A disjunctive programming approach for the optimal design of reactive distillation columns

[1]  Steinar Hauan,et al.  Graphical methods for reaction distribution in a reactive distillation column , 2000 .

[2]  I. Grossmann,et al.  Disjunctive Programming Models for the Optimal Design of Distillation Columns and Separation Sequences , 2000 .

[3]  R. Fletcher,et al.  Initialising distillation column models , 2000 .

[4]  E. Gilles,et al.  Steady-state multiplicities in reactive distillation columns for the production of fuel ethers MTBE and TAME: theoretical analysis and experimental verification , 1999 .

[5]  Michael F. Doherty,et al.  Design method for kinetically controlled, staged reactive distillation columns , 1998 .

[6]  Kai Sundmacher,et al.  Multiple Steady States in a Reactive Distillation Column for the Production of the Fuel Ether TAME Part II: Experimental Validation , 1998 .

[7]  B. Bessling,et al.  Design of Processes with Reactive Distillation Line Diagrams , 1997 .

[8]  I. Grossmann,et al.  Logic-based MINLP algorithms for the optimal synthesis of process networks , 1996 .

[9]  Efstratios N. Pistikopoulos,et al.  Generalized modular representation framework for process synthesis , 1996 .

[10]  I. Grossmann,et al.  Global optimization of bilinear process networks with multicomponent flows , 1995 .

[11]  Constantinos C. Pantelides,et al.  Design of reaction/separation networks using detailed models , 1995 .

[12]  Michael F. Doherty,et al.  New tools for the design of kinetically controlled reactive distillation columns for ternary mixtures , 1995 .

[13]  Amy R. Ciric,et al.  Synthesis of nonequilibrium reactive distillation processes by MINLP optimization , 1994 .

[14]  R. Raman,et al.  Modelling and computational techniques for logic based integer programming , 1994 .

[15]  Michael F. Doherty,et al.  Design of three-component kinetically controlled reactive distillation columns using fixed-points methods , 1994 .

[16]  Ignacio E. Grossmann,et al.  Optimal feed locations and number of trays for distillation columns with multiple feeds , 1993 .

[17]  J. Bravo,et al.  Investigations in a catalytic distillation pilot plant. Vapor/liquid equilibrium kinetics, and mass-transfer issues , 1993 .

[18]  I. Grossmann,et al.  A combined penalty function and outer-approximation method for MINLP optimization : applications to distillation column design , 1989 .

[19]  Garth P. McCormick,et al.  Computability of global solutions to factorable nonconvex programs: Part I — Convex underestimating problems , 1976, Math. Program..

[20]  A. I. Stankiewicz Process Intensification: Transforming Chemical Engineering , 2000 .

[21]  Johann Stichlmair,et al.  MINLP optimization of reactive distillation columns , 2000 .

[22]  Michael F. Doherty,et al.  Reactive distillation by design , 1992 .

[23]  C. Yaws Calculate liquid heat capacity , 1991 .

[24]  V. Agreda,et al.  High-purity methyl acetate via reactive distillation , 1990 .

[25]  M. Doherty,et al.  The simple distillation of homogeneous reactive mixtures , 1988 .

[26]  John J.J. Chen Comments on improvements on a replacement for the logarithmic mean , 1987 .

[27]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[28]  Klaus D. Timmerhaus,et al.  Plant design and economics for chemical engineers , 1958 .