ChemEngSquirrel
Chemical
- Jun 10, 2010
- 72
What is the minimum recommended design pressure for a hydrocarbon vessel which is atmospherically vented?
The vessel operates at < 0.1 barg so I am considering setting design pressure at 1 barg. The vent is to a safe location and has a flame arrestor on it.
Thanks.
The vessel operates at < 0.1 barg so I am considering setting design pressure at 1 barg. The vent is to a safe location and has a flame arrestor on it.
Thanks.