Article | REF: J2611 V1

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. Ternary diagrams of residual curve networks

    The analysis of ternary residue curve diagrams is at the heart of design tools for azeotropic or extractive distillation units for non-ideal mixtures. The addition of one-third body E to the A-B mixture enables ternary A-B-E diagrams to be plotted and analyzed graphically.

    4.1 Representation of ternary liquid-vapor equilibria

    The three-dimensional representation of the bubble [T b,p (x )] and dew [T d,p (y )] surfaces as shown in figure 10 a is the most complete but is difficult to exploit. For its part, the projected equilibrium vectors...

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    Ternary diagrams of residual curve networks