[article]
Titre : |
Hydroformylation of 1-butene on Rh catalyst |
Type de document : |
texte imprimé |
Auteurs : |
Tapio Salmi, Auteur ; Johan Ahlkvist, Auteur ; Andreas Bernas, Auteur |
Année de publication : |
2009 |
Article en page(s) : |
p. 1325–1331 |
Note générale : |
Chemical engineering |
Langues : |
Anglais (eng) |
Mots-clés : |
Hydroformylation Rhodium catalyst Butene |
Résumé : |
Kinetics of homogeneously catalyzed hydroformylation of 1-butene was studied in a pressurized semibatch autoclave reactor. Kinetics was determined for a reaction mixture, which consisted of 1-butene, carbon monoxide, hydrogen, a rhodium-based catalyst, and 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate as a solvent. The following reaction parameters were investigated: temperature (70−100 °C), total pressure (1−3 MPa), catalyst concentration (100−200 ppm), catalyst (Rh)-to-ligand ratio, and the initial ratio of the synthesis gas (hydrogen and carbon dioxide) components. The solubility of 1-butene, carbon monoxide, and hydrogen in the solvent was determined by precise pressure and weight measurements and modeled mathematically. The main reaction products were pentanal (P) and 2-methylbutanal (MB), while trace amounts of cis-2- and trans-2-butene were detected as reaction intermediates. The ratio of the main products (P and MB) was practically independent of temperature, but the ligand-to-Rh ratio affected considerably the product distribution: an increasing ratio preferred the formation of pentanal (P). Increasing total pressure diminished the yield of pentanal (P). On the basis of the experimentally recorded kinetic data, a stoichiometric scheme was constructed and simplified. The kinetic data were combined with solubility models, and the parameters of an empirical power-law rate model were determined by nonlinear regression analysis. The kinetic parameters were well identified and physically reasonable being in accordance with qualitative observations. |
En ligne : |
http://pubs.acs.org/doi/abs/10.1021/ie800215t |
in Industrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1325–1331
[article] Hydroformylation of 1-butene on Rh catalyst [texte imprimé] / Tapio Salmi, Auteur ; Johan Ahlkvist, Auteur ; Andreas Bernas, Auteur . - 2009 . - p. 1325–1331. Chemical engineering Langues : Anglais ( eng) in Industrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1325–1331
Mots-clés : |
Hydroformylation Rhodium catalyst Butene |
Résumé : |
Kinetics of homogeneously catalyzed hydroformylation of 1-butene was studied in a pressurized semibatch autoclave reactor. Kinetics was determined for a reaction mixture, which consisted of 1-butene, carbon monoxide, hydrogen, a rhodium-based catalyst, and 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate as a solvent. The following reaction parameters were investigated: temperature (70−100 °C), total pressure (1−3 MPa), catalyst concentration (100−200 ppm), catalyst (Rh)-to-ligand ratio, and the initial ratio of the synthesis gas (hydrogen and carbon dioxide) components. The solubility of 1-butene, carbon monoxide, and hydrogen in the solvent was determined by precise pressure and weight measurements and modeled mathematically. The main reaction products were pentanal (P) and 2-methylbutanal (MB), while trace amounts of cis-2- and trans-2-butene were detected as reaction intermediates. The ratio of the main products (P and MB) was practically independent of temperature, but the ligand-to-Rh ratio affected considerably the product distribution: an increasing ratio preferred the formation of pentanal (P). Increasing total pressure diminished the yield of pentanal (P). On the basis of the experimentally recorded kinetic data, a stoichiometric scheme was constructed and simplified. The kinetic data were combined with solubility models, and the parameters of an empirical power-law rate model were determined by nonlinear regression analysis. The kinetic parameters were well identified and physically reasonable being in accordance with qualitative observations. |
En ligne : |
http://pubs.acs.org/doi/abs/10.1021/ie800215t |
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