Valente, J.; Quintana-Solorzano, R.; Armendariz-Herrera, H.; Barragan-Rodriguez, G.; López Nieto, JM. (2014). Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst. Industrial and Engineering Chemistry Research. 53(5):1775-1786. doi:10.1021/ie402447h
Por favor, use este identificador para citar o enlazar este ítem: http://hdl.handle.net/10251/64212
Title:
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Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst
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Author:
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Valente, J.S.
Quintana-Solorzano, R.
Armendariz-Herrera, H.
Barragan-Rodriguez, G.
López Nieto, José Manuel
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UPV Unit:
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Universitat Politècnica de València. Instituto Universitario Mixto de Tecnología Química - Institut Universitari Mixt de Tecnologia Química
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Issued date:
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Abstract:
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[EN] A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained ...[+]
[EN] A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3(k) experimental design to investigate the simultaneous effect of temperature (400-480 degrees C) and space time [23-70 g(cat) h (mol of ethane) I]. A fixed-bed reactor at atmospheric pressure was employed, feeding a mixture of ethane, oxygen, and nitrogen. Ethane conversion varied from 17 to 85%, whereas selectivity for ethylene and COx varied from 94 to 76% and from 4.0 to 24%, respectively. These types of analyses are useful for determining the optimum reaction conditions to enhance the catalytic performance of the mixed oxides presented herein.
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Subjects:
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Mo-V-Te-Nb
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Oxides
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Ethane oxidative dehydrogenation
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Kinetic study
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Copyrigths:
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Reserva de todos los derechos
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Source:
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Industrial and Engineering Chemistry Research. (issn:
0888-5885
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DOI:
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10.1021/ie402447h
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Publisher:
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American Chemical Society
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Publisher version:
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http://dx.doi.org/10.1021/ie402447h
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Description:
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This document is the Accepted Manuscript version of a Published Work that appeared in final form in
Industrial & Engineering Chemistry Research, copyright © American Chemical Society after peer review and technical editing by the publisher.
To access the final edited and published work see [insert ACS Articles on Request author-directed link to
Published Work, see http://doi.org/10.1021/ie402447h
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Thanks:
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This work was financially supported by the Instituto Mexicano del Petroleo. Technical support from Eng. G. Alonso-Ramirez is gratefully acknowledged.
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Type:
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Artículo
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