I need HYSYS case study for Ethanol Water Azeotropic Distillation to achieve 99% purity from 80% purity. At what pressure column should be operated to break the aezotrope? I m operating the column at 10 atm. Which Activity Model ( Fluid package ) should be used? I am using NTRL but column is un-converged. What Binary Coefficients should be used ?
Anyone can give any other suggestion.



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