Bourbon103
Chemical
- Nov 30, 2005
- 32
I have a heat exchanger that external fire is considered the controlling scenario for over-pressurization. Currently, relief is in the form of a 6" x 10" relief valve on the inlet to the shell ~1000 ft. away in another building.
I know per ASME XIII that an ASME coded vessel requires at least a minimally sized relief valve on its shell. Is there a restriction as far as how "local" the relief valve needs to be or is the only requirement that it passes 3% inlet pressure drop?
I know per ASME XIII that an ASME coded vessel requires at least a minimally sized relief valve on its shell. Is there a restriction as far as how "local" the relief valve needs to be or is the only requirement that it passes 3% inlet pressure drop?