The influence of equilibrium chemical reactions on vapor—liquid phase diagrams
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[1] Domingos Barbosa,et al. A new set of composition variables for the representation of reactive-phase diagrams , 1987, Proceedings of the Royal Society of London. A. Mathematical and Physical Sciences.
[2] M. Doherty,et al. Theory of phase diagrams and azeotropic conditions for two-phase reactive systems , 1987, Proceedings of the Royal Society of London. A. Mathematical and Physical Sciences.
[3] Michael F. Malone,et al. Modeling of reactive distillation systems , 1987 .
[4] Michael F. Doherty,et al. Separation of closely boiling mixtures by reactive distillation. 2. Experiments , 1985 .
[5] Michael F. Doherty,et al. Separation of closely boiling mixtures by reactive distillation. 1. Theory , 1985 .
[6] H. Lee,et al. Isothermal vapor-liquid equilibrium accompanied by esterification; ethanol-formic acid system , 1985 .
[7] P. Delogu,et al. Equilibrium constant for the methyl tert-butyl ether liquid-phase synthesis using UNIFAC , 1983 .
[8] Aage Fredenslund,et al. Computerized Design of Multicomponent Distillation Columns Using the UNIFAC Group Contribution Method for Calculation of Activity Coefficients , 1977 .
[9] C. D. Holland,et al. A new method of convergence for solving reacting distillation problems. , 1977 .
[10] W. A. Holve. Theoretical Analysis of Changes in Relative Volatility via Reversible Metalation Reactions and the Application to Fractionation , 1977 .
[11] Paul A. Nelson,et al. Countercurrent equilibrium stage separation with reaction , 1971 .
[12] Hiroshi Yagi,et al. CALCULATION OF MULTICOMPONENT DISTILLATION ACCOMPANIED BY A CHEMICAL REACTION , 1971 .
[13] S. Saito,et al. SEPARATION OF META- AND PARA-XYLENE MIXTURE BY DISTILLATION ACCOMPANIED BY CHEMICAL REACTIONS , 1971 .
[14] Thomas E. Corrigan,et al. A development study of methanol acetic acid esterification , 1969 .
[15] T. Corrigan,et al. Effect of Distillation on a Chemical Reaction , 1968 .
[16] E. Sebastiani,et al. Acetic acid—water system thermodynamical correlation of vapor—liquid equilibrium data , 1967 .
[17] L. E. Schniepp,et al. Continuous Process for Acetylation of 2 3-Butylene Glycol , 1945 .
[18] D. B. Keyes,et al. Esterification Processes and Equipment , 1932 .
[19] M. Doherty,et al. The simple distillation of homogeneous reactive mixtures , 1988 .
[20] H. Sawistowski,et al. Vapor-liquid equilibrium with association in both phases. Multicomponent systems containing acetic acid , 1982 .
[21] F. P. Stein,et al. On the derivation and application of solution thermodynamics for reactive components , 1982 .
[22] J. O’Connell,et al. Solution thermodynamics for “reactive” components , 1981 .
[23] J. Jenkins,et al. Vapour-liquid equilibrium in systems with association in both phases: The simultaneous evaluation of liquid phase models and thermodynamic consistency testing for the system acetic acid-toluene , 1977 .
[24] J. Prausnitz,et al. Generalized Correlation for Fugacity Coefficients in Mixtures at Moderate Pressures. Application of Chemical Theory of Vapor Imperfections , 1973 .
[25] G. M. Wilson,et al. Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing , 1964 .
[26] J. Marek. Rectification with a chemical reaction. II. Plant rectification of a water-acetic acid-acetic anhydride mixture , 1956 .
[27] P. Wyatt,et al. The vapour pressures of nitric acid solutions. Part I. New azeotropes in the water–dinitrogen pentoxide system , 1955 .
[28] J. Marek,et al. Vapor-liquid equilibria in mixtures containing an associating substance. II. Binary mixtures of acetic acid at atmospheric pressure , 1955 .
[29] J. Marek,et al. Vapor-liquid equilibria in mixtures containing an associating substance. I. Equilibrium relationships for systems with an associating component , 1954 .