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Détail de l'auteur
Auteur David Cresswell
Documents disponibles écrits par cet auteur
Affiner la rechercheDetailed reaction kinetics for the dehydrogenation of methylcyclohexane over Pt catalyst / Muhammad Usman in Industrial & engineering chemistry research, Vol. 51 N° 1 (Janvier 2012)
[article]
in Industrial & engineering chemistry research > Vol. 51 N° 1 (Janvier 2012) . - pp. 158–170
Titre : Detailed reaction kinetics for the dehydrogenation of methylcyclohexane over Pt catalyst Type de document : texte imprimé Auteurs : Muhammad Usman, Auteur ; David Cresswell, Auteur ; Arthur Garforth, Auteur Année de publication : 2012 Article en page(s) : pp. 158–170 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Kinetics Résumé : Detailed reaction kinetics of the dehydrogenation of methylcyclohexane were studied over an in-house-prepared 1.0 wt % Pt/γ-Al2O3 catalyst. Experiments were conducted in a fixed-bed reactor for a wide range of operating conditions including reactions without hydrogen in the feed. Kinetic model equations were developed, and the experimental data were analyzed according to the power-law, Langmuir–Hinshelwood–Hougen–Watson (LHHW), and Horiuti–Polanyi kinetic mechanisms. The rate of loss of the first hydrogen molecule in the LHHW single-site surface reaction mechanism was found to be the rate-controlling step. Experiments with 1-methylcyclohexene confirmed that the rate-controlling step does not lie after the loss of the first hydrogen molecule. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie201539v [article] Detailed reaction kinetics for the dehydrogenation of methylcyclohexane over Pt catalyst [texte imprimé] / Muhammad Usman, Auteur ; David Cresswell, Auteur ; Arthur Garforth, Auteur . - 2012 . - pp. 158–170.
Chimie industrielle
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 51 N° 1 (Janvier 2012) . - pp. 158–170
Mots-clés : Kinetics Résumé : Detailed reaction kinetics of the dehydrogenation of methylcyclohexane were studied over an in-house-prepared 1.0 wt % Pt/γ-Al2O3 catalyst. Experiments were conducted in a fixed-bed reactor for a wide range of operating conditions including reactions without hydrogen in the feed. Kinetic model equations were developed, and the experimental data were analyzed according to the power-law, Langmuir–Hinshelwood–Hougen–Watson (LHHW), and Horiuti–Polanyi kinetic mechanisms. The rate of loss of the first hydrogen molecule in the LHHW single-site surface reaction mechanism was found to be the rate-controlling step. Experiments with 1-methylcyclohexene confirmed that the rate-controlling step does not lie after the loss of the first hydrogen molecule. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie201539v