Pump Duty WorkbenchWastewater & water

Pumping station duty check

Example data loaded. A small foul pumping station, one duty and one standby. Replace it with your project's data. Inputs save in this browser.
Setup
All inputs shown
1
Project and fluid
2
Duty requirement

Speed below 100% applies the affinity laws to the pump curve, for VSD-controlled stations.

3
Levels and wet well

Leave average inflow blank to estimate it from dwellings (2.35 persons × 125 L/head/day + 25% infiltration). The design duty is taken at BWL, where static head is highest. If the rising main crosses a summit above the discharge level, enter it as the high point; static head is then measured to the summit.

4
Rising main
FittingKQty

Typical K values for bends, valves and the outlet are included. Tick “Detailed fittings losses” in Setup to edit them.

5
Pump branch, each pump
FittingKQty

Branch pipework and valves carry one pump's flow; the rising main carries the whole station flow.

6
Pump curve, one pump at 100%
Q l/sH mη %NPSHr m

Read 4–8 points off the manufacturer's curve, including shut-off (zero flow). Efficiency and NPSHr are optional but enable the operating range, motor and NPSH checks.

7
Suction conditions

Suction static head is BWL minus impeller eye level, flooded positive.

8
Design criteria

Pump and system curves

Station pump curve System at BWL System at TWL Efficiency Preferred operating range

Design checks

Station section

levels to scale

Hydraulic breakdown

at design duty, BWL

Friction losses use Darcy–Weisbach with the Colebrook–White friction factor and water properties at the stated temperature. Wet well volume uses V = Σ T·ΔQ/(4·n) for each pump stage, with n the number of pumps alternating. Surge uses the Joukowsky upper bound a·V/g. The pump curve is a least-squares quadratic fit through the points entered. Results support design and must be checked before issue.