Residue Curve and Bubble Temperature Distribution for a Ternary Mixture
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Consider a ternary mixture composed of chloroform, acetone, and methanol. This mixture deviates from ideal behavior. Thus, the Wilson model for activity coefficients and the modified Raoult's law are used to predict vapor-liquid equilibrium data.
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Contributed by: Housam Binous, Ikbel El Glaoui, and Ahmed Bellagi (March 2011)
Open content licensed under CC BY-NC-SA
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For more information, see:
M. F. Doherty and M. F. Malone, Conceptual Design of Distillation Systems, New York: McGraw–Hill, 2001.
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