Separating a Ternary Mixture of Water, 2-Propanol, and Acetone at Atmospheric Pressure
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Consider a ternary mixture composed of water, -propanol, and acetone at . This Demonstration plots the residue curve map (RCM) for this mixture. There are two distillation regions separated by a distillation boundary (shown in red) running from pure acetone to the only azeotrope in the ternary system (i.e., the binary azeotrope between water and -propanol shown in red).
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Contributed by: Housam Binous and Naim Faqir (May 2012)
Open content licensed under CC BY-NC-SA
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Reference
[1] E. J. Henley and J. D. Seader, Equilibrium-Stage Separation Operations in Chemical Engineering, New York: Wiley, 1981.
Expressions for pure component vapor and liquid enthalpies were adapted from Aspen-HYSYS. Enthalpies are in .
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