A hybrid modelling approach for separation systems involving distillation

Chemical Engineering Research and Design

Volumn 77, Issue 6, 1999, Pages 519-534

  Schenk, M ^a   Gani, R ^a   Bogle, D ^c   Pistikopoulos, E N ^b  

^a TECHNICAL UNIVERSITY OF DENMARK   (Denmark)

^b IMPERIAL COLLEGE LONDON   (United Kingdom)

^c NONE

Author keywords

Distillation; Equilibrium based; Hybrid modelling; Rate based; Reactive distillation; Separation systems

Indexed keywords

DISTILLATION; PROCESS DESIGN; PROCESS MODEL; PROCESS MONITORING; SIMULATION; SIMULATION MODEL; STEADY STATE;

DESIGN; DISTILLATION COLUMNS; HEAT TRANSFER; MASS TRANSFER; MATHEMATICAL MODELS; PHASE EQUILIBRIA; PROCESS ENGINEERING; SEPARATION;

HYBRID MODELLING; REACTIVE DISTILLATION; SEPARATION SYSTEMS;

DISTILLATION;

BUBBLE SIZE DISTRIBUTION; DISTILLATION; EQUILIBRIUM; FOAM; GAS-LIQUID TWO-PHASE FLOW; MODELING; SURFACTANT;

EID: 0032747510     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1205/026387699526557     Document Type: Article

References (30)

1. Seader, J. D., 1989, The rate-based approach for modelling staged separations, Chem Eng Prog, 85: 41.
2. Taylor, R., and Lucia, A., 1995, Modelling and analysis of multicomponent separation processes, AIChE Symp Series, 91: 19.
3. Kooijman, H.A., and Taylor, R., 1995, A nonequilibrium model for dynamic simulation of tray distillation columns, AIChE J, 41: 1852.
4. Sundmacher, K., and Hoffmann, U., 1996, Development of a new catalytic distillation process for fuel ethers via a detailed nonequilibrium model, Chem Eng Sci, 51: 2359.
5. Higler, A., Krishna, R., and Taylor R., 1998, Modelling a reactive separation process using a non-equilibrium stage model, Comp Chem Eng, 22: S111.
6. Gani, R., Ruiz, C. A., and Cameron, I.T., 1986, A generalized model for distillation columns-I, Comp Chem Eng, 10: 181-199.
7. Krishnamurthy, R., and Taylor, R., 1985, A non-equilibrium stage model of multicomponent separation processes, I and II, AIChE J, 31: 449.
8. Rovaglio, M., and Doherty, M.F., 1990, Dynamics of heterogeneous azeotropic distillation-columns, AIChE J, 36: 39.
9. Skogestad, S., 1997, Dynamics and control of distillation columns - A critical survey, Modelling, Identification and Control, 18: 177.
10. Krishna, R., and Standart, G.L., 1976, A multicomponent film model incorporating the general matrix method of solution to the Maxwell-Stefan equations, AIChE J., 22: 383.
11. AIChE, 1958, Bubble - Tray Design Manual, (AIChE).
12. Taylor, R., Kooijman, H. A., and Woodman, M.R., 1992, Industrial application of a non-equilibrium model of distillation and absorption operations, IChemE Symp Series No. 128, Distillation and Absorption 1992: A415.
13. Taylor, R., and Krishna, R., 1993, Multicomponent Mass Transfer, (Wiley, New York).
14. Gani, R., Sorensen, E.L., Pessergaard, J., 1992, Design and analysis of chemical processes through DYNSIM, Ind Eng Chem Res, 31: 244.
15. Bossen, B.S., Jørgensen, S.B., and Gani, R., 1993, Simulation, design, and analysis of azeotropic distillation operations, Ind Eng Chem Res, 32: 620.
16. Gokhale, V., Hurowitz, S., and J.B. Riggs, 1995, A Comparison of advanced distillation control techniques for a propylene/propane splitter, Ind Eng Chem Res, 34: 4413.
17. King, C. J., 1980, Separation Processes, Second Edition, (Mc.Graw-Hill, NY).
18. Daubert, T.E., and Danner, R.P., 1986, DIPPR Data Compilation, (AIChE, New York).
19. Cameron, I. T., Ruiz, C. A., and Gani, R., 1986, A generalized model for distillation columns-II. Comp Chem Eng, 10: 199.
20. Gani, R., and Cameron, I. T., 1989, Extension of dynamic models of distillation columns to steady state simulation, Comp Chem Engng, 13: 271.
21. Taylor, R., Kooijman, H. A., and Hung, J. S., 1994, A second generation of nonequilibrium model for the computer simulation of multicomponent separation processes, Comp Chem Eng, 18: 205.
22. Schrieber, I., and M. Marek, 1995, Chaotic Behaviour of Deterministic Dissipative Systems, (Cambridge University Press, Cambridge).
23. Gani, R., Hytoft, G., Jaksland C.,and Jensen, A.K., 1997, An integrated computer aided system for integrated design of chemical process, Comp Chem Eng, 21: 1135.
24. gPROMS User Guide, 1997, (Process Systems Enterprise Ltd.).
25. Pilavachi, P. A., Schenk, M., Pérez-Cisneros, E., and Gani, R., 1997, Modelling and simulation of reactive distillation operations, Ind Eng Chem Res, 36: 3188.
26. Rehfinger, A., and Hoffmann, U., 1990, Kinetics of methyl tertiary butyl ether liquid phase synthesis catalyzed by ion exchange resin-I. Intrinsic rate expression in liquid phase activities, Chem Eng Sci, 45: 1605.
27. Suzuki, I., Yagi, H., Komatsu, H., and Hirata, M., 1971, Calculation of multicomponent distillation accompanied by a chemical reaction, J Chem Eng Japan, 4: 26.
28. Bock, H, Jimoh, M., and, Wozny, G., 1997, Analysis of reactive distillation using the esterification of acetic acid as an example, Chem Eng Technol, 20: 182.
29. Bravo, J. L., and Fair, J. R., 1982, Generalised correlation for mass transfer in packed distillation columns, Ind Eng Chem Proc Des Dev, 21: 170.
30. Onda, K., Takeuchi, H., and Okumoto, Y., 1968, Mass transfer coefficients between gas and liquid phases in packed columns, J Chem Eng Japan, 1.