don1980
Chemical
- May 3, 2007
- 669
I have a B31.1 steam header (nonboiler external piping) that is protected by multiple PSVs. This is a 600# system and the gap between the operating pressure and the PSV set pressure is low. So, I want to minimize the risk of popping the PSVs by setting them as high as possible. But when I look in B31.1 I don't find any rules regarding set pressure and peak allowable relief pressure. I read paragraph 107.8.3 (Pressure Relief Requirements on Nonboiler External Piping), but it doesn't address set pressure or peak allowable pressure, nor are these questions answered in the referenced paragraphs of Sec VIII.
Can anyone shed light on the answers to my questions, or point me to where those answers can be found. Thanks.
Can anyone shed light on the answers to my questions, or point me to where those answers can be found. Thanks.