Rapid screening of design alternatives for nonideal multiproduct distillation processes

Computers and Chemical Engineering

Volumn 29, Issue 1, 2004, Pages 165-179

  Brüggemann, Stefan ^a   Wolfgang, Marquardt ^a  

^a RWTH AACHEN UNIVERSITY   (Germany)

Author keywords

Energy integrated distillation; Minimum energy demand; Process screening; Rectification body method; Shortcut methods

Indexed keywords

ENERGY DEMAND; IDEAL MIXTURES; MUTICOMPONENT MIXTURES; RECTIFICATION BODY METHOD (RBM);

ECONOMICS; ENERGY POLICY; LOGIC DESIGN; MIXTURES; SOLUTIONS; THERMOANALYSIS;

DISTILLATION;

CHEMICAL ENGINEERING;

CONFERENCE PAPER; DECISION MAKING; DECOMPOSITION; DISTILLATION; ENERGY CONSUMPTION; ENERGY COST; HEAT; PROCESS DESIGN; RELIABILITY; SEPARATION TECHNIQUE; STEADY STATE;

EID: 9644264140     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.compchemeng.2004.07.009     Document Type: Conference Paper

References (34)

1. Agrawal R. Thermally coupled distillation with reduced number of intercolumn vapor transfers AIChE J. 46 2000 2198
2. Agrawal R. Synthesis of multicomponent distillation column configurations AIChE J. 49 2003 379
3. Agrawal R., and Fidkowski Z.T. Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? Ind. Eng. Chem. Res. 37 1998 3444
4. Agrawal R., and Fidkowski Z.T. Thermodynamically efficient systems for ternary distillation Ind. Eng. Chem. Res. 38 1999 2065
5. Bauer M.H., and Stichlmair J. Design and economic optimization of azeotropic distillation processes using mixed-integer nonlinear programming Comp. Chem. Eng. 22 1998 1271
6. Bausa J., von Watzdorf R., and Marquardt W. Shortcut methods for nonideal multicomponent distillation: 1. Simple columns AIChE J. 44 1998 2181
7. Bekiaris N., Meski G.A., Radu C.M., and Morari M. Multiple steady states in homogeneous azeotropic distillation Ind. Eng. Chem. Res. 32 1993 2023
8. Biegler L.T., Grossmann I.E., and Westerberg A.W. Systematic methods of chemical process design 1997 Prentice-Hall New Jersey
9. Brüggemann, S., & Marquardt, W. (2004). Shortcut methods for nonideal multicomponent distillation: 3. Extractive distillation columns. AIChE J., 50, 1129.
10. Caballero J.A., and Grossmann I.E. Generalized disjunctive programming model for the optimal synthesis of thermally linked distillation columns Ind. Eng. Chem. Res. 40 2001 2260
11. Carlberg N.A., and Westerberg A.W. Temperature-heat diagrams for complex columns. 2. Underwood's method for side strippers and enrichers Ind. Eng. Chem. Res. 28 1989 1379
12. Carlberg N.A., and Westerberg A.W. Temperature-heat diagrams for complex columns 3 Underwood's method for the Petlyuk configuration Ind. Eng. Chem. Res. 28 1989 1386
13. Dünnebier G., and Pantelides C.C. Optimal design of theramlly coupled distillation columns Ind. Eng. Chem. Res. 38 1999 162
14. Esbjerg K., Andersen T.R., Müller D., Marquardt W., and Jørgensen S.B. Multiple steady states in heterogeneous azeotropic distillation sequences Ind. Eng. Chem. Res. 37 1998 4434
15. Franklin N.L., and Forsyth J.S. The interpretation of minimum reflux conditions in multi-component distillation Trans. Inst. Chem. Eng. 31 1953 363
16. Halvorsen I.J., and Skogestad S. Optimal operation of Petlyuk distillation: steady-state behavior J. Proc. Contr. 9 1999 407
17. Halvorsen I.J., and Skogestad S. Minimum energy consumption in multicomponent distillation 2 Three-product Petlyuk arrangements Ind. Eng. Chem. Res. 42 2003 605
18. Halvorsen I.J., and Skogestad S. Minimum energy consumption in multicomponent distillation 3 More than three products and generalized Petlyuk arrangements Ind. Eng. Chem. Res. 42 2003 616
19. Güttinger T.E., and Morari M. Multiple steady states in homogeneous separation sequences Ind. Eng. Chem. Res. 35 1996 4597
20. Julka V., and Doherty M.F. Geometric behavior and minimum flows for nonideal multicomponent distillation Chem. Eng. Sci. 45 1990 1801
21. Kaibel G., and Schoenmakers H. Process synthesis and design in industrial practice Eur. Symp. Computer-Aided Process Eng. 12 2002 9
22. Köhler J., Aguirre P., and Blass E. Minimum reflux calculations for nonideal mixtures using the reversible distillation model Chem. Eng. Sci. 46 1991 3007
23. Levy G.S., van Dongen D.B., and Doherty M.F. Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns Ind. Eng. Chem. Fundam. 24 1985 463
24. Rev E., Emtir M., Szitkai Z., Miszey P., and Fonyo Z. Energy savings of integrated and coupled distillation systems Comp. Chem. Eng. 25 2001 119
25. Rong B-G., Kraslawski A., and Turunen I. Synthesis of functionally distinct thermally coupled configurations for quaternary distillations Ind. Eng. Chem. Res. 42 2003 1204
26. Shah P.B. Sqeeze more out of complex columns Chem. Eng. Prog. 98 2002 46
27. Stichlmair J.G., and Fair J.R. Distillation-principles and practices 1998 Wiley-VCH New York
28. Timoshenko A.V., Patkina O.D., and Serafimov L.A. Synthesis of optimal distillation flowsheets consisting of columns with various numbers of sections Theo. Found. Chem. Eng. 35 2001 458
29. Triantafyllou C., and Smith R. The design and optimisation of fully thermally coupled distillation columns. Trans. I. Chem. Eng. 70 1992 118
30. Underwood A.J. Fractional distillation of multicomponent mixtures Chem. Eng. Prog. 44 1948 603
31. Watzdorf R.von., Bausa J., and Marquardt W. Shortcut methods for nonideal multicomponent distillation: 2. Complex columns AIChE J. 45 1999 1615
32. Wenzel S., and Röhm H.-J. Auslegung thermisch und stofflich gekoppelter Destillationskolonnen mittels Gesamtkostenoptimierung Chemie Ingenieur Technik 75 2003 534
33. Westerberg A.W. The synthesis of distillation-based separation systems Comp. Chem. Eng. 9 1985 421
34. Wolff E.A., and Skogestad S. Operation of integrated three-product (Petlyuk) distillation columns Ind. Eng. Chem. Res. 34 1995 2094