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You are here: Fluid Machinery Templates and Tutorials > Centrifugal Pump > Centrifugal Pump Tutorials > Step 4 – Calculation of NPSHr
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On completion of 5 iterations, open results_0.025_step1.csv.
Similarly, open results_0.025_step5.csv and predicted userdef.head at step5 is 371753.34 Pa. The difference between the head at step 1 and step 5 is 3.55 % which is close to 3% head loss due to cavitation.
using the relation
, where
is the Total Pressure at inlet for 3% head loss,
is the Saturation vapor pressure and
is the density.In results_0.025_step5.csv, the variable userdef.in_pt is the predicted total pressure at inlet which is 36372.8 Pa. Hence,
is calculated as shown below.
| We got, | |||
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= 36372.8 Pa | ||
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= 3610 Pa | ||
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= 998 kg/m3 | ||
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= 9.81 m/s2 |
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The calculated net positive suction head required at the pump inlet is 3.35 m for 0.025 m3/s flow rate and 2500 rpm.
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