UK HQ Your time

Hydraulic Design — Surge & Water Hammer

Transient pressure analysis: the Joukowsky surge equation, pressure-wave speed and the critical time 2L/a, surge mitigation (slow valves, VFD ramps, surge vessels, air valves) and a worked valve-slam example.

ΔP=ρaΔv
Joukowsky
2L/a
critical time
Surge
protection

Surge & Water Hammer

When flow in a pipeline is stopped or started quickly — a valve slamming, a pump tripping — the moving column of water cannot stop instantly. Its momentum converts to a pressure wave that races up and down the line: water hammer. The transient pressure can be many times the steady operating pressure, bursting pipes, wrecking joints and collapsing them under the following vacuum. Every pumped main and fast-acting valve needs a surge check.

Joukowsky & Wave Speed

For an instantaneous flow change, the peak pressure rise is the Joukowsky equation:

Joukowsky surgeΔP = ρ · a · Δv   ·   ΔH = a·Δv / g

The wave speed depends on fluid compressibility and pipe elasticity, and the change is “sudden” only if it happens faster than the pipe’s characteristic time:

Wave speed & critical timea = √[ (K/ρ) / (1 + (K·D)/(E·e)) ]   ·   tc = 2L/a

Designing the Transient Out

MeasureWhat it doesBest for
Slow-closing / actuated valvesExtend closure beyond 2L/a so the surge is “slow”Most pumped mains
Soft starters / VFD rampsRamp pump speed so Δv is gradualPump start/stop transients
Surge / air vesselsCushion the column with a gas pocketLong high-energy mains
Air-release / vacuum valvesAdmit air to prevent column separation & collapseProfiles with high points
Flywheels on pumpsAdd inertia so a trip decelerates slowlyPump-trip protection

How Big Is the Surge?

Worked example: valve-slam surge

Steel main, L = 800 m, wave speed a ≈ 1200 m/s, flow velocity v = 1.8 m/s suddenly stopped (Δv = 1.8 m/s).

tc = 2L/a = 2×800/1200 = 1.33 s → closure faster than this is “sudden”
ΔH = a·Δv/g = 1200×1.8/9.81 = 220 m (≈ 21.6 bar) of surge head
A 220 m transient on top of operating head would burst most pipework — so the valve must close over ≥ ~10× tc (or a surge vessel is fitted). Wall thickness for the rated pressure is then confirmed against the hoop-stress method in the Pipeline Design Guide, and supports checked for the transient thrust.

Run the Numbers

Confirm wall thickness for the rated/transient pressure and support spacing for the thrust.

Related Hydraulic Design

Need this engineered for your plant?

Reynolds & Bauhm sizes pipework, pumps and valves and closes the head budget as part of a gated, fully documented bespoke design — every figure traceable from flow to fabrication.

Industries We Serve

Our expertise spans multiple industries with sector-specific water treatment solutions.