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Suction Lift With Non-Selfpriming Centrifugal Pumps

When handling water at temperatures below 100C ie. chilled or cold water services, the available inlet pressure Herf at the pump suction port will become of negative value.

That means that the local atmospheric pressure pb is higher than the sum of net positive suction head HH and vapour pressure pv; the inlet pressure is thus no longer required. This interrelation is based on the drastic reduction of the vapour pressure of cold water. In practice, that means:

Pumps operating at a negative minimum inlet pressure Herf are capable of creating a suction lift (not self-priming).

The suction capacity is approximately equal to the level of the negative minimum inlet pressure minus 1m safety factor.

As pumps normally used in conjunction with building services are generally not of selfpriming characteristics, the following conditions for suction lift operation must be met:

  • Filling and venting of the suction-side pipework including the pump before commissioning.
  • Avoiding air entrainment during pump operation (aeration will result in break-down of suction capabi-lity).
  • Avoiding drainage of suction-side piping on standdown of pump by providing and installing a footvalve
  • (Danger of leakage due to dirt particles).


Reliance on non-return valves in the discharge pipe is not sufficient, as air can be entrained by way of the shaft seal (mechanical or packed gland seals) on pump standdown.

The suction capability of non-selfpriming pumps is, on account of their construction features, generally limited to the range of max. 2 to 4 m. Higher suction lifts (max. 8 to 9 m) and selfpriming operation require the use of Special Pumps.



Also see:
Avoiding Cavitation
Cavitation
Self-Priming Centrifugal Pumps
Working Pressure







Subject area PUMP TYPES


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