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  2. Centrifugal pump - Wikipedia

    en.wikipedia.org/wiki/Centrifugal_pump

    Centrifugal pumps with an internal suction stage such as water-jet pumps or side-channel pumps are also classified as self-priming pumps. [10] Self-Priming centrifugal pumps were invented in 1935. One of the first companies to market a self-priming centrifugal pump was American Marsh in 1938. [citation needed]

  3. Sundyne - Wikipedia

    en.wikipedia.org/wiki/Sundyne

    Sundyne Pumps also utilizes state-of-the-art inducers for low NPSH (Net Positive Suction Head) situations. Sundyne centrifugal pumps and compressors are traditionally utilized for processes requiring high-head (pumps: 6,300 ft or 1,921 m)(compressors: 4000 psi or 350 bara), and low-flow (pumps: 1,100 GPM or 250 m3/hr)(compressors: 10000 acfm or ...

  4. Centrifugal pump selection and characteristics - Wikipedia

    en.wikipedia.org/wiki/Centrifugal_pump_selection...

    Discharge Head, is the net head obtained at the outlet of a pump. For a centrifugal pump, the discharge pressure depends on the suction or inlet pressure as well, along with the fluid’s density. Thus, for the same flow rate of the fluid, we may have different values of discharge pressure depending on the inlet pressure.

  5. Net positive suction head - Wikipedia

    en.wikipedia.org/wiki/Net_positive_suction_head

    If an NPSH A is say 10 bar then the pump you are using will deliver exactly 10 bar more over the entire operational curve of a pump than its listed operational curve. Example: A pump with a max. pressure head of 8 bar (80 metres) will actually run at 18 bar if the NPSH A is 10 bar. i.e.: 8 bar (pump curve) plus 10 bar NPSH A = 18 bar.

  6. Pump inducer - Wikipedia

    en.wikipedia.org/wiki/Pump_inducer

    An inducer is the axial inlet portion of a centrifugal pump rotor, the function of which is to raise the inlet head by an amount sufficient to prevent significant cavitation in the following pump stage. [1] It is used in applications in which the inlet pressure of a pump is close to the vapor pressure of the pumped liquid.

  7. Specific speed - Wikipedia

    en.wikipedia.org/wiki/Specific_speed

    Pumps of higher specific speeds develop head partly by centrifugal force and partly by axial force. An axial flow or propeller pump with a specific speed of 10,000 or greater generates its head exclusively through axial forces. Radial impellers are generally low flow/high head designs whereas axial flow impellers are high flow/low head designs.

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