1
8 1 General Pump Selection 1.3 NPSH value The NPSH value (Net Positive Suction Head) is significant in assessing the suction characteristics of a centrifugal pump: It describes the minimum inlet pressure required by each centrifugal pump for reliable and cavitation-free operation [1.13]. We need to distinguish between the permissible cavitation, which causes the developed head of the pump to drop by 3 percent (also referred to as NPSH r = required) and the NPSH value of the system (also referred to as NPSH a = available). Cavitation-free pump operation generally requires the following condition to be met: The safety allowance is defined in accordance with ATV (German Association for Water, Waste Water and Waste) and HI (Hydraulic Institute) as 30 % of NPSH 3% of the pump. NPSH a can be calculated using equation (10a). NPSH a ^ NPSH r , NPSH r = NPSH 3% + safety allowance (9) NPSH a = z e + + - HI pe + p b - pD ρ · g 2 · g v e 2 (10a) This equation can be simplified for an open system installed at altitudes up to 3300 ft AOD and a fluid temperature of 86 °F: NPSH a = z e + 10 m (10b) To be able to document the NPSH 3% value of a pump in the sales literature, pump manufac- turers conduct a test run in a test field using a special dry pump installation. In a wet installation this NPSH value is practically impossible to measure. As the NPSH 3% value changes in relation to the flow rate it is entered as a function of the flow rate NPSH r = f(Q). This value describes the pressure head in meters or feet required above the vapor pressure of the fluid at the impeller inlet (reference point for NPSH = intersection of pump shaft axis and the perpendicular plane through the extremities of the vane leading edge, sometimes referred to as the impeller eye, see Fig. 1.3). P S' P S' P S' P S' P S' P S' Fig. 1.3: “Position of the reference point Ps’ for various impeller types” (Source: KSB publication Selecting Centrifugal Pumps)

Data 111

Embed Size (px)

DESCRIPTION

Data 111

Citation preview

  • 81 General Pump Selection

    1.3NPSH value

    The NPSH value (Net Positive

    Suction Head) is significant in

    assessing the suction

    characteristics of a centrifugal

    pump: It describes the minimum

    inlet pressure required by each

    centrifugal pump for reliable

    and cavitation-free operation

    [1.13]. We need to distinguish

    between the permissible

    cavitation, which causes the

    developed head of the pump to

    drop by 3 percent (also referred

    to as NPSHr = required) and the

    NPSH value of the system (also

    referred to as NPSHa =

    available).

    Cavitation-free pump operation

    generally requires the following

    condition to be met:

    The safety allowance is defined in

    accordance with ATV (German

    Association for Water, Waste

    Water and Waste) and HI

    (Hydraulic Institute) as 30 % of

    NPSH3% of the pump. NPSHa can

    be calculated using equation (10a).

    NPSHa ^ NPSHr , NPSHr = NPSH3% + safety allowance

    (9)

    NPSHa = ze + + - HI

    pe + pb - pD

    g 2 gve

    2

    (10a)

    This equation can be simplified

    for an open system installed at

    altitudes up to 3300 ft AOD and

    a fluid temperature of 86 F:

    NPSHa = ze + 10 m

    (10b)

    To be able to document the

    NPSH3% value of a pump in the

    sales literature, pump manufac-

    turers conduct a test run in a test

    field using a special dry pump

    installation. In a wet installation

    this NPSH value is

    practically impossible to measure.

    As the NPSH3% value changes

    in relation to the flow rate it is

    entered as a function of the

    flow rate NPSHr = f(Q). This

    value describes the pressure head

    in meters or feet required above

    the vapor pressure of the fluid

    at the impeller inlet (reference

    point for NPSH = intersection

    of pump shaft axis and the

    perpendicular plane through

    the extremities of the vane

    leading edge, sometimes

    referred to as the impeller eye,

    see Fig. 1.3).

    PS'

    PS'

    PS' PS'PS' PS'

    Fig. 1.3: Position of the reference point Ps for various impeller types (Source: KSB publication Selecting Centrifugal Pumps)