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P-200Centrifugal Pump Duty, Power and NPSH

A centrifugal pump does not deliver a flow. It delivers a relationship between flow and head, and the system decides where on that curve it lands. Get the suction wrong and none of it matters.

Cutaway — Centrifugal Pump Duty, Power and NPSH
SuctionDischarge

How it works

  1. What a pump gives you — A centrifugal pump has no fixed output. It has a curve — head falling as flow rises. Ask it for more flow and it gives you less head, whether you wanted that or not.
  2. The system curve — The pipework answers with its own curve: a fixed static head you must lift against, plus friction that grows with the square of flow. Static lift is there at zero flow; friction is nothing at zero flow and dominates at the top end.
  3. The duty point — The pump runs where the two curves cross, and nowhere else. You do not choose the flow — you choose the two curves, and the intersection chooses the flow. Close a valve and you steepen the system curve, walking the duty point up and to the left.
  4. NPSH and cavitation — The suction side is where pumps are actually killed. If absolute head at the impeller eye falls to the vapour pressure, water flashes to steam, the bubbles collapse on the vane, and the impeller erodes. Keep NPSH available above NPSH required with a metre in hand — and remember hot water leaves you far less room.
  5. What governs it — Head sets the duty point, efficiency sets the power bill, and NPSH decides whether the pump survives. Push the temperature up or the suction level down and watch the margin close: that is the number that strands installations, not the head.
  6. The end-suction pump — One impeller, one suction eye, back pull-out so the rotating element comes out without disturbing the pipework. The curve is comparatively steep — shut-off around 1.3 times duty head — which means flow changes little when system head moves. That is a virtue on a plant whose filters foul.

Design parameters

The panel opposite runs the same correlations as the P-200 design sheet, so the animation and the calculator cannot disagree. Every parameter below is live — drag one and the picture responds.

ParameterUnitDefaultRange
Pump type
TypeEnd-suction4 options
Type changes the shape of the curve and the NPSH required, not just the badge. A submerged first stage removes suction lift from the problem entirely.
Duty
Design flowm³/h12010 – 500
Static headm220 – 90
Friction at design flowm90 – 60
Pump efficiency%7230 – 88
Suction lift (−) / head (+)m1.5-7 – 8
Water temperature°C201 – 95

Open the full P-200 design sheet for the other eight inputs, all twenty-eight results with their envelopes, the six equations printed beside the numbers they produce, and a calculation record you can export and put in a design file.

Live parameters

Six of the fourteen inputs the P-200 design sheet takes.

Pump type

Type changes the shape of the curve and the NPSH required, not just the badge. A submerged first stage removes suction lift from the problem entirely.

Duty

You have an estimate. The design sheet is the justification.

This page sizes the unit on six variables and tells you whether the headline numbers land in range. That is enough to sketch with, and it stays free. What it will not do is survive a design review: it does not show you the equation behind any number, it checks the obvious limits rather than all of them, and there is nothing to file.

The P-200 design sheet runs the same physics on fourteen inputs, reports twenty-eight results against their envelopes, prints the six governing equations beside the numbers they produce, and exports the lot as a calculation record for the design file.

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