Happy rains to all
in my plant we have a carbon steel pipe line header of flange rating 600 psi. Its rated pressre is 102 barg.
Can we operate this pipe line on 100 barg? if NO, than which standdard and clause retricts us?
And if YES, than:
1 . what do standards allow us?
2. what are the factors we should be aware of before doing this - such as a pressure shock?
3. at what set point should a PSV be set?