Prominent enhancement of Mn or Co addition on the performance of Cu - Ce - O catalyst used for H2 production via dimethyl ether steam reforming / Xiaoyan Zhou in Chemical engineering journal, Vol. 174 N° 1 (Octobre 2011)  

Public ISBD [article]  inChemical engineering journal > Vol. 174 N° 1 (Octobre 2011) . - pp. 400–407 Titre : Prominent enhancement of Mn or Co addition on the performance of Cu - Ce - O catalyst used for H2 production via dimethyl ether steam reforming Type de document : texte imprimé Auteurs : Xiaoyan Zhou, Auteur ; Ming Meng, Auteur ; Zhaosong Sun, Auteur Année de publication : 2012 Article en page(s) : pp. 400–407 Note générale : Génie chimique Langues : Anglais (eng) Mots-clés : Cu-Ce-O catalyst Promoter Cobalt Manganese H2 production Dimethyl ether steam reforming Résumé : The Mn or Co promoted Cu-Ce-O catalysts were prepared by citric acid complexation, and used for the catalytic production of hydrogen via the route of dimethyl ether steam reforming (DME SR). Multiple techniques such as X-ray diffraction (XRD), X-ray absorption fine structure (XAFS), X-ray photoelectron spectra (XPS), temperature-programmed reduction by H2 (H2-TPR), CO-pulse chemisorption and thermal gravimetry/differential thermal analysis (TG/DTA) were employed for catalyst characterization. It is revealed by the results of XRD, XPS and XAFS that in the spent catalysts the copper species mainly exist as Cu0 and Cu+. The addition of Co or Mn could enhance both the dispersion and the reducibility of copper species, significantly increasing the DME conversion and H2 yield at the temperature of 400 °C or below. At higher temperature, the H2 yield over Cu-Ce-Co-O is almost the same as that for Cu-Ce-O, due to the side reactions of CH3OH decomposition and/or DME steam reforming to syngas. Addition of Mn to Cu-Ce-O can increase both DME conversion and H2 yield in the whole temperature region of 300–450 °C. Much higher CO2 selectivity is achieved over the Mn promoted catalyst. XPS and CO-pulse chemisorption results indicate that Cu-Ce-Mn-O catalyst contains more Cu+ species, which determines its novel catalytic performance including higher DME conversion and higher H2 yield. ISSN : 1385-8947 En ligne : http://www.sciencedirect.com/science/article/pii/S138589471101076X [article] Prominent enhancement of Mn or Co addition on the performance of Cu - Ce - O catalyst used for H2 production via dimethyl ether steam reforming [texte imprimé] / Xiaoyan Zhou, Auteur ; Ming Meng, Auteur ; Zhaosong Sun, Auteur . - 2012 . - pp. 400–407. Génie chimique Langues : Anglais (eng) in Chemical engineering journal > Vol. 174 N° 1 (Octobre 2011) . - pp. 400–407 Mots-clés : Cu-Ce-O catalyst Promoter Cobalt Manganese H2 production Dimethyl ether steam reforming Résumé : The Mn or Co promoted Cu-Ce-O catalysts were prepared by citric acid complexation, and used for the catalytic production of hydrogen via the route of dimethyl ether steam reforming (DME SR). Multiple techniques such as X-ray diffraction (XRD), X-ray absorption fine structure (XAFS), X-ray photoelectron spectra (XPS), temperature-programmed reduction by H2 (H2-TPR), CO-pulse chemisorption and thermal gravimetry/differential thermal analysis (TG/DTA) were employed for catalyst characterization. It is revealed by the results of XRD, XPS and XAFS that in the spent catalysts the copper species mainly exist as Cu0 and Cu+. The addition of Co or Mn could enhance both the dispersion and the reducibility of copper species, significantly increasing the DME conversion and H2 yield at the temperature of 400 °C or below. At higher temperature, the H2 yield over Cu-Ce-Co-O is almost the same as that for Cu-Ce-O, due to the side reactions of CH3OH decomposition and/or DME steam reforming to syngas. Addition of Mn to Cu-Ce-O can increase both DME conversion and H2 yield in the whole temperature region of 300–450 °C. Much higher CO2 selectivity is achieved over the Mn promoted catalyst. XPS and CO-pulse chemisorption results indicate that Cu-Ce-Mn-O catalyst contains more Cu+ species, which determines its novel catalytic performance including higher DME conversion and higher H2 yield. ISSN : 1385-8947 En ligne : http://www.sciencedirect.com/science/article/pii/S138589471101076X

Exemplaires

Code-barres	Cote	Support	Localisation	Section	Disponibilité
aucun exemplaire