Guides

When piping vibrates: identifying causes and remedying them deliberately

A pipe must be able to move when the temperature changes. At the same time it must not be excited to unacceptable vibration by pumps, pressure fluctuations or flow-induced forces. Herein lies an important conflict of objectives in piping design: what is favourable for thermal flexibility can be unfavourable from the point of view of vibration. Piping vibration is more than a noise problem. Repeated loading can cause fatigue cracks and leaks. A systematic assessment is therefore useful not only when designing new plant but also for modifications, changed operating conditions and anomalies in existing plant. The decisive question is not only “How do we hold the pipe in place?” but first of all “What is exciting it to vibrate?”

Author
Dr.-Ing. Philipp Schwittek
Reading time
10 minutes
Updated
04. October 2026
When piping vibrates
When piping vibrates
The key points
  • Mobility alone does not produce sustained vibration. Only an excitation, that is a supply of energy, sets the system in lasting motion; resonance can amplify the response considerably.
  • Thermal flexibility and vibration behaviour must be considered together. As few supports as possible is no more a universal solution than fixing the pipe as rigidly as possible.
  • The cause is not always a machine. Flow, pressure let-down, cavitation and valves operating unstably can also trigger vibration.
  • Countermeasures must suit the mechanism. Depending on the cause, operational changes, modified supports or targeted damping come into consideration. A thermal pipe stress analysis alone does not replace a dynamic investigation where one is required.
01

Why thermally flexible piping can be susceptible to vibration

Mobility is necessary – but not in every direction.
Anyone who considers a pipe solely with regard to its thermal expansion will often provide sufficiently long pipe legs and movements that are restrained as little as possible. This reduces thermal restraint forces. On a line subject to vibration, however, the same properties can be unfavourable: long unsupported sections and flexible supports can encourage dynamic movements.

The design objective should therefore not be “as many degrees of freedom as possible” but: permit the thermal movements that are required and deliberately limit unwanted dynamic movements.

These requirements need not be mutually exclusive in principle. There are, for example, pipe support concepts that allow thermal sliding and at the same time ensure a defined, vibration-reducing support. What matters are the actual design and the behaviour of the support arrangement as a whole.

What determines the vibration behaviour?
A pipe has natural frequencies and associated mode shapes. These describe the frequencies at which, and the patterns of movement in which, the system preferentially vibrates. Pipe dimensions, routing, masses and the arrangement and stiffness of the supports influence these properties. An additional valve or a modified support can therefore change the behaviour.

If a matching excitation acts close to a natural frequency, resonance can occur. Particularly with low damping, large vibration responses can then develop. Resonance is not the only cause of critical movements, however: sufficiently strong shock-like or broadband excitations can also be problematic.

An excitation need not be visible from outside
A single disturbance can cause the pipe to ring down. For sustained vibration, by contrast, energy must be supplied continuously. This energy can come from a machine, but equally from the flow or from an interaction between valve, pressure and flow rate.

One example is a chattering safety valve: unfavourable pressure conditions can trigger repeated opening and closing. The vibration then arises from the interaction of plant and valve – not from a periodic impulse imposed from outside.

02

What can cause piping vibration?

Pumps and vibrating machines are the obvious suspects. For a sound root cause analysis, however, the flowing fluid must also be considered.

Small connections deserve particular attention
The largest pipe section is not always the critical point. Small, cantilevered branches with valves or instruments can react sensitively to the movement of the main line. The connection areas and welds in particular must then be considered with regard to their fatigue loading.

A small nominal size is therefore no reliable argument against a vibration assessment.
The number of load cycles is also easily underestimated: a vibration with ten complete cycles per second already causes 36,000 cycles in one hour. This simple count is not yet a fatigue life verification, but it illustrates the difference from a few thermal start-up and shutdown cycles. Further causes:

  • Pumps, compressors and other machines - Mechanical movements can be transmitted via connections and supporting structures. In addition, machines generate pressure fluctuations in the fluid; in centrifugal pumps, for example, through the interaction between impeller vanes and flow.
  • Turbulent flow - At bends, branches or partially closed valves, fluctuating flow forces arise. These can excite the piping system without any conspicuously vibrating machine being present.
  • Cavitation - When vapour bubbles form and collapse in a liquid, noise, pressure fluctuations and damaging loads can occur. Both pumps and valves can be affected.
  • Valves operating unstably - Flutter or chatter can arise from unfavourable operating and pressure conditions. With safety valves, for example, the pressure losses of the inlet and outlet lines play a part.
  • Acoustic excitation during gas let-down - Large pressure let-downs at control or relief valves can generate high-frequency acoustic energy. This can cause local vibration of the pipe wall and high loading at welded-on details.
  • Two-phase and slug flow - Liquid slugs and changing flow regimes can produce considerable dynamic forces. Such excitations need not occur regularly or at a constant frequency.
  • Condensate and water hammer in steam systems - Unfavourable pipe routing, condensate accumulation or inadequate drainage can trigger sudden impact loads. The cause then often lies in the system layout and not solely in the component affected.
  • Pump switching and rapid valve movements - Rapid changes in flow velocity generate pressure waves. These can load pipes, valves and supports dynamically.
  • Acoustic resonances in side branches - Branches with no flow through them can also be excited acoustically under certain conditions. This can result in pressure pulsations and fluctuating forces in the piping system.
03

Countermeasures: understand first, then change

Before any design change, it should be clarified under which conditions the vibration occurs: permanently or only during start-up, at a particular speed, after a valve movement or only at a particular throughput?

For the investigation, it is not only visible deflections that are of interest. Depending on the task, vibration velocity, acceleration or strain are recorded and matched with the operating condition. By combining measured data and calculation model, the loading of critical connection areas can be assessed more precisely.

In the case of new, severe vibration, lines that are hammering, visible damage or leaks, the safe assessment of the operating condition takes priority first. Changes should not be made by improvised clamping or uncontrolled operating trials.

Our approach is to examine first whether an improvement at the cause is possible.
With pressure surges, for example, adapted switching sequences or suitable valve closing characteristics can be part of a solution. Which measure is suitable depends on the hydraulic system as a whole; a sequence that is merely slower or faster is not automatically right.

If the excitation arises at a control valve, its selection and operating conditions should be examined. With large pressure drops, valve trims and pressure reduction concepts designed for the purpose may be required. Cavitation or flow-induced excitation cannot be reliably remedied by fixing the downstream pipe more firmly.

On steam lines, by contrast, slope, drainage and condensate removal are possible starting points. An additional support does not eliminate a condensate accumulation.

A change in the mode of operation can be the simplest solution – but it is only suitable if process requirements, permissible operating ranges and safety functions continue to be met. Settings on safety devices are not parameters that may be freely changed for optimisation.

If the excitation cannot be reduced sufficiently, modifying the supports comes into consideration. This can include additional supports, shorter unsupported pipe sections or a stiffer connecting structure.

It is not enough to consider the pipe clamp alone: an effective support also needs a sufficiently stiff load path into the load-bearing steelwork or the building. The position of the support must suit the governing mode of vibration.

At the same time the thermal movement required must be preserved. A suitable support can, for example, control one direction of movement without preventing all longitudinal displacement. Manufacturers also offer pipe supports specifically matched to thermal sliding and vibration limitation for this purpose.

More stiffness is one possible measure but not an end in itself. It must be checked whether the dynamic response improves and which additional forces arise in the hot operating condition.

Dampers act at a different point: they extract energy from the vibrating system.
Viscoelastic pipe dampers convert kinetic energy into heat and can thereby reduce resonant vibration in particular. For selection, travel, frequency range, temperature and the connection to a suitable abutment, among other things, are decisive. The dampers described do not replace a static weight support.

A distinction must be made between these and shock arrestors, or snubbers. These permit slow thermal movements with little resistance and provide an approximately rigid connection during rapid movements. They thus serve above all to limit dynamic events; their suitability for the specific loading must be checked separately.

Springing and damping are not the same thing either. An elastic element first of all changes the support characteristics. Whether effective vibration reduction is achieved with it depends on how it is tuned to the system.

A dynamic investigation should suit the question being asked. The natural frequency analysis alone does not yet provide actual operating vibrations or dynamic stresses. For that, excitation, damping and boundary conditions must also be taken into account.

Besides static analysis, ROHR2 offers, among other things, the calculation of natural frequencies and mode shapes and investigations with harmonic or time-dependent excitation. This allows suitable models to be built for assessing dynamic loads.

For high-frequency local pipe wall vibration, however, a different approach is required than for the bending vibration of an entire pipe section. An additional guide is therefore not the appropriate answer to every vibration mechanism.

After implementation, the effect should be checked under comparable operating conditions.

Frequently asked questions

Frequently asked questions about Piping vibration – causes and countermeasures

Is piping vibration always dangerous?

No. Mechanical vibration is unavoidable to a certain extent with machines and flowing fluids. What matters is which loads result from it and whether they are permissible for the specific system.

Can a pipe vibrate even though its pipe stress analysis shows nothing unusual?

Yes. A calculation for weight, pressure and thermal expansion does not automatically answer the question of loading from operational vibration. Where there are corresponding excitations, a supplementary dynamic assessment is required.

Is it enough to fit additional pipe clamps?

Not as a matter of principle. Additional supports can help but must be assessed with regard to their position, stiffness and the remaining thermal mobility. A clamp on a flexible substructure may not solve the problem.

Why does vibration sometimes occur only in certain operating conditions?

Changes in operation can alter the excitation. Pressure fluctuations in a pump, for example, depend on the flow conditions; cavitation, too, may occur only under certain conditions. The relationship between vibration and operating point is therefore an important part of the investigation.

Is there a generally permissible vibration displacement in millimetres?

A single displacement value does not permit a generally valid assessment. Geometry, frequency and the conversion of the movement into local stresses also play a part. Investigations on small pipe branches show why an assessment related to the specific component is important.

Does an existing system have to be reconsidered after a modification?

When the mode of operation, the process or the equipment is changed, it should be checked whether the vibration risk has changed. We examine new plant as well as existing plant and modifications to existing systems.

About the author

Dr.-Ing. Philipp Schwittek

Managing Director, Entracon Planungsgesellschaft mbH

Engineer with a doctorate, specialising in plant engineering, digital design and process automation – from simulation through to commissioning.

  • Sizing
  • Design
  • Plant engineering
  • Standards and safety
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