[article]
Titre : |
Isoprene and C5 olefins production by oxidative dehydrogenation of isopentane |
Type de document : |
texte imprimé |
Auteurs : |
Rita X Valenzuela, Auteur ; Josè M. Asperilla, Auteur ; Vicente Cortés, Auteur |
Année de publication : |
2008 |
Article en page(s) : |
p.8037–8042 |
Note générale : |
Chemical engineering |
Langues : |
Anglais (eng) |
Mots-clés : |
oxidative dehydrogenation soprene and isoamylenes |
Résumé : |
The current limited availability of isoprene and isoamylenes (methyl butenes), which are the feedstock for a variety of petrochemical processes, could be boosted by converting the isopentane contained in the same refinery C5-fractions from which they are obtained. The oxidative dehydrogenation (ODH) of isopentane to isoprene and isoamylenes for this purpose has been studied very little to date. We present here a study of this reaction on oxide catalysts, using oxygen as an oxidant, without any dopant in the feed. After a broad catalyst formulations screening, a V−Mg oxide catalyst (15 wt % V2O5) was selected to study the influence of the reaction parameters (temperature, residence time, and feed composition). Selectivity values of ca. 25% to isoprene, and 70% to isoprene plus isomylenes, could be attained under selected reaction conditions. These results are promising for the direct conversion of the branched C5-hydrocarbons fraction to isoprene. |
En ligne : |
http://pubs.acs.org/toc/iecred/47/21 |
in Industrial & engineering chemistry research > Vol. 47 n°21 (Novembre 2008) . - p.8037–8042
[article] Isoprene and C5 olefins production by oxidative dehydrogenation of isopentane [texte imprimé] / Rita X Valenzuela, Auteur ; Josè M. Asperilla, Auteur ; Vicente Cortés, Auteur . - 2008 . - p.8037–8042. Chemical engineering Langues : Anglais ( eng) in Industrial & engineering chemistry research > Vol. 47 n°21 (Novembre 2008) . - p.8037–8042
Mots-clés : |
oxidative dehydrogenation soprene and isoamylenes |
Résumé : |
The current limited availability of isoprene and isoamylenes (methyl butenes), which are the feedstock for a variety of petrochemical processes, could be boosted by converting the isopentane contained in the same refinery C5-fractions from which they are obtained. The oxidative dehydrogenation (ODH) of isopentane to isoprene and isoamylenes for this purpose has been studied very little to date. We present here a study of this reaction on oxide catalysts, using oxygen as an oxidant, without any dopant in the feed. After a broad catalyst formulations screening, a V−Mg oxide catalyst (15 wt % V2O5) was selected to study the influence of the reaction parameters (temperature, residence time, and feed composition). Selectivity values of ca. 25% to isoprene, and 70% to isoprene plus isomylenes, could be attained under selected reaction conditions. These results are promising for the direct conversion of the branched C5-hydrocarbons fraction to isoprene. |
En ligne : |
http://pubs.acs.org/toc/iecred/47/21 |
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