duncan8943
Chemical
- Feb 9, 2010
- 11
I have a n-butane bullet with an existing relief valve. I am trying to provide supporting calculations for the relief valve, but can't even get close to the size valve that is installed. Blocked in is applicable and results in a small valve. As far as fire sizing, the butane will vaporize if there is a leak and the bullets are in an isolated area where flammable liquid could not pool beneath them. The pipeline supply pressure is less than the MAWP. There is a natural gasoline tank nearby with an earthen berm around it. The natural tank and berm is at a higher elevation. I was thinking that you could have a natural gasoline fire and use radiant heat transfer to the butane tanks. Any other ideas out there? Thanks.