Taco Pump Curves How to Read and Use

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  • 8/10/2019 Taco Pump Curves How to Read and Use

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    HYDRONICSYSTEMSPARTPUMP CURVES -HOW TO READ

    ND US

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    INTRODUCTIONThis text provides reference information for a seminar on reading nd using pump cuwesThe information in this seminar will pply to products m nuf ctured by T CO nd other companies T COproducts nd illustrations are used in some cases to offer specific examples in the text

    CONTENTSP RT I - Fundamentals

    P RT II - The System Curve 3

    P RT Ill - Stable Curves Unstable Curves and Parallel Pumping 5

    P RT IV - Non-Overloading Pump Curve - What Does It Really Mean 7

    P RT V - NPSH and Pump Cavitation 9

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    PART I FundamentalsA centrifugal pump operated at constant speeddelivers any capacity from zero to maximumdepending on the head, design and suctionconditions. Pump performance is most commonlyshown by means of plotted curves which are

    graphical representations of a pump s performancecharacteristics. Pump curves present the averageresults obtained from testing several pumps of the

    same design under standardized test conditions. Fora single family residential app lication, considerationsother than flow and head are of relatively littleeconomic or functional importance, since the totalload is small and the equipment used is relativelystandardized. For many smaller circulators, only theflow and pressure produced are represented on theperforman ce curve (Fig. 1-1 ). For larger and morecomplex buildings and systems, economic andfunctional considerations are more critical, and

    PERFORMANCE FIELD

    F L O W M 3/H

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    F L O W GPM

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    performance curves must relate the hydraulicefficiency, the power required, the shaft speed, andthe net positive suction head required in addition tothe flow and pressure produced (Fig. 1-2). Pumpperformance curves show this interrelation of pumphead, flow and efficiency for a speci fic impellerdiameter and casing size. Since impellers of morethan one diameter can usually be fitted in a givenpump casing, pump curves show the performance ofa given pump with impellers of various diameters.Often, a complete line of pumps of one design isavailable and a plot called a c omposite or quickselection curve can be used, to give a completepicture of the available head and flow for a givenpump line (Fig. 1-3). Such charts normal ly give flow,head and pump size only, and the specificperformance curve must then be referred to forimpeller diameter, efficiency, and other details. Formost application s in our industry, pump curves arebased on clear water with a specific gravity of 1.0.

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    Quick Selection Curve

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    v , .FLOW IN GALLONS PER MINUTE

    . Fig. 1 3

    ow is a volume measure to establish pumppacity per unit of time, usually as GPM.

    ead is a pressure measure represented by how highe pump can lift a column of liquid, usually in feet.convert the popular pressure expression P S I to

    et of water, multiply P S I x 2.31.

    orsepower H.P.) is the term used to express themount of power available to drive the pump.

    rake Horsepower BHP) is the term used to expresse amount of power required to drive the pump.

    et Positive Suction Head Required NPSHR) is aessure measure - in absolute units - expressed inet and indicates the pressure required at the

    ump suction to prevent cavitation. Reducing theessure at the pump flange below the vaporessure of the liquid can cause formation of vappr

    ockets in the impeller passes. This conditionavitation) will interfere with pump performance,d is usually accompanied by noise as the vapor

    ockets collapse. NPSHR can be thought of as themount of pressure in excess of vapor pressurequired to prevent the formation of vapor pockets.

    et Positive Suction Head Available NPSHA) is therm used to express the pressure available at theump suction flange. If NPSHAis less than NPSHR.vitation problems should be expected.

    mp Efficiency indicates the percentage of brakeorsepower converted into useful work. Pumpficiency, along with flow, head, and liquid specificavity affect the power required to drive the pump.

    he more efficient the pump, the less power requireddrive it.

    ecific Gravity S.G.) is the term used to expressldtive weight of a liquid when compared withater water= 1.0 S.G. .

    2

    R.P.M. is the term used to express the rotationalspeed of a pump.

    Some addi tional terms that are often used whenconsidering a pump's relationship to the particularsystem into which it will be installed are reviewedbelow.

    Shut. )ff Head is the term used to express the headdeveloped by a pump at zero flow.

    static Head is the term used to express the pressure

    at the pump discharge which the pump mustovercome before it can produce flow. Static head isa difference in elevation and can be computed for avariety of condit ions surrounding a pump installation.

    System Resistance is the term used to express thepressure on the pump discharge resulting from theresistance to flow created by friction between thefluid and the piping system. This value will vary withflow rate.

    Suction Pressure is the term used to express thepressure observed at the pump suction connection.This may be a positive pressure or a negativepressure.

    Discharge Pressure is the term used to express thepressure at the discharge connection. This will alwaysbe a positive pressure.

    Differential Pressure is the term used to express thealgebraic difference between the discharge andsuction pressures. This value represents pump head.

    Service Factor is the term used to express the reserve power availab le from an electric motor whenoperating under normal conditions.

    System Curve is a graphical representation of thehydraulic characteristics of a piping system. When

    the pump performance curve is laid over the systemcurve, the intersection indicates the flow and headpressure of the pump when coupled to the hydraulicsystem.

    Constant Speed is the term used to express the RPMof a pump upon which a published pump curve isbased.

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    PART II T h e System CurveUnderstanding a system curve, sometimes cal led asystem head curve, is important because conditionsin larger, more complex p iping systems vary as aresult of either controllable or uncontrollablechanges. A pump can operate at any point of ratingon its performance curve, depending on the actualtotal head of a particular system. Partially closing avalve in the pump discharge or changing the size or

    length of pipes are changes in system conditionsthat will alter the shape of a System Curve and, inturn, affect pump flow. Each pump model has 0definite capacity curve for a given impeller diameterand speed. Developing a system curve provides themeans to determine at what point on that curve apump will operate when used in a particular pipingsystem.

    Pipe, valves and fittings create resistance to flow orfriction head. Developing the data to plot a systemcurve for a closed hydronic system under pressurerequires calculation of the total of these friction headlosses. Friction tables are readily available that

    provide friction loss data for pipe, valves and fittings.These tables usually express the losses in terms of theequiva lent length of straight pipe of the same size asthe valve or fitting. Once the total system friction isdetermined, a plo t can be made because thisfriction varies roughly as the square of the liquid flowin the system. This plot represents the System Curve.By laying the system curve over the pumpperformance curve, the pump flow can edetermined Fig. 2-2). Care must be taken that bothpump head and friction are expressed in feet andthat both are plo tted on the same graph. The systemcurve will intersect the pump performance curve atthe flow rate of the pump because this is the point at

    which the pump head is equal to the requiredsystem head for the same flow.

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