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Pump & System Curves

Hydraulic Modelling — in depth

A pump runs where its curve crosses the system curve. We build both — static lift plus friction for the system, head-flow for the pump — to find the duty point, confirm it sits near best efficiency, and model variable-speed operation so the pump tracks demand efficiently across the full flow range.

Curve Analysis

What matters in practice

System Curve

Static head plus friction vs flow.

Pump Curve

Head-flow characteristic.

Operating Point

Where the curves intersect.

VSD Operation

Speed-adjusted efficient running.

Pump Curve Outputs

ItemUseNote
Duty pointSelectionCurve crossing
EfficiencyEnergyNear BEP
NPSHCavitationMargin
VSDTurndownEfficient

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Pump & System Curves: Engineering Detail

Fundamentals, design drivers and practical guidance

Pump and system-curve analysis — finding the operating point where pump and system curves meet, and optimising efficiency and variable-speed control.

Reynolds & Bauhm builds and calibrates hydraulic models for pressurised and open-channel systems, sizing pumps at their best-efficiency point, checking surge and NPSH, and proving conveyance under design conditions — so plant hydraulics are engineered, not assumed.

Hydraulic modelling underpins reliable water and wastewater conveyance: it predicts how flow, head and pressure behave through pipes, channels, pumps and structures, so a design can be proven on paper before steel and concrete commit it. Whether the question is pump selection, surge, or whether a channel will surcharge, the model turns governing equations into actionable design margins.

Pressurised networks are solved from continuity and energy, with friction losses from Darcy-Weisbach or Hazen-Williams and minor losses at fittings; the system curve so produced is intersected with the pump curve to fix the duty point. Getting this right avoids the classic failures — a pump run far from its best-efficiency point, cavitation from inadequate NPSH, or a network that cannot deliver design flow at the far node.

Design & Specification Considerations

What our engineers assess on every scope of this type

  • NPSH-available check against required to avoid cavitation
  • Best-efficiency-point operation and turndown range
  • Manning's equation and specific energy for open channels
  • Sub/super-critical regime and hydraulic-jump location
  • Freeboard and surcharge check under design storm flow
  • Continuity and energy solution of pressurised networks
ParameterTypical basisWhy it matters
RegimeFroude numberLocates jumps; sets freeboard
FrictionDarcy-Weisbach / Hazen-WilliamsSets head loss along pipes
Duty pointSystem curve x pump curveFixes flow and head delivered
NPSHAvailable > requiredPrevents cavitation damage
BEPOperate near best efficiencySaves energy, extends pump life
Open channelManning's equationSizes channel for design flow

Frequently Asked Questions

Common questions on hydraulic modelling

How is a pump duty point found?

The network's system curve — static lift plus friction and minor losses — is intersected with the manufacturer's pump curve. The crossing point gives the delivered flow and head; the design aims to place it near the pump's best-efficiency point.

What is NPSH and why does it matter?

Net Positive Suction Head available must exceed that required by the pump, or the liquid flashes to vapour and the impeller cavitates, eroding it and collapsing performance. The check is part of every pump-system analysis.

How does open-channel design differ?

It is governed by Manning's equation and specific energy rather than pressurised pipe losses, and must account for sub- and super-critical flow, hydraulic jumps and freeboard so the channel passes design storm flow without surcharging.

What makes a model trustworthy?

Calibration and disciplined inputs — realistic roughness, accurate geometry and correct boundary conditions. A model is only as good as those assumptions, which is why Pump & System Curves is built and checked against known operating data where available.

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