| Output Parameter | Value | Unit | Status | | :--- | :--- | :--- | :--- | | Total Dynamic Head | 52.3 | m | ✅ OK | | Flow Rate | 50 | m³/h | ✅ OK | | NPSHa | 4.2 | m | ✅ > NPSHr (3.7 m) | | Required Motor Power | 11 | kW | Select 11 kW / 15 HP | | Velocity | 2.1 | m/s | ⚠️ High (limit 2.0 m/s) |
TDH = H_geo + H_friction + (P_discharge - P_suction) * 10.2 booster pump calculation excel
(Note: 10.2 converts bar to meters of water) | Output Parameter | Value | Unit |
Q_m3h = 50 [m³/h] Q_m3s = Q_m3h / 3600 D_m = 0.08 [80 mm] Area = PI() * (D_m/2)^2 v = Q_m3s / Area f = 0.02 (assume clean steel pipe) L = 150 g = 9.81 H_friction = f * (L / D_m) * (v^2 / (2*g)) Create a lookup table for f based on pipe material and Reynolds number using the Moody chart. Use XLOOKUP or INDEX-MATCH . 2.3 NPSH Available (Net Positive Suction Head) – The Cavitation Check Cavitation destroys pumps. Always calculate NPSHa: Always calculate NPSHa: NPSHa = (D10*10
NPSHa = (D10*10.2) - 0.34 - H_friction_suction Condition: NPSHa must be > NPSHr (from pump curve) by at least 0.5 m. Once you have TDH and Q, calculate hydraulic, shaft, and motor power.
Cell A10: Elevation (m) = 25 Cell B10: Friction Loss (m) = Calculate per 2.2 below Cell C10: P_discharge (bar) = 4.0 Cell D10: P_suction (bar) = 2.5 Cell E10: TDH (m) = A10 + B10 + (C10 - D10)*10.2 This is where Excel shines for iterative design.