Impact of mass transfer coefficient correlations on prediction of reactive distillation column behaviour

Chemical Engineering Journal

Volumn 140, Issue 1-3, 2008, Pages 381-390

  Svandova Z ^a   Markos J ^a   Jelemenský, Ľ ^a  

^a SLOVAK UNIVERSITY OF TECHNOLOGY   (Slovakia)

Author keywords

Mass transfer coefficient; Multiple steady states; Nonequilibrium model; Reactive distillation; Sensitivity to model parameters prediction

Indexed keywords

BINARY MIXTURES; CORRELATION METHODS; DISTILLATION; MATHEMATICAL MODELS;

MULTIPLE STEADY STATES; NONEQUILIBRIUM MODEL; PARAMETERS PREDICTION; REACTIVE DISTILLATION;

MASS TRANSFER;

BINARY MIXTURES; CORRELATION METHODS; DISTILLATION; MASS TRANSFER; MATHEMATICAL MODELS;

EID: 44349159508     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2007.10.022     Document Type: Article

References (41)

1. Švandová Z., Jelemenský L., Markoš J., and Molnár A. Steady state analysis and dynamical simulation as a complement in the HAZOP study of chemical reactors. Trans. IChemE, Part B: Process Saf. Environ. Prot. 83 B5 (2005) 463-471
2. Švandová Z., Markoš J., and Jelemenský L. HAZOP analysis of CSTR with utilization of mathematical modeling. Chem. Pap. 59 6b (2005) 464-468
3. Labovský J., Jelemenský L., and Markoš J. Safety analysis and risk identification for tubular reactor using the HAZOP methodology. Chem. Pap. 60 6 (2006) 454-459
4. Labovský J., Švandová Z., Markoš J., and Jelemenský L. Model-based HAZOP study of a real MTBE plant. J. Loss Prev. Proc. 20 3 (2007) 230-237
5. Labovský J., Švandová Z., Markoš J., and Jelemenský L. Mathematical model of a chemical reactor-useful tool for its safety analysis and design. Chem. Eng. Sci. 62 (2007) 4915-4919
6. Molnár A., Markoš J., and Jelemenský L. Some considerations for safety analysis of chemical reactors. Trans. IChemE, Part A: Chem. Eng. Res. Des. 83 A2 (2005) 167-176
7. Taylor R., and Krishna R. Modelling reactive distillation. Chem. Eng. Sci. 55 22 (2000) 5183-5229
8. Mohl K.-D., Kienle A., Gilles E.-D., Rapmund P., Sundmacher K., and Hoffmann U. Steady-state multiplicities in reactive distillation columns for the production of fuel ethers MTBE and TAME: theoretical analysis and experimental verification. Chem. Eng. Sci. 54 8 (1999) 1029-1043
9. Thiel C., Rapmund P., Sundmacher K., Hoffmann U., Mohl K.D., Kienle A., and Gilles E.D. Intensified production of fuel ethers in reactive distillation columns-experimental validation of predicted multiple steady states. Proceedings of the first European Congress on Chemical Engineering-ECCE-1, vol. 2. Florence (1997) 1423-1426
10. Jacobs R., and Krishna R. Multiple solutions in reactive distillation for methyl tert-butyl ether synthesis. Ind. Eng. Chem. Res. 32 8 (1993) 1706-1709
11. Higler A.P., Taylor R., and Krishna R. Nonequilibrium modelling of reactive distillation: multiple steady states in MTBE synthesis. Chem. Eng. Sci. 54 10 (1999) 1389-1395
12. Chen F., Huss R.S., Doherty M.F., and Malone M.F. Multiple steady states in reactive distillation: kinetic effects. Comput. Chem. Eng. 26 1 (2002) 81-93
13. Noeres C., Kenig E.Y., and Górak A. Modelling of reactive separation processes: reactive absorption and reactive distillation. Chem. Eng. Process. 42 3 (2003) 157-178
14. Taylor R., and Krishna R. Multicomponent Mass Transfer (1993), John Wiley & Sons, Inc., New York
15. Švandová Z., Kotora M., Markoš J., and Jelemenský L. Dynamic behaviour of a CSTR with reactive distillation. Chem. Eng. J. 119 (2006) 113-120
16. Švandová Z., Markoš J., and Jelemenský L. Multiple steady states in a CSTR with total condenser: comparison of equilibrium and nonequilibrium models. Chem. Pap. 60 6 (2006) 432-440
17. Švandová Z., Labovský J., Markoš J., and Jelemenský L. Impact of mathematical model selection on prediction of steady state and dynamic behaviour of a reactive distillation column. In: Plesu V./E., and Agachi P.S./E. (Eds). Computer Aided Chemical Engineering vol. 24 (2007), Elsevier, Amsterdam 1235-1240 ISBN 987-0-444-53157-5
18. Baur R., Higler A.P., Taylor R., and Krishna R. Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation. Chem. Eng. J. 76 1 (2000) 33-47
19. Kooijman H.A., and Taylor R. The ChemSep Book (2000), Libri Books on Demand, Norderstedt
20. http://www.sulzerchemtech.com/desktopdefault.aspx
21. http://www.koch-glitsch.com
22. A. Górak, L.U. Kreul, M. Skowronski, Strukturierte Mehrzweckpakung, Deutsches Patent 19,701,045 (1997).
23. Górak A. Modelling reactive distillation. Proceedings of the 33rd International Conference of Slovak Society of Chemical Engineering. Tatranské Matliare, Slovakia (2006). 80-227-2409-2 (Plenary lecture)
24. Kolodziej A., Górak A., and Jaroszynski M. Reactive distillation: a success story with obstacles. Proceedings of the 34th International Conference of Slovak Society of Chemical Engineering. Tatranské Matliare, Slovakia (2007). 978-80-227-2640-5 (Plenary lecture)
25. INTINT project: Intelligent column internals for reactive separation, http://www.cpi.umist.ac.uk/intint.
26. Buchaly C., Kreis P., and Górak A. Hybrid separation processes-combination of reactive distillation with membrane separation. Chem. Eng. Process. 46 9 (2007) 790-799
27. M. Kotora, C. Buchaly, P. Kreis, A. Górak, J. Markoš, Reactive distillation-experimental data for n-propyl propionate synthesis, Chem. Pap. 61(1) (2008), in press.
28. Krishnamurthy R., and Taylor R. A nonequilibrium stage model of multicomponent separation processes. I-Model description and method of solution. AIChE J. 31 3 (1985) 449-456
29. Krishnamurthy R., and Taylor R. A nonequilibrium stage model of multicomponent separation processes. II-Comparison with experiment. AIChE J. 31 3 (1985) 456-465
30. Reid R.C., Prausnitz J.M., and Sherwood T.K. The Properties of Gases and Liquids. third ed. (1977), McGraw-Hill, New York
31. Perry R.H., Green D.W., and Maloney J.O. Perry's Chemical Engineers' Handbook. seventh ed. (1997), McGraw-Hill, New York
32. Wesselingh J.A., and Krishna R. Mass Transfer (1990), Ellis Horwood, Chichester, England
33. Rehfinger A., and Hoffmann U. 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 6 (1990) 1605-1617
34. E.M. Jones Jr., Contact structure for use in catalytic distillation, US Patent 4,536,373 (1985).
35. Kubíček M. Algorithm 502. Dependence of solution of nonlinear systems on a parameter [C5]. ACM Trans. Math. Software 2 1 (1976) 98-107
36. Kooijman H.A., and Taylor R. Modelling mass transfer in multicomponent distillation. Chem. Eng. J. 57 2 (1995) 177-188
37. Hauan S., Hertzberg T., and Lien K.M. Multiplicity in reactive distillation of MTBE. Comput. Chem. Eng. 21 10 (1997) 1117-1124
38. AICHE Bubble Tray Design Manual (1958), AIChE, New York
39. Chan H., and Fair J.R. Prediction of point efficiencies on sieve trays. 1: Binary systems. Ind. Eng. Chem. Des. Dev. 23 4 (1984) 814-819
40. Chen G.X., and Chuang K.T. Prediction of point efficiency for sieve trays in distillation. Ind. Eng. Chem. Res. 32 (1993) 701-708
41. Zuiderweg F.J. Sieve trays: a view on the state of the art. Chem. Eng. Sci. 37 10 (1982) 1441-1464