a. Simulation of multicomponent distillation in process simulation environment (e.g.
Aspen Hysys, Aspen Plus, ChemCad) is very handy. Nevertheless, the approximate
methods using Fenske Underwood Gilliland Kirkbride equations cannot be
undermined. Can you please explain how these approximate methods are useful to
establish the simulation using simulation package?
[10 marks]
b. Can you please elaborate the advantages and limitations of MESH equations for the
multicomponent distillations? In line with the limitations, you should also highlight the
ways to overcome the challenges of the implementation.
[10 marks]
Fig: 1