Compute multicomponent vapor–liquid phase equilibrium with a cubic equation of state and an activity-coefficient model.
Enter each component by name and overall mole fraction z. Leave Tc, Pc, and ω blank to look up common solvents by name, or fill all three together. Txy and Pxy require exactly two components.
| Name | z | Tc (K) | Pc (Pa) | ω | |
|---|---|---|---|---|---|
Flash a mixture at specified temperature and pressure.