Hybrid separation processes-Combination of reactive distillation with membrane separation

Chemical Engineering and Processing: Process Intensification

Volumn 46, Issue 9 SPEC. ISS., 2007, Pages 790-799

  Buchaly, Carsten ^a   Kreis, Peter ^a   Górak, Andrzej ^a  

^a TU DORTMUND UNIVERSITY   (Germany)

Author keywords

Distillation; Esterification; Experiments; Hybrid process; Membrane separation; Non equilibrium model; Propyl propionate; Reactive distillation; Vapour permeation

Indexed keywords

COMPUTER SIMULATION; DISTILLATION; DISTILLATION COLUMNS; ESTERIFICATION; NUMERICAL METHODS; PROPANOL; PROPYLENE;

DISTILLATE STREAM; EQUILIBRIUM MODEL; HYBRID PROCESS; VAPOUR PERMEATION;

MEMBRANES;

COMPUTER SIMULATION; DISTILLATION; DISTILLATION COLUMNS; ESTERIFICATION; MEMBRANES; NUMERICAL METHODS; PROPANOL; PROPYLENE;

EID: 34547697759     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cep.2007.05.023     Document Type: Article

References (34)

1. Hiwale R.S., Mahajan Y.S., Bhate N.V., and Mahajani S.M. Industrial applications of reactive distillation: recent trends. Int. J. Chem. Reac. Eng. 2 (2004)
2. Kaibel G., Miller C., Holtmann T., and Schoenmakers H. Reaktivdestillation. Chem. Ing. Tech. 77 11 (2005) 1749-1758
3. Rautenbach R. Membranverfahren- Grundlagen der Modul- und Anlagenauslegung. 1st ed. (1997), Springer-Verlag, Berlin, Heidelberg
4. Lipnitzki F., Field R.W., and Ten P. Pervaporation-based hybrid processes: a review of process design, applications and economics. J. Membr. Sci. 153 (1999) 183-210
5. Kreis P., and Górak A. Process analysis of hybrid separation processes-combination of distillation and pervaporation. Chem. Eng. Res. Des. 84 (2006) 595-600
6. Steinigeweg S., and Gmehling J. Transesterification processes by combination of reactive distillation and pervaporation. Chem. Eng. Proc. 43 (2004) 447-456
7. von Scala C., Fässler P., Gerla J., and Maus E. Kontinuierliche Herstellung von kosmetischen Fettsäureestern mittels Reaktivrektifikation und Pervaporation. Chem. Ing. Tech. 77 11 (2005) 1809-1813
8. E.G. Lundquist, Catalyzed esterification process, US Patent 5,426,199, Rohm and Haas Company (1995).
9. Blagov S., Parada S., Bailer O., Moritz P., Lam D., Weinand R., and Hasse H. Influence of ion-exchange resin catalysts on side reactions of the esterification of n-butanol with acetic acid. Chem. Eng. Sci. 61 (2006) 753-765
10. NIST Chemistry Web Book. http://webbook.nist.gov/chemistry/, December 2005.
11. S. Tlatlik, Description of n-propyl-propionate-synthesis, internal report in the frame of the EU Project "INSERT-Integrating Separation and Reaction Technologies", 2005.
12. Gmehling J. Azeotropic Data (1994), VCH Weinheim
13. Taylor R., and Krishna R. Modelling reactive distillation. Chem. Eng. Sci. 55 (2000) 5183-5229
14. Noeres C., Kenig E.Y., and Górak A. Modelling of reactive separation processes: reactive absorption and reactive distillation. Chem. Eng. Proc. 42 (2003) 157-178
15. Kenig E.Y., and Górak A. In: Keil F.J. (Ed). Modelling of Process Intensification. 1st ed. (2007), Wiley-VCH, Weinheim
16. Richter J., Górak A., and Kenig E.Y. In: Schmidt-Traub H., and Górak A. (Eds). Reactive Distillation (2006), Springer, Heidelberg
17. Hayden J.G., and O'Connell J.P. A generalized method for predicting second virial coefficients. Ind. Eng. Chem. Process Des. Dev. 14 3 (1975) 209-216
18. Duarte C., Buchaly C., Kreis P., and Loureiro J.M. Esterification of propionic acid with n-propanol catalytic and noncatalytic kinetic study. Inz. Chem. Procesowa 27 (2006) 273-286
19. Klöker M., Kenig E.Y., Hoffmann A., Kreis P., and Górak A. Rate-based modelling and simulation of reactive separations in gas/vapour-liquid systems. Chem. Eng. Proc. 44 (2005) 617-629
20. Górak A., and Hoffmann A. Catalytic distillation in structured packings: methyl acetate synthesis. AIChE J. 47 5 (1999) 1067-1076
21. Schneider R., Noeres C., Kreul L.U., and Górak A. Dynamic modelling and simulation of reactive batch distillation. Comp. Chem. Eng. 23 (1999) 423-426
22. E. Brunazzi, Mass Transfer Study of Katapak-SP 11 Packing: Experimental Setup, Measurement Procedures, Correlations, internal report in the frame of the EU Project "INSERT-Integrating Separation and Reaction Technologies", 2006.
23. Brunazzi E., and Viva A. Distillation & Absorption 2006. In: Sorensen E. (Ed). Proceedings of the IChemE Symposium Series No. 152 (2006) 554-562 ISBN 100852955057
24. Bravo J.L., Rocha J.A., and Fair J.R. Mass transfer in gauze packings. Hydrocarbon Process. 1 (1985) 91-95
25. Rocha J.A., Bravo J.L., and Fair J.R. Distillation columns containing structured packings: a comprehensive model for their performance. 1. Hydraulic models. Ind. Eng. Chem. Res. 32 (1993) 641-651
26. DIN Deutsches Institut für Normung, Bestimmung der Totalen Kapazität von Kationenaustauscher, DIN 54403, Deutsche Norm (2000).
27. Buchaly C., Kreis P., and Górak A. Distillation & Absorption 2006. In: Sorensen E. (Ed). Proceedings of the IChemE Symposium Series No. 152 (2006) 373-383 ISBN 100852955057
28. Sulpak 3.0 (2001), Sulzer Chemtech Ltd.
29. M. Schmitt, Heterogen katalysierte Reaktivrektifikation: Stoffdaten, Experimente, Simulation und Scale-up am Beispiel der Synthese von Hexylacetat, PhD Thesis, Institut für Technische Thermodynamik und Thermische Verfahrenstechnik, Universität Stuttgart, 2005.
30. Wijmans J.G. Process PERFORMANCE = membrane properties + operating conditions - letter to the editor. J. Membr. Sci. 220 (2003) 1-3
31. van Baelen D., Reyniers A., van der Bruggen B., Vandecasteele C., and Degreve J. Pervaporation of binary and ternary mixtures of water with methanol and/or ethanol. Sep. Sci Technol. 39 (2004) 563-580
32. O.J. Stange, Stofftransport durch eine hydrophile Polymermembran am Beispiel der Dampfpermeation, PhD Thesis, GKSS-Forschungszentrum Geesthacht GmbH, GKSS 2001/37, 2001.
33. Kreis P., and Górak A. Prozessanalyse hybrider Trennverfahren am Beispiel der Kopplung von Rektifikation und Membrantrennung. Chem. Ing. Tech. 77 11 (2005) 1737-1748
34. Ortega J., and Galvan S. Vapor-liquid equilibria of propyl propanoate with 1-alkanols at 101.32 kPa of pressure. J. Chem. Eng. Data 39 (1994) 907-910