Hello,
I have a question concerning the inlet piping to a relief valve. Similar to foxymophandlpapa but a little different.
The [b]existing[\b] relief valve in question protects down stream piping and equipment (similar to a natural gas header) from a regulator failure. The existing line is...
Hello,
I have a question concerning the inlet piping to a relief valve. Similar to foxymophandlpapa but a little different.
The existing relief valve in question protects down stream piping and equipment (similar to a natural gas header) from a regulator failure. The existing line is a 0.75”...
It appears the allowable overpressure is 6%. But there is also a requirement for a maximum lift of the relief valve after 3%. I will check with my reference material once I get to the office.
Thanks for the link [medal]. I thought I did a good search before posting [blush].
Hey Guys,
I am currently evaulating a boiler relief valve at my plant for a future PHA. This is my first time dealing with a boiler PSV vs Section VIII Pressure vessel.
I know the boilers are allowed a 6% overpressure based on ASME, Section 1, PG 67. This is where is starts getting fuzy. Is...
