usmcmcc
Mechanical
- Sep 10, 2003
- 1
I'm using a 24"dia by 48" long steel vessel which is 75% jacketed for 50psig steam in the jacket and full vacuum in the vessel. The steam heats the liquid inside the vessel to just under atmospheric pressure in normal operations. The vessel and jacket are seperatll code to ASME "U" stamp.
Do I use a rupture disc alone to protect the liquid vessel? Or do I use a pressure relief valve? Or both?
Do I use a rupture disc alone to protect the liquid vessel? Or do I use a pressure relief valve? Or both?