AutoEngCalc - Engineering Calculators

Pump Sizing Calculator

Centrifugal and positive displacement pump selection and performance analysis

3 Pump Analysis Tools

Featured: Hydraulic power calculation, NPSH analysis, and affinity laws

Pump Basic Parameters

Calculate hydraulic power, shaft power, and motor power requirements

[Pump diagram will appear here]
Visual representation based on input parameters

Power Results

Hydraulic Power: - kW
Shaft Power: - kW
Motor Power: - kW
Motor Power (with SF): - kW

NPSH Analysis

Calculate Net Positive Suction Head available and required to prevent cavitation

[NPSH diagram will appear here]
Visual representation of suction conditions

NPSH Results

NPSH Available: - m
NPSH Required: - m
NPSH Margin: - m
Status: -

Affinity Laws

Calculate pump performance at different speeds or impeller diameters

Pump Performance Curve

Enter parameters to view pump curve

Performance Results

New Flow Rate: - m³/h
New Head: - m
New Power: - kW
Change Factor: -

Pump Theory Reference

Hydraulic Power Calculation

Hydraulic power (Ph) is calculated as:

Ph = (ρ × g × Q × H) / (3.6 × 106)

Shaft power (Ps) is calculated as:

Ps = Ph / ηpump

Where:
ρ = fluid density (kg/m³)
g = gravitational acceleration (9.81 m/s²)
Q = flow rate (m³/h)
H = total head (m)
ηpump = pump efficiency (decimal)

Affinity Laws

For speed changes (N1 to N2):

Q2 = Q1 × (N2/N1)

H2 = H1 × (N2/N1)2

P2 = P1 × (N2/N1)3

For impeller diameter changes (D1 to D2):

Q2 = Q1 × (D2/D1)

H2 = H1 × (D2/D1)2

P2 = P1 × (D2/D1)3

These laws are approximations and become less accurate with large changes (>20%)

NPSH Calculation

Net Positive Suction Head Available (NPSHA):

NPSHA = (Ps - Pv)/(ρ × g) + hs - hf

Where:
Ps = suction pressure (Pa)
Pv = vapor pressure (Pa)
hs = static head (m)
hf = friction losses (m)
ρ = fluid density (kg/m³)
g = gravitational acceleration (9.81 m/s²)

Pump Selection Tips

  • Select pump for 10-20% higher than design flow
  • NPSHA should exceed NPSHR by at least 0.5m
  • Best efficiency point (BEP) should be near normal operating point
  • Consider system curve when selecting pump

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