Reactive separation systems I. Computation of physical and chemical equilibrium
暂无分享,去创建一个
Rafiqul Gani | Michael Locht Michelsen | R. Gani | M. Michelsen | E. Cisneros | E.-S. Perez Cisneros
[1] Ravindra Datta,et al. Integral analysis of methyl tert-butyl ether synthesis kinetics , 1995 .
[2] S. Brinkley,et al. Calculation of the Equilibrium Composition of Systems of Many Constituents , 1947 .
[3] P. Delogu,et al. Equilibrium constant for the methyl tert-butyl ether liquid-phase synthesis using UNIFAC , 1983 .
[4] Rafiqul Gani,et al. Simulation, design, and analysis of azeotropic distillation operations , 1993 .
[5] 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.
[6] K. Denbigh,et al. The Principles of Chemical Equilibrium , 1956 .
[7] M. Doherty,et al. Vapor-liquid phase equilibrium in systems with multiple chemical reactions , 1995 .
[8] Javier Tejero,et al. Equilibrium constants for methyl tert-butyl ether liquid-phase synthesis , 1992 .
[9] P. L. Douglas,et al. Mathematical modelling and simulation of an MTBE catalytic distillation process using SpeedUp and AspenPlus , 1995 .
[10] T. M. Williams,et al. Practical Methods of Optimization. Vol. 1: Unconstrained Optimization , 1980 .
[11] D. R. Stull,et al. The chemical thermodynamics of organic compounds , 1969 .
[12] D. B. Scully. Calculation of the equilibrium compositions for multi-constituent systems , 1962 .
[13] Youn Yong Lee,et al. VAPOR-LIQUID EQUILIBRIA WITH CHEMICAL REACTION EQUILIBRIUM - SYSTEMS CONTAINING ACETIC ACID, ETHYL ALCOHOL, WATER, AND ETHYL ACETATE - , 1992 .
[14] Rafiqul Gani,et al. Aspects of simulation, design and analysis of reactive distillation operations , 1996 .
[15] Aage Fredenslund,et al. Calculation of simultaneous chemical and phase equilibria in nonideal systems , 1989 .
[16] F. S. Manning,et al. Computation of Multicomponent, Multiphase Equilibrium , 1976 .
[17] Mitsuho Hirata,et al. FORMULATION AND PREDICTION OF QUATERNARY VAPOR-LIQUID EQUILIBRIA ACCOMPANIED BY ESTERIFICATION , 1970 .
[18] V. Brandani,et al. Thermodynamic consistency of vapor-liquid equilibrium data for the water-formaldehyde system , 1984 .
[19] Jorge Ricardo Paloschi. The numerical solution of nonlinear equations representing chemical processes , 1982 .
[20] Rajamani Krishna,et al. Multiple solutions in reactive distillation for methyl tert-butyl ether synthesis , 1993 .
[21] W. White. Numerical Determination of Chemical Equilibrium and the Partitioning of Free Energy , 1967 .
[22] I. Grossmann,et al. Computation of phase and chemical equilibria , 1981 .
[23] W. Seider,et al. Multiphase equilibria of reactive systems , 1996 .
[24] Michael L. Michelsen. Calculation of multiphase ideal solution chemical equilibrium , 1989 .
[25] L. A. Smith,et al. New MTBE design now commercial. [Methyl tertiary butyl ether] , 1982 .
[26] Michael F. Doherty,et al. Necessary and sufficient conditions for reactive azeotropes in multireaction mixtures , 1995 .
[27] M. Doherty,et al. The simple distillation of homogeneous reactive mixtures , 1988 .
[28] Michael F. Doherty,et al. Reactive distillation by design , 1992 .
[29] Christodoulos A. Floudas,et al. Decomposition based and branch and bound global optimization approaches for the phase equilibrium problem , 1994, J. Glob. Optim..
[30] R. Fletcher. Practical Methods of Optimization , 1988 .
[31] C. Floudas,et al. Global optimization for the phase and chemical equilibrium problem: Application to the NRTL equation , 1995 .
[32] Ulrich Hoffmann,et al. Kinetics of methyl tertiary butyl ether liquid phase synthesis catalyzed by ion exchange resin—I. Intrinsic rate expression in liquid phase activities , 1990 .
[33] S. Saito,et al. SEPARATION OF META- AND PARA-XYLENE MIXTURE BY DISTILLATION ACCOMPANIED BY CHEMICAL REACTIONS , 1971 .
[34] H. Chien,et al. Simultaneous Chemical and Phase Equilibrium Calculation , 1973 .
[35] John P. O'Connell,et al. A Generalized Method for Predicting Second Virial Coefficients , 1975 .
[36] Terje Hertzberg,et al. Why methyl tert-butyl ether production by reactive distillation may yield multiple solutions , 1995 .
[37] Christodoulos A. Floudas,et al. Global Optimization and Analysis for the Gibbs Free Energy Function Using the UNIFAC, Wilson, and ASOG Equations , 1995 .
[38] M. Michelsen. The isothermal flash problem. Part I. Stability , 1982 .