?????????? I can't decide whether this thread is constructive on the matter of hydro versus pnuematic testing.
A fundamental point seems to be missing from the discussion - the purpose of a pressure test.
Why specificaly can't the OP's pressure vessel be hydrotested during fabrication? A reactor vessel isn't fabricated with a refractory lining, so why can't it be hydro'd before the lining goes in? IMO The extra benefits and confidence afforded by a
hydrotest, definitely outweighs the short term concerns of drying the vessel out.
A pneumatic test wont get you the benefits (notch blunting, shake down, integrity testing etc) of a hydrotest and has substantially more danger involved - remember, we're testing an untested vessel for it's integrity - the potential stored energy can not be overlooked.
Australia's pressure vessel code includes an appendix to calculate the pneumatic stored energy and the the recommended exclusion zone required for a pneumatic test. If you post up the dimensions, I'll run the numbers. For kicks I sometimes work out the equivalent kg of TNT that a pneumatic test represents - it helps put things in perspective.
If in building a vessel I know that I
must do a pneumatic pressure test (and that's rare), apart from many controls during the test, I also specify that the vessel is extensively NDE'd during fabrication. This helps increase the confidence level that there isn't a defect lurking that might cause the vessel to fail.
On the topic of testing and rerating lines, let me ask you this question. Using round numbers, say you have a pipe with 100psi DP, hydrotested to 150psi. Now the process dept need it rerated to 125psi but don't want to get the line wet - so hydrotesting is out. A 1.1DP pneumatic test is still within the original hydrotested envelope... would there be any benefit in a pneumatic test? Do you give the line carteblanche approval to operate at the new condition without any pressure test? Additional NDE??
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