I'm working on a project with the fluid being API 42 crude. I'm having a bunch of trouble finding a clear answer on allowable velocities for inlet and outlet lines for the relief. For inlets, I've found the general rule for <3% pressure drop but I'm expecting fluid velocity to matter prior to that for a liquid line.
Key in this question also is the velocity through the valves on the upstream and downstream side.
Thanks for the help. This is all for a 31.4 system.
Key in this question also is the velocity through the valves on the upstream and downstream side.
Thanks for the help. This is all for a 31.4 system.