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Cold and Hot Testing / Calibration of PSVs

02/15/2010 12:05 AM

We have several PSVs installed on steam and air pipe lines at a manufacturing site, which are to work or to blow off at different pressures.

But when we calibrate them on our test bench that uses water at normal temperature, the results are very diffrent. Is there any factor that need to be catered for when calibrating PSVs using water but their operating fluids be different?

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#1

Re: Cold and Hot Testing/Calibration of PSVs

02/15/2010 11:42 AM

This is an excerpt from ASME Section VIII, Division 1, 1992 Edition, Pressure Relief Devices, Section UG-136, Subsection (d):

(4) Each valve shall be tested to demonstrate its popping or set pressure. Valves marked for steam service or having special internal parts for steam service shall be tested with steam, except that valves beyond the capability of the production steam test facility either because of size or set pressure may be tested on air. Necessary corrections for differentials in popping pressure between steam and air shall be established by the manufacturer and applied to the popping point on air. Valves marked for gas or vapor may be tested with air. Valves marked for liquid service shall be tested with water or other suitable liquid. Test fixtures and test drums where applicable shall be of adequate size and capacity to ensure that valve action is consistent with the stamped set pressure within the tolerances required by UG-134(d).

(5) A seat tightness test shall be conducted at a maximum expected operating pressure, but at a pressure not exceeding the reseating pressure of the valve. When testing with either water or steam, a valve exhibiting no visible signs of leakage shall be considered adequately tight. Leakage tests conducted with air shall be in accordance with industry accepted standards.

(6) Testing time on steam valves shall be sufficient, depending on size and design, to insure that test results are repeatable and representative of field performance.

I have performed quality control surveillance, verification, and inspection activities for set point testing in nuclear power plants where this function is taken very seriously. I don't believe there is a test method that allows the use of noncompressible fluid to certify set pressure for safety valve. I'd check with the manufacturer for assistance.

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#2

Re: Cold and Hot Testing / Calibration of PSVs

02/16/2010 2:17 AM

Dear all,

From Crosby Engineering Handbook;

cold differential test pressure -(CDTP) the inlet static pressure
at which a pressure relief valve is adjusted to open
on the test stand. This test pressure includes corrections
for service conditions of superimposed back pressure
and/or temperature.

Is anybody knows how to calculate correction factors?

Regards,

Eyup Tan

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Anonymous Poster
#3
In reply to #2

Re: Cold and Hot Testing / Calibration of PSVs

02/16/2010 9:22 AM

The correction for temperature given by Crosby is as follows.

operating temp VS % excess pressure

0-150F ---------none

151-600F------- 1%

601-800-------- 2%

801-1000F------ 3%

As an example if the relief valve is to to open at 100.0 PSIG while installed on a process running at say 805F,you will test and adjust it on the bench to lift at 103.0 Psig.

This adjustment is only to compensate for the difference between the operating and testing temperature.

As mentioned in the previous answer there are adjustment for back pressure if the valve is NOT a balanced bellow valve.

Also for liquid service you need to adjust for the elevation of the relief valve compared to the equipement it is protecting.Say a liquid relief vave is to protect a line from going above 100.0 Psig and the relief valve is mounted 20.0 Ft above the line it is protecting.

If you set the relief valve at 100.0 psig on the bench the relief valve will not open when the line pressure is 100.0 psig,because the pressure at the relief valve would be 100-(20/2.307) PSI.

In this case you will set at the bench to a value =91.3 PSIG.

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