Shortcut methods for nonideal multicomponent distillation: 3. Extractive distillation columns

AIChE Journal

Volumn 50, Issue 6, 2004, Pages 1129-1149

  Brüggemann, Stefan ^a   Marquardt, Wolfgang ^a  

^a RWTH AACHEN UNIVERSITY   (Germany)

Author keywords

Economic screening; Entrainer selection; Minimum energy demand; Multicomponent extractive distillation; Rectification body method (RBM)

Indexed keywords

AZEOTROPES; COSTS; DEGREES OF FREEDOM (MECHANICS); FLOW OF FLUIDS; NONLINEAR SYSTEMS;

EXTRACTIVE DISTILLATION; FEED FLOW RATE;

DISTILLATION;

AZEOTROPIC MIXTURE; DESIGN; DISTILLATION COLUMN; EXTRACTION; FLUID FLOW; PROCESSING TECHNIQUE;

ANALYTIC METHOD; ARTICLE; COMPUTER AIDED DESIGN; DISTILLATION; EXTRACTION; FEASIBILITY STUDY; FLOW RATE; MULTICOMPONENT EXTRACTIVE DISTILLATION; NONIDEAL MULTICOMPONENT DISTILLATION; NONLINEAR SYSTEM; PHASE SEPARATION; RECTIFICATION BODY METHOD; SCREENING;

EID: 2642527000     PISSN: 00011541     EISSN: None     Source Type: Journal    
DOI: 10.1002/aic.10108     Document Type: Article

References (25)

1. Andersen, H. W., L. Laroche, and M. Morari, "Effect of Design on the Operation of Homogeneous Azeotropic Distillation," Comp. Chem. Eng., 19(1), 105 (1995).
2. Bauer, M. H., and J. Stichlmair, "Design and Economic Optimization of Azeotropic Distillation Processes Using Mixed-Integer Nonlinear Programming," Comp. Chem. Eng., 22(9), 1271 (1998).
3. Bausa, J., "Näherungsverfahren für den konzeptionellen Entwurf und die thermodynamische Analyse von destillativen Trennprozessen, " Reihe 3, Nr. 692, Fortschritt-Berichte VDI, Düsseldorf (2001).
4. Bausa, J., and W. Marquardt, "Shortcut Design Methods for Hybrid Membrane/Distillation Processes for the Separation of Nonideal Multicomponent Mixtures," Ind. Eng. Chem. Res., 39(6), 1658 (2000).
5. Bausa, J., R. v. Watzdorf, and W. Marquardt, "Shortcut Methods for Nonideal Multicomponent Distillation: 1. Simple Columns," AIChE J., 44(10), 2181 (1998).
6. Beyn, W.-J., A. Champneys, E. Doedel, W. Govaerts, Y. A. Kuznetsov, and B. Sanstede, "Numerical Continuation and Computation of Normal Forms, " Handbooks of Dynamical Systems, B. Fiedler, ed., Vol. 2, pp. 149-219 (2002).
7. Black, C., "Distillation Modeling of Ethanol Recovery and Dehydration Processes for Ethanol and Gasohol," Chem. Eng. Prog., 76, 78 (1980).
8. Doherty, M. F., and G. A. Caldarola, "Design and Synthesis of Homogeneous Azeotropic Distillations: 3. The Sequencing of Columns for Azeotropic and Extractive Distillations," Ind. Eng. Chem. Fundam., 24, 474 (1985).
9. Doherty, M. F., and M. F. Malone, Conceptual Design of Distillation Systems, McGraw-Hill, New York (2001).
10. Doherty, M. F., and J. D. Perkins, "On the Dynamics of Distillation Processes-1. The Simple Distillation of Multicomponent Non-reacting, Homogeneous Liquid Mixtures," Ind. Eng. Chem. Proc. Des. Dev., 17, 272 (1978).
11. Fidkowski, Z. T., M. F. Doherty, and M. F. Malone, "Feasibility of Separations for Distillation of Nonideal Ternary Mixtures," AIChE J., 39(8), 1303 (1993).
12. Foucher, E. R., M. F. Doherty, and M. F. Malone, "Automatic Screening of Entrainers for Homogeneous Azeotropic Distillation," Ind. Eng. Chem. Res., 30, 760 (1991).
13. Franklin, N. L., and J. S. Forsyth, "The Interpretation of Minimum Reflux Conditions in Multi-Component Distillation," Trans. Inst. Chem. Eng., 31, 363 (1953).
14. Harper, P. M., R. Gani, P. Kolar, and T. Ishikawa, "Computer-aided Molecular Design with Combined Molecular Modeling and Group Contribution," Fluid Phase Equilibria, 158-160, 337 (1999).
15. Julka, V., and M. F. Doherty, "Geometric Behavior and Minimum Flows for Nonideal Multicomponent Distillation," Chem. Eng. Sci., 45(7), 1801 (1990).
16. Knapp, J. P., and M. F. Doherty, "Minimum Entrainer Flows for Extractive Distillation: A Bifurcation Theoretic Approach," AIChE J., 40(2), 243 (1994).
17. Knight, J. R., and M. F. Doherty, "Optimal Design and Synthesis of Homogeneous Azeotropic Distillation Sequences," Ind. Eng. Chem. Res., 28, 564 (1989).
18. Köhler, J., P. Aguirre, and E. Blass, "Minimum Reflux Calculations for Nonideal Mixtures Using the Reversible Distillation Model," Chem. Eng. Sci., 46(12), 3007 (1991).
19. Laroche, L., N. Bekiaris, H. W. Andersen, and M. Morari, "Homogeneous Azeotropic Distillation: Comparing Entrainers," Can. J. Chem. Eng., 69, 1302 (1991).
20. Laroche, L., N. Bekiaris, H. W. Andersen, and M. Morari, "The Curious Behavior of Homogeneous Azeotropic Distillation-Implications for Entrainer Selection," AIChE J., 38(9), 1309 (1992).
21. Levy, S. G., and M. F. Doherty, "Design and Synthesis of Homogeneous Azeotropic Distillations: 4. Minimum Reflux Calculations for Multiple-Feed Columns," Ind. Eng. Chem. Fundam., 25, 269 (1986).
22. Pham, H. N., P. J. Ryan, and M. F. Doherty, "Design and Minimum Reflux for Heterogeneous Azeotropic Distillation Columns," AIChE J., 35, 1585 (1989).
23. Thong, D. Y.-C., F. J. L. Castillo, and G. P. Towler, "Destillation Design and Retrofit Using Stage-composition Lines," Chem. Eng. Sci., 55, 625 (2000).
24. Underwood, A. J., "Fractional Distillation of Multicomponent Mixtures," Chem. Eng. Prog., 44, 603 (1948).
25. Urdaneta, R. Y., J. Bausa, S. Brüggemann, and W. Marquardt, "Analysis and Conceptual Design of Ternary Heterogeneous Distillation Processes," Ind. Eng. Chem. Res., 41, 3849 (2002).