Minimum internal recycle in nonideal homogeneous multicomponent distillation
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[1] E. Blass,et al. Minimum reflux calculations for nonideal mixtures using the reversible distillation model , 1991 .
[2] Don W. Green,et al. Perry's chemical engineers' handbook. 7th ed. , 1997 .
[3] T. L. Wayburn,et al. Homotopy continuation methods for computer-aided process design☆ , 1987 .
[4] J. D. Seader,et al. Simulation of continuous reactive distillation by a homotopy-continuation method , 1988 .
[5] J. Prausnitz. Computer calculations for multicomponent vapor-liquid and liquid-liquid equilibria , 1980 .
[6] J. W. Kovach. Heterogenous azeotropic distillaion-homotopy-continuation methods , 1987 .
[7] J. Gaube. J. Gmehling, U. Onken: Vapor‐Liquid Equilibrium Data Collection, Aqueous‐Organic Systems, in der Reihe: Chemistry Data Series, Vol. I, Part. 1. DECHEMA, Frankfurt 1977. 698 Seiten, Preis: DM 120,‐ , 1978 .
[8] S. Glanz,et al. Calculating minimum reflux of nonideal multicomponent distillation using eigenvalue theory , 1994 .
[9] D. J. Vickery,et al. Path-following approaches to the solution of multicomponent, multistage separation process problems , 1986 .
[10] Jorge R. Paloschi,et al. Bounded homotopies to solve systems of sparse algebraic nonlinear equations , 1997 .
[11] Eugene L. Allgower,et al. Numerical continuation methods - an introduction , 1990, Springer series in computational mathematics.
[12] E. Blass,et al. A review on minimum energy calculations for ideal and nonideal distillations , 1995 .
[13] A. W. Westerberg,et al. The product composition regions of single-feed azeotropic distillation columns , 1992 .
[14] G. D. Byrne,et al. Distillation calculations using a locally paramaterized continuation method , 1985 .
[15] Michael F. Doherty,et al. Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns , 1985 .
[16] S. Skogestad. DYNAMICS AND CONTROL OF DISTILLATION COLUMNS A tutorial introduction , 1997 .
[17] M. F. Malone,et al. Feasibility of separations for distillation of nonideal ternary mixtures , 1993 .
[18] J. Ilavský,et al. Global simulation of countercurrent separation processes via one-parameter imbedding techniques , 1981 .
[19] Thomas Kuen,et al. Minimum energy demand for distillations with distributed components and side-product withdrawals , 1994 .
[20] Johann Stichlmair,et al. Minimum reflux and minimum reboil in ternary distillation , 1993 .
[21] D. Vickery,et al. An efficient continuation method for the solution of difficult equilibrium stage separation process problems , 1988 .
[22] Achim Kienle,et al. Bifurcation analysis and steady-state multiplicity of multicomponent, non-equilibrium distillation processes , 1991 .
[23] Michael F. Doherty,et al. Geometric behavior and minimum flows for nonideal multicomponent distillation , 1990 .
[24] Johann Stichlmair,et al. Minimum energy demand of distillation columns with multiple feeds , 1997 .
[25] J. Gmehling. Vapor-Liquid Equilibrium Data Collection , 1977 .
[26] J. R. Knight,et al. Design and synthesis of homogeneous azeotropic distillations. 5. Columns with nonnegligible heat effects , 1986 .
[27] J. D. Seader. Computer modeling of chemical processes , 1985 .
[28] Michael F. Malone,et al. Nonideal Multicomponent Distillation: Use of Bifurcation Theory for Design , 1991 .