Does anyone know what the guidelines are for piping ruptures i.e., at what pressure will piping rupture without a blocked flow condition (fluid with a open flow path to a low pressure rated vessel). I'm looking for a good resource on this subject. For example: 2000 psig gas flowing through 250...
I am trying to locate the Joule Thompson coefficient for natural gas or the Beattie-Bridgeman constants for naturaal gas so that I can calculate it. Does anyone know of a good resource?
