Glossary

Pressure surge

A pressure surge is a short-term change in pressure caused by rapid changes in flow conditions, for example when valves or pumps are operated.

Also
Hydraulic transient · Surge pressure · Fluid transient
Also known as
  • Hydraulic transient
  • Surge pressure
  • Fluid transient
01

How a pressure surge arises

Flowing fluid carries kinetic energy. If it is suddenly slowed or accelerated – by a closing valve, a tripping pump, a slamming check valve – that energy is converted into pressure. The pressure change travels through the line as a wave at the speed of sound and is reflected at vessels, branches and closed ends.

Pressure surge is the general term for such events. In liquid lines it is also called water hammer; in steam lines, slugs of condensate can cause similarly violent impacts.

02

The Joukowsky equation

The magnitude of the surge for an instantaneous change in velocity is given by the Joukowsky equation: Δp = ρ · a · Δv, where ρ is the density of the fluid, a the wave speed in the pipe and Δv the change in flow velocity.

An example: water at 1000 kg/m³, a wave speed of 1000 m/s and a velocity change of 2 m/s give 2,000,000 Pa – that is, 20 bar on top of the operating pressure. The wave speed depends on the fluid, the pipe material and the wall thickness; in steel pipes carrying water it is in the order of 1000 m/s, in plastic pipes considerably lower.

03

The reflection time decides

Whether the full Joukowsky surge occurs depends on the closing time. The pressure wave runs from the valve to the nearest reflection point and back; this takes the reflection time 2 · L / a, with L as the length of the line. If the valve closes faster, the full surge develops. If it closes much more slowly, the returning wave already relieves the pressure while closing is still in progress.

Long lines are therefore more sensitive than short ones: a closing time that is harmless over twenty metres can trigger the full surge over two kilometres.

04

What the surge does to the line

The pressure peak loads the pipe wall – that is the obvious part. The more dangerous part is often the force on the line itself: while the wave passes through a straight section between two elbows, the pressure at the two ends differs. The difference acts as an unbalanced force along the pipe axis, displaces the line and loads supports and anchors.

Verification takes two steps: a fluid transient calculation provides pressure against time, and a dynamic structural analysis derives stresses and support loads from it.

05

Limiting pressure surges

The most effective measure addresses the cause, not the consequences.

  • Lengthen valve stroking times or close in stages.
  • Start and stop pumps under control; flywheels extend the run-down.
  • Select check valves that close before reverse flow sets in.
  • Place air vessels or surge vessels close to the source.
  • Provide vacuum breakers against sub-atmospheric pressure and column separation.

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Overview

Causes of pressure surges and countermeasures

Cause What happens Countermeasure
Fast-closing valve Flow is stopped abruptly Longer or staged closing time
Pump trip Flow collapses, low pressure downstream of the pump Flywheel, air vessel, vacuum breaker
Check valve slam Reverse flow is stopped instantly Fast-closing type, damping
Start-up against an empty line Liquid front hits an obstruction Fill slowly, vent
Condensate in a steam line Slug is carried along or a steam pocket collapses Drain, warm up slowly
Frequently asked questions

Frequently asked questions about Pressure surge

Above which closing time is a valve uncritical?

There is no fixed figure. The closing time has to be well above the reflection time 2 · L / a; how far above depends on the valve characteristic, because many valves only really throttle the flow over the last part of their stroke.

Does the design pressure cover a pressure surge?

Only if the surge was taken into account when it was set. The codes allow limited margins for short-term excursions; the forces on supports are not covered by the design pressure in any case.

Can pressure surges also occur in gas lines?

Yes, but because of the low density the pressure changes are much smaller. More critical there are the reaction forces when safety valves lift, and liquid slugs carried along by the gas.

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