Are you interested in learning more about Valve Pressure Test Table? Contact us today to secure an expert consultation!
The realization of safe and smooth operations of industrial processes is heavily reliant on valves performing their function with precision. Thus, valve testing ensures that these valves meet design specifications for the duration of their operational life.
Generally, valve testing simulates operating conditions in a controlled environment to ensure fit for service valves. However, testing also occurs periodically after installation in line with standard practices.
In this article, we will review common valve testing types and industry standards that offer guidelines for valve testing.
There are several types of testing to which a valve could undergo. The required test depends on the application, manufacturer standards, and customer specifications. The following sections examine common tests, an overview of their procedure, and industry guidelines.
This test involves filling a valve body with a testing fluid, which is usually water with a corrosion inhibitor. Then, technicians apply pressure over a specific period of time. The time and level of pressure varies depending on factors including the valve material, valve size, and category of pressure test. But in most cases, the pressure level is higher than the operational/working pressure of the valve. Also, the procedure for the pressure test varies depending on the type of valve in question. Generally, pressure tests aim to ascertain the integrity of the valve shell, seat, and seal against leakages due to pressure. After carrying out a test, a valve will not be accepted if the following occurs:
Common industry guidelines for pressure testing valves can be found in ASME B16.34, API 598, MSS-SP-61, API 527, and ISO . Many tests are recorded on paper wheel charts or manually, although digital options are becoming more prevalent.
Valve Test Read-out Stand, Courtesy: Axcel TSAlthough water (hydrostatic) is the most common test medium in pressure testing, some conditions require pneumatic pressure testing of valves. For pneumatic testing, air or an inert gas such as nitrogen are the preferred media. Generally, in industry, hydrostatic testing is ideal for high-pressure applications where the equipment is not moisture sensitive.
In situations where moisture can damage certain equipment usually via corrosion or alter the chemical balance in the system, pneumatic testing is recommended. Also, industry guidelines recommend the use of pneumatic testing for cryogenic and low temperature valves. This is because it is difficult to remove all water after the test. The presence of moisture in an operating system is highly discouraged. The table below highlights more of the differences between hydrostatic and pneumatic testing in line with standards and industry practices.
Hydrostatic TestingPneumatic TestingTypically, the system is pressurized to at least 1.5 times above the maximum operating pressure for shell testing, and 1.10 times for seat testing.Because it is used mostly for low-pressure applications, the system is usually pressurized to 10% above the maximum operating value or 100 psi max.The use of pressure-relieving devices is recommended. The use of pressure-relieving devices is mandatory.Requires extensive post-test clean-up to avoid damage to components or disruption to the system when operation begins.There is little or no need for cleaning after testing.Usually records low rates of equipment failure. It sees common equipment failure.The process is straight-forward and poses less danger. Thus, semi-skilled personnel can oversee it.Because of the dangers involved, an experienced operator supervises this process. For example, nitrogen leakage can gradually displace the air in the test lab and affect personnel. Also, the effects of overpressure are more catastrophic. Hydraulic Testing vs. Pneumatic TestingNote: Testing above 100 psi gas pressure can be very dangerous due to the expansion properties of a gas.
When pressure testing a valve, there are key components that are given a closer look for the duration of the process. Three of these include the shell, seal, and seat.
The valve shell refers to the main body of the device. Moreover, its testing in the industry is driven mostly by guidelines from API 598 and ASME B16.34. Typically, the valve is mounted on a test bench and partially opened. Then, the shell is pressurized, with ASME B16.34 recommending a minimum of 1.5 times the valve pressure rating at 100 (38 ) for hydrostatic testing. While that of pneumatic seat testing is 1.1 times the maximum allowable pressure. Pneumatic testing is done to 80-100 psi. Also, both the API and ASME standards recommend varying test duration depending on the size of the valve being tested. The table below summarizes the test duration.
Valve Size (Inches)Test Duration (Seconds) 2..5 6..0 12..0 300Valve Size vs. Test Duration For Shell TestIn addition, the test water temperature should range between 41 (5 ) and 122 (50 ). And the pressure gauge used for measurements should have calibration ranging from not less than 1.5 times the test pressure, to not more than 4 times the test pressure. For a valve shell to pass the test, there shall be no visible leakage for the duration of the test.
A valve stem seal (packing) is also monitored during the shell test. For adjustable stem seals, the occurrence of leakage during the test is NOT a cause for rejection, as long as the manufacturer can demonstrate the seals capacity to retain at least the maximum allowable pressure of the valve without any visible leakage. Adjustments to the packing are allowed to eliminate leakage. For non-adjustable stem seals, no leakage is permitted during the shell test.
Typically, the valve seat test is carried out after testing the valve shell. With the same API and ASME standards as with the shell test providing guidance. The recommended pressure is 110% of the maximum allowable pressure at 100 (38 ), and the test time varies with size in accordance with ASME B16.34.
Valve Size (Inches)Test Duration (Seconds) 2..5 8..0 18..0 120Valve Size vs. Test Duration For Seat TestThe test duration recommendations from API 598 are similar to these, and it also states the allowable leakage rates from the seat.
Valve Size (Inches)Hydrostatic Leakage Rate (Drops Per Minute)Pneumatic Leakage Rate (Bubbles Per Minute) 2..5 6..0 12.For valve sizes greater than 14 inches, the hydrostatic test leakage rate should not exceed two drops per minute per inch. While the pneumatic test leakage rate should be less than four bubbles per minute per inch.
One of the requirements of industrial valves is having reliable fire protection. This holds particularly true for sensitive applications such as oil and gas, refinery, and petrochemical industries. Moreover, valves in these industries must guarantee a reliable and safe shut-off in case of a fire incident.
In a fire test, a valve is pressurized and subject to high-temperature flames between (750 ) and ( ) for a period of thirty minutes. During this period, the heat intensity and the leakages both internal and external are monitored and measured. Also, after extinguishing the flames and allowing the valve to cool, the technician test its pressure-retaining capacity. All through the test, the leakage levels should be within acceptable limits for the valve to pass as being fire-safe. Some key things to note about fire testing include:
Standards such as API 607, API 6FA, ISO , BS , and BS constitute industry guidelines for fire testing. On the basis of these guidelines, several companies set up their bespoke procedure for fire-safety valves. Of all the fire testing guidelines, API 607 and API 6FA are the most widely used. API 607 provides testing criteria for valves with non-metallic seating and quarter-turn valves. API 6FA provides the testing criteria for metal seated valves.
Note: Most metal-to-metal seated Gates, Globes, and Swing checks are NOT tested to API 607 due to their inherently Fire Safe Design. (There are no soft parts to melt during a fire.)
A fugitive emissions test aims to assess the impact of gas or vapor leakage from a valve. Although this leakage can be from anywhere along the piping system, statistics show that approximately 60% of fugitive emissions stem from valves. This data highlights the importance of this test. In addition, the impact of these emissions has significant consequences including:
When carrying out fugitive emission tests, the most common test gases are helium and methane. The valve is pressurized with the test gas at varying temperatures. Then technicians monitor for leakages via the sniffing or vacuum method. International standards such as API 622, API 624, API 644, ISO -1, and ISO -2 all provide guidance on how to carry out this valve test. However, most organizations develop their specifications to ensure application suitability.
Cryogenic testing of valves is done for those operating at low temperatures or in cryogenic service. The test procedure involves placing the valve within an insulated tank, with liquid nitrogen at temperatures of down to -320 (-196 ).
Then, helium pressurizes the valve to the operating pressure specified for its class. During the test, technicians closely monitor the temperature inside the valve and leakages. In the end, the valve is depressurized and warmed up until it attains ambient temperature. Thereafter, a detailed report summarizes the performance of the valve and whether leakages were within acceptable limits. There are several international standards that provide guidelines for cryogenic valve testing including ISO -1, ISO -2, EN , and BS .
In addition to the standards mentioned in the previous section, there are a host of standards that provide recommendations for different valve types and test procedures. The table below provides a list of these standards and the areas of testing they cover, for quick referencing.
Applicable StandardValve Type and Test Procedure API 598Valve inspection and test. Testing of cast iron gate, plug, check, and globe valves. Also, testing of steel gate, globe, check, ball, and butterfly valves. Cryogenic valves.API 527 and ASME PTC 25Pressure relief valves.API 6DTesting of pipeline valves.ASME B16.34Pressure seal valves and steal valves larger than NPS 24 inches. Flanged, threaded, and welded end of valves.MSS SP-80Bronze gate, globe, angle, and check valves.MSS SP-70, MSS SP-71, MSS SP-78 and MSS SP-85Testing of cast iron valves, flanged, and threaded ends.ISA S-75, ISO , and MSS SP61Hydrostatic testing of valves.FCI 70-2, ISA S-75Control valve testing.Standards for Valve TestingINTELLIGENT WORK FORUMS
FOR ENGINEERING PROFESSIONALS
Log In
Are you an
Engineering professional?
Join Eng-Tips Forums!
*Eng-Tips's functionality depends on members receiving . By joining you are opting in to receive .
Promoting, selling, recruiting, coursework and thesis posting is forbidden.
Eng-Tips Posting Policies
Confused about ball valve pressure testing
thread408- Forum Search FAQs Links MVPsForum
If you are looking for more details, kindly visit Valve Test Table.
Search
FAQs
Links
MVPs
(Mechanical)
(OP)
18 Dec 17 11:11Hey
Greetings!
Firstly I have bought a Class 800 Socket welded three piece ball valve of CF8M material from a local purchaser.
Now I wanted to check if the purchaser has done proper testing of the valve according to API 598. And when I referred the standards the shell hydrostatic testing pressure should be 1.5 times cold working pressure for the given material from Table 2.2 (ASME 16.34), I found that the test should be done at around 1.5*132.4(approx)= 198.6 bar. Is that correct?
And if it is correct then what seat material should have been used while testing?
Because the material provided with the valve seat is PTFE and I have read that PTFE has 63 bar cold working pressure only. So is it that while testing at 198.6 bar PTFE will work correctly?
(P.S. I could have asked the purchaser directly but then its not learning RIGHT?)
Thanks in advance :)
(Petroleum)
18 Dec 17 11:47The shell hydrotest can be undertaken either with the valve in partially open (50%) position so that the pressure containing parts are exposed to pressure or without the valve ball or seals / seats.Class 800 as noted before is a strange rating but if you use 132 as the rated pressure you're probably ok, so 1.5 times that for the shell PT is good.Now that doesn't mean that the valve you buy is designed to seal at that pressure if the valve data sheet states max differential pressure is something different. In other words you can buy a class 800 valve that is only good for sealing up to 50 bar. The valve body won't break, but the seals might blow out if you put 100 bar across it. If you only are ever going to see say 10 bar or less, why pay more for a valve to seal at 132 bar when you don't need it to?That lower max operating / differential pressure becomes your seat test pressure ( X 1.1 usually).I don't know where you got 63 bar for PTFE, but may well be taken out of context. However the valve seat at best is only designed for 132 bar x 1.1. 198 bar is for the shell test ONLY, not the seat leakage test.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
(Mechanical)
(OP)
19 Dec 17 03:42Okay so if I want to do the shell testing that means I can do it at 198 bar pressure but without my seals/seats and all other valve trims except my body. Correct?
I mean what if I do it with whole valve assembled and at some 63 bar pressure I find leakage or the seals blow out then how am I supposed to test it because it hasn't reached 198 bar (calculated testing pressure for Cl800 CF8M material)?
P.S. I am trying to learn something here :)
Thanks in advance.
(Petroleum)
19 Dec 17 09:42Ok I'll try again.You can test the shell with or without the ball etc. This test should be at 1.5 x rated pressure of the valve ( in your case a total of 198 bar)If you test the shell with the ball and seats in place, the valve MUST be OPEN or at least 50% Open to prevent damage to the seats.To test the seats you close the valve and test against one end or both ends.What the seat test pressure is depends on what you have specified as the required Max pressure. In your case it appears to be a max of 63 bar, but I don't know where you got that figure from.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
(Mechanical)
(OP)
21 Dec 17 03:16okay I got it!
I will check the valve accordingly at 198 bar for shell test and 1.1 times the maximum pressure for hydrostatic seat leakage test.
Thanks for the help and you are really a true expert @LittleInch :)
Please let us know here why this post is inappropriate. Reasons such as off-topic, duplicates, flames, illegal, vulgar, or students posting their homework.
Thank you for helping keep Eng-Tips Forums free from inappropriate posts.
The Eng-Tips staff will check this out and take appropriate action.
Click Here to join Eng-Tips and talk with other members! Already a Member? Login
Contact us to discuss your requirements of Horizontal Type Testing Machine. Our experienced sales team can help you identify the options that best suit your needs.
Comments
Please Join Us to post.
0