EGT01
Chemical
- Dec 11, 2002
- 435
I'm in the process of reviewing the design basis for a vacuum relief valve on an ASME Sec VIII vessel that has a MAWP of 25 psi internal and 4 psi external.
The vacuum relief valve is set at 4 psi vacuum, same as the external MAWP rating. This is what I'm questioning.
My experience with API 650 and API 620 storage tanks is that the vacuum relief valve must be set so that the valve can achieve the required relief rate without exceeding the external MAWP rating.
What about for an ASME Sec VIII vessel, can the vacuum relief valve be set at the external MAWP rating?
Also, I would appreciate it if someone could direct me to a section or paragraph in ASME Sec VIII that addresses vacuum relief valve setting and/or requirements.
Just for reference, here's two threads I found that had closely related discussions.
thread794-35462
thread124-29282
The vacuum relief valve is set at 4 psi vacuum, same as the external MAWP rating. This is what I'm questioning.
My experience with API 650 and API 620 storage tanks is that the vacuum relief valve must be set so that the valve can achieve the required relief rate without exceeding the external MAWP rating.
What about for an ASME Sec VIII vessel, can the vacuum relief valve be set at the external MAWP rating?
Also, I would appreciate it if someone could direct me to a section or paragraph in ASME Sec VIII that addresses vacuum relief valve setting and/or requirements.
Just for reference, here's two threads I found that had closely related discussions.
thread794-35462
thread124-29282