Booster Pump Calculation Excel Review

#EngineeringExcel #PumpSizing #HydraulicCalculations #BoosterPump #ExcelForEngineers

TDH = H_geo + H_friction + (P_discharge - P_suction) * 10.2

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. booster pump calculation excel

(Note: 10.2 converts bar to meters of water)

| Parameter | Unit | Description | Typical Value | | :--- | :--- | :--- | :--- | | Flow Rate (Q) | m³/h or GPM | Peak demand (fixture units, sprinkler heads, etc.) | Variable | | Suction Pressure (P_suction) | bar or psi | Pressure available at pump inlet (from city main or tank) | 2.5 bar | | Required Discharge Pressure (P_discharge) | bar or psi | Pressure needed at the highest/farthest fixture | 4.0 bar | | Elevation Difference (H_geo) | m or ft | Vertical distance from pump to highest point | 25 m | | Pipe Length (L) | m | Total length of the longest run | 150 m | | Pipe Diameter (D) | mm or in | Nominal bore | 80 mm | | Friction Factor (f) | dimensionless | Darcy-Weisbach or Hazen-Williams C-factor | 0.02 (or C=130) | A booster pump isn’t just a "water pusher

NPSHa = P_suction*10.2 - H_vapour - H_suction_friction

| Parameter | Formula | Excel Example | | :--- | :--- | :--- | | Hydraulic Power (P_h) | Q (m³/s) * TDH (m) * ρ * g | = (Q_m3h/3600) * TDH * 1000 * 9.81 | | Shaft Power (P_s) | P_h / Pump Efficiency (η_p) | = P_h / 0.75 (for 75% efficiency) | | Motor Power (P_m) | P_s / Motor Efficiency (η_m) | = P_s / 0.92 | Use XLOOKUP or INDEX-MATCH

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.

A booster pump isn’t just a "water pusher." It is the critical component that ensures adequate pressure and flow in water supply systems—from high-rise buildings and industrial plants to irrigation networks. Under-sizing leads to low pressure at fixtures; over-sizing leads to energy waste, premature wear, and cavitation.

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: