- Safety
- Reliability of operation
- and leak tightness of pressure systems
- Also The last physical quality test in the fabrication process
Nomally two methods for pressure testing: hydrostatic and pneumatic, are widely used in process industry.
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Hydrostatic Testing
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Pneumatic Testing
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Test pressure is normally 30% higher than the design pressure
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Test pressure is normally 10% higher than the design pressure
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Recommended for high pressure applications
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Recommended only for low pressure applications
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Test media (Water) used is not compressible by pressure application
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Test media (Air) used is compressible by pressure application
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Energy stored per unit volume of water under test pressure is very negligible
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Energy stored per unit volume of compressed air under test pressure is very high
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Needs thorough cleaning after test to
eliminate moisture especially for service which are reactive to moisture / fluids
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Easy to clean after testing
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Pressure Relief devices are recommended to control sudden increase in pressure during testing
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Pressure relief devices are must during test to ensure no over pressurisation
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Chances of equipment/ Pipe / test apparatus
failures are very low
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Chances of equipment/ Pipe / test apparatus
failures are high
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Weight of equipment along with test medium as
water is high hence special attention should be given to floor and supporting arrangements
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Weight of equipment with test medium
as air is comparatively less
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Needs verification and examination of joints and connections before testing
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Needs very careful checking of weld joints thoroughly before testing
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Test media can be reused or transferred to other place after testing
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Test media can not be reused or transferred to other place after testing
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Skilled and semi skilled personnel can carry out the test
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Needs involvement of senior experienced staff to monitor the test.
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Recommended where large volumes are to be tested at same time (example pipe lines )
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If pipe lines are tested should be done with small segmental lengths at a time.
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Damages made by failures are less compared to failures in pneumatic testing
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Damages made by failures in testing are very huge and extensive
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Hydrotest is a regular day to day practice and safe procedure and it can be followed in any work site
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Needs special attention and safety precautions
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Pressure changes finite amount by infinitesimal change in volume |
Pressure change proportional to volume change |
- Supply & disposal of water, disposal of fluid additives
- Water leak can cause equipment damage
- Freeze susceptibility
- Structural support limitations
- Contamination
- Operational impacts – process contaminant
- Affect dry-out of internal refractory linings
- When the systems are designed in such a way thet it cannot be filled with water.
- When the systems are such that it is to be used in services where traces of the testing medium cannot be tolerated.
Using a pneumatic test instead of hydrostatic requires approval from proper authority or body.
Test Pressure:
Pt=minimum test gauge pressure
Pd=internal design gauge pressure
St=allowable stress value at test temperature
Sd=allowable stress value at design temperature.
The maximum allowable value of St/Sd is 6.5The pneumatic test pressure shall be as per the following equation: Pt=1.1*PdNormal Basis for Test Method Selection:
Normally the following basis is followed in process piping industry for selection of hydro or pneumatic tests.
- If the fluid handled by piping system is liquid then the pipe must be hydrotested.
- If the fluid handled is vapour or gas then the internal design pressure dictates the testing method. For pipe design pressure 10 bar and above the pipe is hydrotested. For pipe design pressure below 10 bar pipe is pneumatically tested.
- If fluid handled is stream then hydrotesting is suggested.
- If fluid handles is two-phase flow then hydrotesting is suggested. However for big size flare headers pneumatic testing is performed.
- The tower overhead lines which are normally hydro tested shall be decided by stress engineer group whether to hydro test after erection or at grade, based on the capacity of standard clip available as per engineering specification for pipe supports.
- During hydrotest in case of big bore it should be decided first that line is to be hydrotested on rack or grade if hydrotest is done on rack , hydrotest load should be considered in case of vapour lines while providing structure / rack loading information.

Hi,
Thanks for providing valuable information on hydrotest and pneumatic test. One of the questions I had on my current project is that we are buying Stainless Steel inline instruments on Carbon steel lines. Also it is noticed that the hydrotest pressure on such lines is calculated based on corresponding operating pressure for Stainless steel material at that temperature.
My opinion is that by doing so we are derating the hydrotest pressure for carbon steel and are not testing it to the required pressure. Is it ok to do so.
Please provide your feedback.
Regards,
Vinay
Very good and explained.
Thanks.
This is very good article about Hydro Test and Pneumatic test in Piping.
Thanks
Very good article but comparison table shows hydrostatic test = 30% higher than design pressure when it should read 50%
i.e. Pt=1.5*Pd*(St/Sd)
thanks
Where did this 1.3Pd came from?
Very very useful for piping beginners and stress engineers. Its look like a Google for piping learners. Thanks
Very clear. Table is very quick reference.
Hi there,
what will be the load cases we will be using for pressure test in case of FLARE SYSTEM .
Normally Flare lines are not hydrotested.
Check the project document.
If pneumatically tested then separate load case is not required.
If hydrotested then same load case (WW+HP)—HYD need to be prepared what you make for other systems.
Nozzle is getting fail in hydro Case. Almost 15 times the allowable. What could be the reason behind it? Burdon effect is activated.
Hydro Pressure is OK. Thickness of Pipe is OK. Units are OK.
Any other reason ?
Please let me know the reason of multiplying St/Sd.
Please let me know the detail of that equation.
Can you please explain how to calculate the energy stored in piping due to pneumatic pressure?
Very informative article!! Thank you.
Stored energy in a pipe during Pneumatic testing :
The process inside the system is assumed as adiabatic compression.
As per the ideal Gas equation-
PV= mRT
Where
P= Pressure
V= Volume
m= Mass of Gas
R= Gas constant
T=Temperature of the Gas
Work done in an adiabatic compression = mCv DT
= mCv (T2-T1) Constant Volume process
=R/( -1) m (T2-T1)
=R/( -1) mT2( 1-T1/(T2 )) mT2= P2V2/R – Ideal gas equation
=R/( -1) P2V2/R {1-( V2/V1) (-1)}
=R/( -1) P2V2/R {1-( P1/P2) (-1/)} as per adiabatic equation PV = C
= P2V2/(-1) {1-( P1/P2) (-1/)}
Where
P2= Test pressure(abs)….psi
V2=Volume of the pipe (Total Volume under test pressure)….m3
= Ratio of specific heat for the test fluid (gamma)
P1=Abs Atmospheric pressure….psi
This formula is similar to the one given by the ASME standard ASME-PCC-2-2008 regarding the energy calculation in its Article No. -5.1, Mandatory Appendix II.
what is the minimum air pressure test for pipes for bs 1387 pipes
All water piping shall be tested to hydro-static test pressure of at least one and a half times the maximum
operating pressure but not less than 10 kg/sq cm for a period of not less than 24 hours. Why 24 hours is required?
We have situation where a Discharge Pipe for an LPG storage bullet (pressure vessel) is encased (sleeved) inside a larger diameter pipe. The weld joint connecting the discharge line to the bullet is a golden weld (GW). Our project Spec does not allow GW. However this GW is located inside a larger diameter pipe sleeve which is welded to the bullet at one end and to the discharge pipe at the other end. The sleeve pipe can be tested (pneumatically) to the same required test pressure for the Discharge Pipe. My question is as follow: If we pneumatically test the sleeve pipe to the same test pressure of the Discharge Pipe, which in turn will be subjecting the GW joint on the Discharge Pipe to external test pressure, can this be considered a substitute to subjecting the Discharge Pipe GW to internal pneumatic pressure testing? Your reply will be much appreciated.
Can u give some information about pressure relief device that at what pressure and at what pipe dia we should use pressure relief device