The attached flowsheet is for separation of methanol two phase stream. Stream 15 is a two phase mixture. It has vapor in equilibrium with liquid. It enters a Flash Separator Sep. The intention to put in a flash is to separate vapor from liquid. The will obviously require no heat. Therefore the simulation parameter are zero pressure drop and the outlet temperate same as the inlet temperature.
On simulating this flowsheet, in pvf mode i get warning, "message: TEA warning: PVF inside-out flash failed: Trivial solution for equilibrium calculation
message: WARNING: Flash Sep: temperature post-check failed for liquid product (temperature deviation too high). Using TP flash."
On using TP flash option. the vapor has liquid and the liquid has vapor, but there are no warnings. Any suggestions to deal with the warning??