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1
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gwalkerb
Petroleum
- Jul 4, 2012
- 74
Note that everything below is based on piping systems built to B31.3 with B16.5 flanges.
Our QC and hydro-test group had occasionally in the past accidentally taken hydro-tests to pressures higher than specified. Although there weren't any visual indication of failure (i.e. leakage or deformation), they passed the details of the test back to us in engineering to validate if the materials were still usable, or if they needed to be scrapped.
The flanges are typically the limiting component in our piping systems, and our standard hydro-test pressures are based on 1.5x the maximum design pressure of B16.5 flanges at 100F. The methodology that was explained to me to validate over-pressure during a hydro-test (by someone who no longer works here), was to use the formulas from B16.5 Nonmandatory Appendix A section A-2, but calculate a pressure using 100% of the yield strength at 100F instead of 60%. If our hydro-test pressure didn't exceed that value, then we could be confident that we didn't exceed the yield strength of the material, and didn't create any plastic deformation.
To provide further protection, and avoid ever damaging flanges, we've decided to use relief valves in our testing system, set appropriately for each flange class and material group. So I've been tasked with sizing and specifying these relief valves.
Using the methodology above to determine relief valve set-pressures works fine for group 1 materials (e.g. A105N, A350-LF2 CL1), which is the majority of what we fabricate. We do sometimes use group 2 materials (A182-F316, A182-F304, A182-F316L, A182-F304L) but when I was doing the same exercise for group 2 materials, I realized that hydrotesting a group 2 flange at 1.5x the design pressure would then exceed the calculated yield limit. This arises as group 2 and 3 materials follow the same formula for determining rating, but use a yield strength factor of 70% instead of 60%. So a hydrotest at 1.5x design pressure which is based on 60% of yield strength would then occur at 90% of yield strength. But a hydrotest of a group 2 or 3 material with design pressure based on 70% of yield strength would then occur at a pressure equivalent to 105% of yield strength, which implies that the flanges could potentially be plastically deforming.
I'm not sure how to reconcile this information, and set relief valves appropriately for group 2 or 3 materials. Therefore I have a couple questions:
1. Is the methodology described above of using a 100% factor on yield strength, but still following the A-2.2(a)(1-3) formulas a valid way to determine a limit on hydrotest pressures?
2. If this methodology is flawed, what is the proper way to determine the limit of hydrotest pressures?
3. If this method is sound, how does that work with group 2 materials exceeding their yield strength based on the 70% x1.5?
Our QC and hydro-test group had occasionally in the past accidentally taken hydro-tests to pressures higher than specified. Although there weren't any visual indication of failure (i.e. leakage or deformation), they passed the details of the test back to us in engineering to validate if the materials were still usable, or if they needed to be scrapped.
The flanges are typically the limiting component in our piping systems, and our standard hydro-test pressures are based on 1.5x the maximum design pressure of B16.5 flanges at 100F. The methodology that was explained to me to validate over-pressure during a hydro-test (by someone who no longer works here), was to use the formulas from B16.5 Nonmandatory Appendix A section A-2, but calculate a pressure using 100% of the yield strength at 100F instead of 60%. If our hydro-test pressure didn't exceed that value, then we could be confident that we didn't exceed the yield strength of the material, and didn't create any plastic deformation.
To provide further protection, and avoid ever damaging flanges, we've decided to use relief valves in our testing system, set appropriately for each flange class and material group. So I've been tasked with sizing and specifying these relief valves.
Using the methodology above to determine relief valve set-pressures works fine for group 1 materials (e.g. A105N, A350-LF2 CL1), which is the majority of what we fabricate. We do sometimes use group 2 materials (A182-F316, A182-F304, A182-F316L, A182-F304L) but when I was doing the same exercise for group 2 materials, I realized that hydrotesting a group 2 flange at 1.5x the design pressure would then exceed the calculated yield limit. This arises as group 2 and 3 materials follow the same formula for determining rating, but use a yield strength factor of 70% instead of 60%. So a hydrotest at 1.5x design pressure which is based on 60% of yield strength would then occur at 90% of yield strength. But a hydrotest of a group 2 or 3 material with design pressure based on 70% of yield strength would then occur at a pressure equivalent to 105% of yield strength, which implies that the flanges could potentially be plastically deforming.
I'm not sure how to reconcile this information, and set relief valves appropriately for group 2 or 3 materials. Therefore I have a couple questions:
1. Is the methodology described above of using a 100% factor on yield strength, but still following the A-2.2(a)(1-3) formulas a valid way to determine a limit on hydrotest pressures?
2. If this methodology is flawed, what is the proper way to determine the limit of hydrotest pressures?
3. If this method is sound, how does that work with group 2 materials exceeding their yield strength based on the 70% x1.5?