11.5 Minimum inlet pressure
The minimum inlet pressure "H" in metres head
required during operation to avoid cavitation in the
pump can be calculated from the following formula:
H
= p
x 10.2 - NPSH - H
b
p
= Barometric pressure in bar.
b
(Barometric pressure can be set to
1 bar.)
In closed systems, p
system pressure in bar.
NPSH = Net Positive Suction Head in metres
head (to be read from the NPSH curves
on pages 22 to 24 at the highest flow the
pump will be delivering).
H
= Friction loss in suction pipe in metres
f
head.
H
= Vapour pressure in metres head.
v
See fig. 18, page 25.
t
= liquid temperature.
m
H
= Safety margin = min. 0.5 metres head.
s
If the calculated value of "H" is positive, the pump
can operate with a maximum suction lift of "H"
metres.
If the calculated value of "H" is negative, a minimum
suction head of "H" metres is required during
operation to avoid cavitation.
Example
p
= 1 bar.
b
Pump type: CM 3, 50 Hz.
3
Flow rate: 4 m
/h.
NPSH (from fig. 14, page 22): 3.3 metres head.
H
= 3.0 metres head.
f
Liquid temperature: 90 °C.
H
(from fig. 18, page 25): 7.2 metres head.
v
H = p
x 10.2 - NPSH - H
b
H = 1 x 10.2 - 3.0 - 3.3 - 7.2 - 0.5 = -3.8 metres head.
This means that a suction head of 3.8 metres is
required during operation.
Pressure calculated in bar: 3.8 x 0.0981 = 0.37 bar.
Pressure calculated in kPa: 3.8 x 9.81 = 37.3 kPa.
11.6 Maximum inlet pressure
The actual inlet pressure plus the pressure when the
pump is operating against a closed valve should
always be lower than the maximum system pressure.
- H
- H
f
v
s
indicates the
b
- H
- H
[metres head].
f
v
s
17