I am looking at a relief valve with a relief pressure of 0.09 barg. The relief valve spec says that this corresponds to a flow of 10000 scm/hr of air.
What is the method for converting this flow of air to a flow of propane?
Is the volumetric flowrate effectively the same, with only the mass...
I am trying to model the commingling of two oil wells. Well One has a flowing well head pressure of 41 bar and Well Two has a flowing well head pressure of 52 bar.
Do i choke the Well Two down to 41 bar so that this well does not 'back out' Well One?
Or do i choke back Well One so that the...