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Détail de l'auteur
Auteur Dhaval Patel
Documents disponibles écrits par cet auteur
Affiner la rechercheKinetics and modeling of the flexible fuel reformer: n-hexadecane steam reforming and combustion / Preshit V. Gawade in Industrial & engineering chemistry research, Vol. 49 N° 15 (Août 2010)
[article]
in Industrial & engineering chemistry research > Vol. 49 N° 15 (Août 2010) . - pp 6931–6940
Titre : Kinetics and modeling of the flexible fuel reformer: n-hexadecane steam reforming and combustion Type de document : texte imprimé Auteurs : Preshit V. Gawade, Auteur ; Dhaval Patel, Auteur ; G. Glenn Lipscomb, Auteur Année de publication : 2010 Article en page(s) : pp 6931–6940 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Kinetics Flexible fuel. Résumé : Steam reforming of liquid hydrocarbon fuels provides one possible solution for the production of hydrogen for solid oxide fuel cells (SOFCs). However, the design of the reformer is dependent on the kinetics of the catalytic reaction, which is not widely reported. Because reforming is highly endothermic, we have investigated the use of a heat exchange device, designated the flexible fuel reformer (FFR), as a reactor in which combustion and reforming can be simultaneously accomplished. In the present study, we evaluated the reforming and combustion kinetics of n-hexadecane (used as an analog for diesel) over the rhodium/nickel catalyst supported on alumina. Reforming data obtained over the temperature range of 500−750 °C was compared against three different mechanistic models: Eley−Rideal, Langmuir−Hinshelwood bimolecular adsorption, and Langmuir−Hinshelwood dual site. Among all, Eley−Rideal produced good data fitting and fulfilled the thermodynamic criteria in every case. Combustion kinetics of hexadecane was also studied, since our proposed reactor configuration uses the heat from the exothermic combustion reaction as a driver for the endothermic reforming reaction. It was found that power-law model produced the best fit among all the models and this result was further corroborated using statistical analysis. The kinetic results can be combined with the reactor design model to predict the performance and demonstrate the benefit obtained from simultaneous reforming and combustion. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901819x [article] Kinetics and modeling of the flexible fuel reformer: n-hexadecane steam reforming and combustion [texte imprimé] / Preshit V. Gawade, Auteur ; Dhaval Patel, Auteur ; G. Glenn Lipscomb, Auteur . - 2010 . - pp 6931–6940.
Chimie industrielle
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 49 N° 15 (Août 2010) . - pp 6931–6940
Mots-clés : Kinetics Flexible fuel. Résumé : Steam reforming of liquid hydrocarbon fuels provides one possible solution for the production of hydrogen for solid oxide fuel cells (SOFCs). However, the design of the reformer is dependent on the kinetics of the catalytic reaction, which is not widely reported. Because reforming is highly endothermic, we have investigated the use of a heat exchange device, designated the flexible fuel reformer (FFR), as a reactor in which combustion and reforming can be simultaneously accomplished. In the present study, we evaluated the reforming and combustion kinetics of n-hexadecane (used as an analog for diesel) over the rhodium/nickel catalyst supported on alumina. Reforming data obtained over the temperature range of 500−750 °C was compared against three different mechanistic models: Eley−Rideal, Langmuir−Hinshelwood bimolecular adsorption, and Langmuir−Hinshelwood dual site. Among all, Eley−Rideal produced good data fitting and fulfilled the thermodynamic criteria in every case. Combustion kinetics of hexadecane was also studied, since our proposed reactor configuration uses the heat from the exothermic combustion reaction as a driver for the endothermic reforming reaction. It was found that power-law model produced the best fit among all the models and this result was further corroborated using statistical analysis. The kinetic results can be combined with the reactor design model to predict the performance and demonstrate the benefit obtained from simultaneous reforming and combustion. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901819x