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FK 40 - Tri-Canada

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Pump technology<br />

terms<br />

NPSH value [m]<br />

NPSH value of the<br />

pump<br />

NPSH value of the<br />

plant<br />

Thus the calculated Reynolds number is:<br />

The Reynolds number exceeds the critical Reynolds number Re =2320. The flow is turbu-<br />

krit<br />

lent.<br />

NPSH is the abbreviation for Net Positive Suction Head<br />

Besides the flow rate Q and the pump head H, the NPSH value is one of the most important<br />

characteristic parameter of a centrifugal pump.<br />

The NPSH value of the pump depends on the design and speed of the pump. The higher the<br />

speed of the pump, the higher the NPSH value will be.<br />

The NPSH value is measured on a pump test stand and cannot be modified without supplement<br />

ary means.<br />

The NPSH value of the plant depends on the loss of head including the losses in fittings<br />

and apparatus in the line of the plant, and should be always checked by calculation.<br />

p = E pressure at the inlet cross section of the plant [bar]<br />

p = A pressure at t he out let cross section of t he plant [bar]<br />

p = D vapour pressure of the f luid at t he middle<br />

of t he suction connection of t he pump [bar]<br />

p = b air pressure at t he inst allation site of t he pump<br />

[bar]<br />

H = VS loss of head of t he suction line, f rom t he inlet<br />

cross section of the plant t o t he inlet cross<br />

section of t he pump [m]<br />

H = geodetic suction height (negative, in case of<br />

sgeo<br />

f looded suction) [m]<br />

ρ = density of the fluid [kg/m≈]<br />

v = E inlet flow velocity [m/s]<br />

NPSH =<br />

p + p - p<br />

ρ× g<br />

+ v ≤<br />

2g<br />

E b D E<br />

+ H - H<br />

sgeo VS

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