Booster Pump Calculation Excel -

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:

TDH = H_geo + H_friction + (P_discharge - P_suction) * 10.2 booster pump calculation excel

(Note: 10.2 converts bar to meters of water) Q_m3h = 50 [m³/h] Q_m3s = Q_m3h / 3600 D_m = 0

#EngineeringExcel #PumpSizing #HydraulicCalculations #BoosterPump #ExcelForEngineers Always calculate NPSHa: TDH = H_geo + H_friction

H_friction = f * (L / D) * (v² / (2*g))

| 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) |