Advanced kinetic concepts and experimental methods for catalytic three-phase processes

Industrial and Engineering Chemistry Research

Volumn 43, Issue 16, 2004, Pages 4540-4550

  Salmi, Tapio ^a   Murzin, Dmitry Yu ^a   Mikkola, Jyri Pekka ^a   Wärnå, Johan ^a   Mäki Arvela, Päivi ^a   Toukoniitty, Esa ^a   Toppinen, Sami ^a  

^a ÅBO AKADEMI UNIVERSITY   (Finland)

Author keywords

[No Author keywords available]

Indexed keywords

ADSORPTION; ALDEHYDES; AROMATIC COMPOUNDS; CATALYSIS; CHEMICAL REACTORS; HYDROGENATION; MATHEMATICAL MODELS;

ENANTIOSELECTIVE HYDROGENATION; LANGMUIR-HINSHELWOOD CONCEPT; THREE PHASE SYSTEMS;

REACTION KINETICS;

ALDEHYDE;

KINETICS;

ADSORPTION; ARTICLE; AUTOCLAVE; CATALYSIS; CHEMICAL REACTION KINETICS; ENANTIOSELECTIVITY; HYDROGENATION; MATHEMATICAL MODEL;

EID: 3543044981     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0307481     Document Type: Article

References (21)

1. Smith, J. M. Chemical Engineering Kinetics, 3rd ed.; McGraw Hill: New York, 1990.
2. Kobayashi, H; Kobayashi, M. Transient response method in heterogeneous catalysis. Catal. Rev.-Sci. Eng. 1974, 10, 1139-1176.
3. Bennett, C. O. Experiments and processes in the transient regime for heterogeneous catalysis. Adv. Catal. 2002, 44, 330-416.
4. Matros, Yu. Sh. Unsteady Processes in Catalytic Reactors; Elsevier: Amsterdam, 1985.
5. Eigenberger, G.; Nieken, U. Katalytische Abluftreinigung: verfahrenstechnische Aufgaben und neue Lösungen. Chem. Ing. Tech. 1991, 63, 781-791.
6. Salmi, T.; Wärnå, J.; Toppinen, S.; Rönnholm, M.; Mikkola, J.-P. Dynamic modelling of catalytic three-phase reactors for hydrogenation and oxidation processes. Braz. J. Chem. Eng. 2000, 17, 1023-1035.
7. Rönnholm, M. R.; Wärnå, J.; Salmi, T. Two- and three-phase oxidation of ferrous sulfate to ferric sulfate-Prom intrinsic kinetics to diffusion-affected kinetics. Chem. Eng. Process. 2002, 41, 753-760.
8. Toppinen, S.; Rantakylä, T.-K.; Salmi, T.; Aittamaa, J. Kinetics of the liquid-phase hydrogenation of benzene and some monosubstituted alkylbenzenes over a Ni catalyst. Ind. Eng. Chem. Res. 1996, 35, 1824-1833.
9. Toppinen, S.; Salmi, T.; Rantakylä, T.-K.; Aittamaa, J. Liquid-phase hydrogenation kinetics of aromatic hydrocarbon mixtures. Ind. Eng. Chem. Res. 1887, 36, 2101-2109.
10. Taylor, R.; Krishna, R. Multicomponent Mass Transfer; Wiley: New York, 1993.
11. Fott, P.; Schneider, P. Multicomponent mass transport with complex reaction in porous catalyst. In Recent Advances in the Engineering Analysis of Chemically Reacting Systems; Doraiswamy, L. K., Ed.; Wiley Eastern: New Dehli, India, 1984.
12. Berger, R. J.; Stitt, E. H.; Marin, G. B.; Kapteijn, F.; Moulijn, J. A. Chemical reaction kinetics in practice. CATTECH 2000, 4, 2-32.
13. Boudart, M.; Djéga-Mariadassou, G. Kinetics of Heterogeneous Catalytic Reactions; Princeton University Press: Princeton, NJ, 1984.
14. Laidler, K. J. Chemical Kinetics; Harper & Row: New York, 1987.
15. Temkin, M. I. The kinetics of some industrial heterogeneous catalytic reactions. Adv. Catal. 1979, 28, 173-292.
16. Snagovskii, Yu. S.; Ostrovskii, G. M. Modeling of Kinetics of Heterogeneous Catalytic Processes; Chimia: Moscow, USSR, 1976 (in Russian).
17. Toukoniitty, E.; Sevcikova, B.; Mäki-Arvela, P.; Wärnå, J.; Salmi, T.; Murzin, D. Yu. Kinetics and modeling of 1-phenyl-1,2-propanedione hydrogenation. J. Catal. 2003, 213, 7-16.
18. Murzin, D.; Salmi, T,; Smeds, S.; Laatikainen, M.; Mustonen, M.; Paatero, E. Toluene and methylcyclohexane adsorption on nickel catalysts. React. Kinet. Catal. Lett. 1997, 61, 227-236.
19. Mikkola, J.-P.; Vainio, H,; Salmi, T.; Sjöholm, R,; Ollonqvist, T.; Väyrynen, J. Deactivation kinetics of Mo-promoted Raney Ni catalyst in the hydrogenation of xylose to xylitol. Appl. Catal. A 2000, 196, 143-155.
20. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The Properties of Gases and Liquids; McGraw Hill: New York, 1988.
21. Blaser, H.-U.; Jalett, H.-P.; Wiehl, J. J. Mol. Catal. 1996, 107, 85.