Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol

Ni-W cataIysts supportedon Ce02.~03andhydrota1cite (HT)were studiedin th.e steamreformingofethanol at 500-650DC. The Ce02 and HT were synthesized by impregnation and direct coprecipitation methods, respectively. Commercia1~03 was used. Nicke} content was varied from !O, 15 and 30% with 1 % W. The ca...

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Autores principales: Hernández, Paz, Fernández, Arturo, Messina, Sarah
Formato: Artículo
Lenguaje:inglés
Publicado: 2011
Materias:
Acceso en línea:http://eprints.uanl.mx/2468/1/Art6.pdf
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author Hernández, Paz
Fernández, Arturo
Messina, Sarah
author_facet Hernández, Paz
Fernández, Arturo
Messina, Sarah
author_sort Hernández, Paz
collection Repositorio Institucional
description Ni-W cataIysts supportedon Ce02.~03andhydrota1cite (HT)were studiedin th.e steamreformingofethanol at 500-650DC. The Ce02 and HT were synthesized by impregnation and direct coprecipitation methods, respectively. Commercia1~03 was used. Nicke} content was varied from !O, 15 and 30% with 1 % W. The catalyst that presentod the highest cataIytic activity and selectivity to bydrogen was 10% Ni-WIHT. Conversian to eth.anol was 100% and selectivities to H2 CH4 CO2 and ca were 75, 5.78, 0.37 and 18.85%, respectively, at a temperature of 500ºC. Moreover, these catalysts showed good stability with respect to carbon deposition and low selectivity towards ~~ production. These are desirablc features for cataIysts to be used in hydrogen production for fuel cell applications.
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spelling eprints-24682014-11-24T20:25:11Z http://eprints.uanl.mx/2468/ Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol Hernández, Paz Fernández, Arturo Messina, Sarah Q Ciencias en General QD Química Ni-W cataIysts supportedon Ce02.~03andhydrota1cite (HT)were studiedin th.e steamreformingofethanol at 500-650DC. The Ce02 and HT were synthesized by impregnation and direct coprecipitation methods, respectively. Commercia1~03 was used. Nicke} content was varied from !O, 15 and 30% with 1 % W. The catalyst that presentod the highest cataIytic activity and selectivity to bydrogen was 10% Ni-WIHT. Conversian to eth.anol was 100% and selectivities to H2 CH4 CO2 and ca were 75, 5.78, 0.37 and 18.85%, respectively, at a temperature of 500ºC. Moreover, these catalysts showed good stability with respect to carbon deposition and low selectivity towards ~~ production. These are desirablc features for cataIysts to be used in hydrogen production for fuel cell applications. 2011 Article PeerReviewed application/pdf en http://eprints.uanl.mx/2468/1/Art6.pdf http://eprints.uanl.mx/2468/1.haspreviewThumbnailVersion/Art6.pdf Hernández, Paz y Fernández, Arturo y Messina, Sarah (2011) Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol. Química Hoy, 2 (1).
spellingShingle Q Ciencias en General
QD Química
Hernández, Paz
Fernández, Arturo
Messina, Sarah
Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
thumbnail https://rediab.uanl.mx/themes/sandal5/images/online.png
title Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
title_full Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
title_fullStr Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
title_full_unstemmed Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
title_short Comparative Study of Ni-W/CeO25 Ni-W/y-Al2O3 and Ni-WIHT CataIysts for H2 Production by Steam Reforming of Bioethanol
title_sort comparative study of ni w ceo25 ni w y al2o3 and ni wiht cataiysts for h2 production by steam reforming of bioethanol
topic Q Ciencias en General
QD Química
url http://eprints.uanl.mx/2468/1/Art6.pdf
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