Azeotropic distillation
Distillation of non-ideal mixtures
Article REF: J2612 V1
Azeotropic distillation
Distillation of non-ideal mixtures

Authors : Vincent GERBAUD, Ivonne RODRIGUEZ-DONIS

Publication date: September 10, 2010, Review date: March 1, 2015 | Lire en français

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4. Azeotropic distillation

4.1 Using residue curves to design distillation units

Established at full reflux, the equation of a residue curve is determined from a global and partial material balance on the boiler of a simple evaporator:

dxi dτ=(xi−yi)    i=1…n        Courbes de résidu 
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