpumpwillneedtobestarted.

  • ParallelConnectedPumps–DemandSequencing

  • ParallelConnectedPumps-EfficiencySequencing

    Eff.%

  • ParallelConnectedPumps-EfficiencySequencing

    Eff.%

  • ParallelConnectedPumps-EfficiencySequencing

    Eff.sequencing,approx.340gpm

    Eff.%

  • ParallelConnectedPumps-EfficiencySequencing

    Eff.sequencing,approx.340gpm

    Eff.sequencing,approx.700gpm

    Eff.%

  • ParallelConnectedPumps-EfficiencySequencing

    Eff.sequencing,approx.340gpm

    Eff.sequencing,approx.700gpm

    Eff.%

    Ifflowandheadarecon2nuouslymeasuredand/orcalculated,pumpefficiencyisknownduringopera2on.Thethirdpumpstartedatapproximately700gpmeventhoughtwopumpscoulddothejobupto840gpm.

  • Onepump–400gpmat62feet

    2.90.683 x 3960

    1.0 x 62 x 400 x 3960

    SG x H x Qbhppump

    ===η

  • Onepump–200gpmat62feet

    4.82x2.40.742 x 3960

    1.0 x 62 x 200 x 3960

    SG x H x Qbhppump

    ====η

    Savingsof8.7%

  • Whatiftherequiredheadchanges?Doesthateffectpumpsequencing?

  • ParallelConnectedPumps-FlowSequencing

    Changesinpumpheadwillrequirereseqngofflow,speedanddemandbasedsequencing.

  • Mostefficient:Stageonefficiency>TotalEfficiency(Electrical+Hydraulic)>HydraulicEfficiency

    ParallelConnectedPumps-PumpSequencing

  • Mostefficient:Stageonefficiency>TotalEfficiency(Electrical+Hydraulic)>HydraulicEfficiency

    Excep2on

    >Limitedsuc2onhead,muststartaddi2onalpumpsbeforeflowgetstoohigh Examples:BoilerFeed,CoolingTower,water supplyfrombreaktank

    ParallelConnectedPumps-PumpSequencing

  • Thankyouforyouraben/on!

  • NOTE:

    ThefollowingslidesarenotpartofmainslidedeckbutarelesherejustincasetheycanbeusedtohelptheQ&Asession.Ifthepresenta2onismadeavailabletotheviewers,theseslidearetobeLEFTOUT.

  • Misconcep2on

    Sincevariableheadlossesaresuchasmallpercentageofthetotalheadinhighrisebuildingapplica2ons,variablefrequencydrivesresultinliuleornoenergysavings.

  • 0

    50

    100

    150

    200

    250

    300

    0 25 50 75 100 125 150 175

    Flow (gpm)

    Hea

    d (ft

    .)

    Shaded areas represent amount of savings potential with vfd driven multi-stage pump+

    Shaded area represents amount of savings potential with vfd driven single stage pump

    SampleMul/-StageA=25gpmat180feetTDH,2882rpm,bhp=2.3B=25gpmat266feetTDH,3500rpm,bhp=3.9C=Lineofconstantefficiency,49%

    SampleSingleStageA=25gpmat180feetTDH,3319rpm,bhp=3.7D=25gpmat200feetTDH,3500rpm,bhp=4.2C=Lineofconstantefficiency,31%

    B

    C

    A

    DAt25gpmtheVFDcontrolledMul2-Stagewillconsume45%lessenergy(2.3bhpvs.4.2bhp)thanthefixedspeedsinglestagepump

  • Typical VFD Efficiency Curve

    84

    86

    88

    90

    92

    94

    96

    98

    10 20 30 40 50 60Frequency (Hz)

    Effic

    ienc

    y (%

    )

    100% Torque

    75% Torque

    50% Torque

    25% Torque

    Source: Hydraulic Institute/Europump Guide to Life Cycle Costs

  • 10

    20

    30

    40

    50

    60

    70

    80

    9.5”

    100

    0 0 100 200 300 400 500 600 700 800

    TOTAL HEAD

    IN FEET

    10

    20

    30

    40

    0

    US GALLONS PER MINUTE

    9”

    8.5”

    8”

    7.5”

    7”

    50%

    60%

    65

    %

    70%

    90 1750 RPM

    NPSHR IN

    FEET

    TypicalSingleStagePumpCurve

  • 10

    20

    30

    40

    50

    60

    70

    80

    9.5”

    100

    0 0 100 200 300 400 500 600 700 800

    TOTAL HEAD

    IN FEET

    10

    20

    30

    40

    0

    US GALLONS PER MINUTE

    9”

    8.5”

    8”

    7.5”

    7”

    50%

    60%

    65

    %

    70%

    90 1750 RPM

    NPSHR IN

    FEET

    TypicalEndSuc2onPumpCurve

    480 gpm at 65 feet required

  • RemembertheBasics…..

    SG x H x Qwhp P3 3960==

    Waterhorsepower(a.k.a.hydraulichorsepower)

    Brake horsepower (Pump Shaft)

    x

    SG x H x Qbhp Ppump

    2 η3960==

    Electrichorsepower(InputPower)

    bhpehp P

    driver1 η

    ==

    x

    0.746 x bhpehp [kW] Pdrivemotor

    1 ηη==

    efficiency driver driverη =

    )eta"" symbol(Greek Efficiency Pump liquid ofGravity SpecificSG

    feet in Head Hgpm in Flow Q

    η ==

    =

    =