FK 40 - Tri-Canada
FK 40 - Tri-Canada
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