Hi
I am working with a new installation where we will install Pilot Operated PSVs with a maximum back pressure that is close to the set pressure of the PSVs. After contacting our normal PSV supplier, I got the information that the max capacity for the PSVs will be reduced to 80% when we have the...
I am calculating relief cases for a system with a water HC mixture. My question is does anyone have a good idée how to calculate the heat of vaporisation for the mixture?
If I take the enthalpy of the mixture in vapour phase (at due point) minus enthalpy of the mixture in liquid phase (at bubble...