RugRat2
Chemical
- Aug 31, 2007
- 4
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 it correct to only use a 3% overpressure when actually sizing the valve?
In pressure vessels we usually use the overpressure that is allowed (i.e., fire 21%, others 10%). The reason I noticed the 3% was due to the capacity tables in the relief valve catalogs.
I just dont understand why we use 3% overpressure.
Thanks for the help.
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 it correct to only use a 3% overpressure when actually sizing the valve?
In pressure vessels we usually use the overpressure that is allowed (i.e., fire 21%, others 10%). The reason I noticed the 3% was due to the capacity tables in the relief valve catalogs.
I just dont understand why we use 3% overpressure.
Thanks for the help.