to simulate a blowdown with Prode Properties (in case the standard procedure is not applicable)
is it better to adopt V-H or V-P flash specifications ?
the Volume-Enthalpy specification should allow a more accurate solution of energy balance, is it true ?
I have a vessel with liquid vaporizing (fire case) and I wish to define my own models for RO and piping,
does that make sense from a practical point of view ?