Intensification of paraxylene production using a simulated moving bed reactor;Intensification de la production de paraxylène à l'aide du lit mobile simulé réactif

Oil and Gas Science and Technology

Volumn 65, Issue 5, 2010, Pages 721-733

  Bergeot, G ^a   Leinekugel Le Cocq, D ^a   Wolff, L ^a   Muhr, L ^b   Bailly, M ^b  

^a IFP ENERGIES NOUVELLES   (France)

^b UNIVERSITÉ DE LORRAINE   (France)

Author keywords

[No Author keywords available]

Indexed keywords

ADSORPTION AND REACTIONS; ANALYTICAL MODEL; EXPERIMENTAL DATA; FIXED BED REACTOR; HZSM-5 ZEOLITES; INDUSTRIAL PROCESSS; LIQUID PHASE; LIQUID PHASE ISOMERIZATION; MULTIFUNCTIONAL REACTOR; OPERATING REGIMES; PARAXYLENE; PRODUCTION PROCESS; PRODUCTIVITY LOSS; RAFFINATES; REACTION STEPS; RECYCLE FLOW; RECYCLE STREAM; SAVE ENERGY; SIMULATED MOVING BED REACTOR; SUSTAINABLE PROCESS; TRUE MOVING BED; XYLENE SEPARATIONS;

ADSORPTION; AROMATIC HYDROCARBONS; CHEMICAL REACTORS; ENVIRONMENTAL IMPACT; FLUIDIZED BEDS; HYDRAULICS; INVESTMENTS; LIQUIDS; MATHEMATICAL MODELS; OPERATING COSTS; RECYCLING; TOLUENE; XYLENE;

COUPLED CIRCUITS;

ADSORPTION; BIOREACTOR; ENERGY CONSERVATION; NUMERICAL MODEL; SEPARATION; TOLUENE; XYLENE;

EID: 78149489570     PISSN: 12944475     EISSN: None     Source Type: Journal    
DOI: 10.2516/ogst/2009086     Document Type: Article

References (17)

1. Bergeot G., Leinekugel-Le-Cocq D., Leflaive P., Laroche C., Muhr L., Bailly M. (2009) Simulated moving bed reactor for paraxylene production, Chem. Eng. Trans. 17, 87-92.
2. Chirico R.D., Steele W.V. (1997) Thermodynamic Equilibria in Xylene Isomerization. 5. Xylene Isomerization Equilibria from Thermodynamic Studies and Reconciliation of Calculated and Experimental Product Distributions, J. Chem. Eng. Data 42, 4, 784-790.
3. Da Silva F.A., Silva J.A., Rodrigues A.E. (1999) A General Package for the Simulation of Cyclic Adsorption Processes, Adsorption 5, 3, 229-244.
4. Dulot H. (2000) Modélisation de réacteurs-adsorbeurs mis en œuvre en lit simulé. Application à la conversion et à la séparation d'hydrocarbures aromatiques, PhD Thesis, novembre 2000.
5. Fish B., Carr R.W., Aris R. (1986) The continuous countercurrent moving bed chromatographic reactor, Chem. Eng. Sci. 41, 4, 661-668.
6. Ganetsos G., Barker P.E., Ajongwen J.N. (1993) Batch and continuous chromatographic systems as combined bioreactor-separators, in Preparative and production scale chromatography, Ganetsos G., Barker P.E. (eds), Marcel Dekker.
7. Hashimoto K., Adachi S., Noujima H., Ueda Y. (1983) A new process combining adsorption and enzyme reaction for producing higher-fructose syrup, Biotechnol. Bioeng. 25, 10, 2371-2393.
8. Kurup A.S., Subramani H.J., Hidajat K., Ray A.K. (2005) Optimal design and operation of SMB bioreactor for sucrose inversion, Chem. Eng. J. 108, 1-2, 19-33.
9. Lode F., Houmard M., Migliorini C., Mazzotti M., Morbidelli M. (2001) Continuous reactive chromatography, Chem. Eng. Sci. 56, 2, 269-291.
10. Minceva M., Gomes P.S., Meshko V., Rodrigues A.E. (2008) Simulated moving bed reactor for isomerization and separation of p-xylene, Chem. Eng. J. 140, 1-3, 305-323.
11. Ruthven D.M., Ching C.B. (1989) Counter-Current and Simulated Counter-Current Adsorption Separation Processes, Chem. Eng. Sci. 44, 1011-1038.
12. Sardin M., Schweich D., Villermaux J. (1993) Preparative fixed-bed chromatographic reactor, in Preparative and production scale chromatography, Ganetsos G., Barker P.E. (eds), Marcel Dekker.
13. Schmidt-Traub H., Strube J. (1996) Dynamic simulation of simulated-moving-bed chromatographic processes, Comput. Chem. Eng. 20, Supplement 1, S641-S646.
14. Storti G., Baciocchi R., Mazzotti M., Morbidelli M. (1995) Design of Optimal Operating Conditions of Simulated Moving Bed Adsorptive Separation Units, Ind. Eng. Chem. Res. 34, 1, 288-301.
15. Takeuchi K., Uraguchi Y. (1977) Experimental studies of a chro-matographic moving-bed reactor, J. Chem. Eng. Jpn 10, 6, 455-460.
16. Takeuchi K., Uraguchi Y. (1976) Separation conditions of the reactant and the product with a chromatographic moving bed reactor, J. Chem. Eng. Jpn 9, 2, 164-166.
17. Yu W., Hidajat K., Ray A.K. (2005) Optimization of reactive simulated moving bed and Varicol systems for hydrolysis of methyl acetate, Chem. Eng. J. 112, 1-3, 57-72.