CASE26 · Water & wastewater · Pumps

Verifying inlet-pump efficiency after replacement

Five-minute and monthly operating data were used to compare wastewater throughput and electricity before and after inlet-pump replacement. Flow-normalized performance improved while the reported treatment capacity remained broadly comparable.

01 · CASE ANALYSIS

Verification challenge

Wastewater inflow changes with time, rainfall and tank level. A simple comparison of electricity totals could therefore confuse changes in pumping demand with the effect of replacement.

The PLC’s level-based unit count and pump combinations were checked before comparing flow and power at corresponding level/head conditions.

02 · CASE ANALYSIS

Data & method

The comparison used tank-level control rules, pump combinations, flow in m³/h, power in kW, one month of total inflow and electricity on each side of replacement, and five-minute data for representative maximum-inflow days.

UPI = pump electricity (kWh) ÷ treated wastewater volume (m³). Monthly and representative-day UPI were cross-checked against flow–power scatter patterns.

Reported before/after comparison
IndicatorBeforeAfterInterpretation
Monthly UPI0.076 kWh/m³0.071 kWh/m³6.8% improvement (reported)
Maximum-flow-day UPI0.078 kWh/m³0.071 kWh/m³8.9% improvement (reported)
Monthly average power211 kW167 kWDemand differed; not the savings-rate basis
Maximum throughputApproximately 5,277 m³/hApproximately 5,149 m³/hCapacity broadly maintained

03 · CASE ANALYSIS

Observed results

Monthly UPI changed from 0.076 to 0.071 kWh/m³, with a reported improvement of 6.8%. On maximum-flow representative days, UPI changed from 0.078 to 0.071 kWh/m³, with a reported improvement of 8.9%.

Average monthly power fell from 211 to 167 kW. Because average inflow differed, this power reduction was used as an operating-pattern indicator rather than the primary savings rate.

Maximum throughput was approximately 5,277 m³/h before and 5,149 m³/h after replacement under three-pump operation. The source interpreted the capacity as broadly maintained.

04 · CASE ANALYSIS

Measurement & verification

The principal finding is improved electricity per unit of treated volume within the reported comparison periods. It is not a claim of a universally applicable pump savings rate.

For longer-term M&V, account for flow, tank level/head, active units, rainfall-related inflow changes and operating time. Compare equivalent service conditions and keep PLC logic changes distinct from equipment replacement effects.

05 · CASE ANALYSIS

Engineering lesson

Pump optimization must satisfy required flow and head while reducing energy input. Parallel operation, variable speed and the actual operating point need to be evaluated as a system.

This framework also applies to water supply, process water and cooling-water systems. A future forecasting or anomaly-detection layer would be an extension rather than an observed result of this project.

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