Page 43 - Distillation theory
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P1: FCH
            0521820928c01  CB644-Petlyuk-v1                                                      June 11, 2004  17:45





                                1.9 Conclusion                                                     17

                                    2       3


                                                    Figure 1.15. Liquid–liquid phase diagram for six-component mix-
                                1                4  ture (points indicate the compositions of equilibrium liquid phases
                                                    of binary constituents).

                                    6       5


                                  We can see that the phase diagrams differ by the number of one- and two-
                                phase liquid regions Reg  . In Fig. 1.13e, a system with a three-phase liquid
                                                      L−L
                                region Reg     is shown among others.
                                         L−L−L
                                  The most common types of phase diagrams are those represented in Figs. 1.13a
                                and b with one two-phase region. In Figs. 1.14a and b, the examples of liquid–
                                liquid phase diagrams for four-component mixtures with one two-phase region
                                are shown.
                                  For a clear representation of liquid–liquid equilibrium in multicomponent sys-
                                tems with one two-phase liquid region Reg  , it is possible to use the graph in
                                                                     L−L
                                Fig. 1.15. From Fig. 1.15, it is clear that component 1 is a heteroforming agent (in
                                practice, it is water that plays this role in most cases). Components 1–2, 1–3, and
                                1–4 form two liquid phases. The rest of the components do not form liquid phases
                                between each other. In such a way, the description of liquid–liquid phase diagrams
                                for multicomponent mixtures with one two-phase region Reg L−L  is rather simple.


                        1.9.    Conclusion

                                The variety of possible compositions of a multicomponent mixture can be repre-
                                sented as a multidimensional simplex. Liquid–vapor phase equilibrium is a factor
                                determining the distillation process results. Depending on the nonideality degree,
                                the following types of mixtures – differing in their behavior during the distillation
                                process – can be distinguished: ideal, nonideal zeotropic, mixtures with a tangent
                                azeotrope, azeotropic mixtures, and heteroazeotropic mixtures. Residue curves
                                and their bundles characterize phase behavior of mixtures in each point of the
                                concentration simplex. Residue curve bundles define the possible cases of mix-
                                ture separation in one of the distillation-limiting modes, in particular, the infinite
                                reflux mode. Residue curve bundles split the concentration simplex into distilla-
                                              ∞
                                tion regions Reg , separated by the lines, surfaces, or hypersurfaces.
                                  Bondsbetweenthestationarypoints(pointsofthecomponentsandazeotropes)
                                and distillation subregions Reg sub  are the structural elements of the distillation
                                regions. Residue curve bundle structure of multicomponent mixtures can be de-
                                scribed with the help of a structural matrix that reflects the bonds available be-
                                tween the stationary points.
                                  Lines, surfaces, and hypersurfaces of equal phase equilibrium coefficients of
                                two components split the concentration simplex into regions of identical order of
                                              ijk
                                components Reg   (K i > K j > K k ) that define the possible causes of separation
                                              ord
                                under the finite reflux mode.
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