#EngineeringExcel #PumpSizing #HydraulicCalculations #BoosterPump #ExcelForEngineers
Download a template or build one using the formulas above. Test it against a known installed pump. Refine it with your local pipe material data. Then use it on every project. Have you built your own pump sizing spreadsheet? What’s the most useful feature you’ve added? Let’s discuss in the comments. booster pump calculation excel
Use data validation dropdowns for units (e.g., m vs. ft) and apply CONVERT functions to standardize all inputs to SI or US customary internally. Part 2: Key Calculations (The Engine of Your Spreadsheet) In a hidden or dedicated column, perform these critical steps. 2.1 Total Dynamic Head (TDH) – The Master Formula The pump must overcome three things: elevation, friction, and velocity head (usually negligible). The core Excel formula for TDH (in meters of water column) is: Then use it on every project
| 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) | Let’s discuss in the comments
NPSHa = P_suction*10.2 - H_vapour - H_suction_friction
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:
H_friction = f * (L / D) * (v² / (2*g))