2010
DOI: 10.1016/j.apcata.2010.05.016
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Reforming of ethanol on Pt/Al2O3-ZrO2 catalyst

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Cited by 34 publications
(7 citation statements)
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“…This can be correlated with the high activity of these catalysts for the WGS reaction, which has been proposed to proceed via interaction of adsorbed CO with surface hydroxyl groups to form intermediate formate species, which is further decomposed toward CO 2 and H 2 [9,34,46]. Dö mö k et al [50] suggested that the WGS reaction over Pt/ZrO 2 catalyst is taking place via decomposition of acetate groups at the metal/support interface and interaction of the so formed products with the OH groups activated on the partially reduced zirconia sites. The detection of adsorbed CO and acetate species up to 450 C over Pt/Al 2 O 3 catalyst indicates that the formation rate of these species is higher than their decomposition or further reaction.…”
Section: In Situ Ftir Spectramentioning
confidence: 95%
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“…This can be correlated with the high activity of these catalysts for the WGS reaction, which has been proposed to proceed via interaction of adsorbed CO with surface hydroxyl groups to form intermediate formate species, which is further decomposed toward CO 2 and H 2 [9,34,46]. Dö mö k et al [50] suggested that the WGS reaction over Pt/ZrO 2 catalyst is taking place via decomposition of acetate groups at the metal/support interface and interaction of the so formed products with the OH groups activated on the partially reduced zirconia sites. The detection of adsorbed CO and acetate species up to 450 C over Pt/Al 2 O 3 catalyst indicates that the formation rate of these species is higher than their decomposition or further reaction.…”
Section: In Situ Ftir Spectramentioning
confidence: 95%
“…3C. It is observed that interaction of the catalyst with the reformate mixture at room temperature results in the appearance of bands due to different vibrational modes of ethoxy (1094, 1055, 1384, 2975, 2930 and 2879 cm À1 ) [28,50], acetate (1559, 1432, 1346 and 1315 cm À1 ) and acetyl species (1648 cm À1 ) [28,50], as well as by negative bands (3777, 3734 and 3683 cm À1 ) related to the consumption of surface OH groups during the interaction of ethanol with the catalyst surface. Increase of temperature to 100 C results in the development of a broad band in the n(CO) frequency region (2100e2000 cm À1 ), which is characterized by two maxima at ca 2059 and 2040 cm À1 attributable, as discussed above, to linearly adsorbed CO species.…”
Section: In Situ Ftir Spectramentioning
confidence: 97%
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“…Catalytic conversion of bio-ethanol received considerable attention in the last decade [32][33][34][35][36][37] and the search for the most active, stable and selective catalyst has resulted in many heterogeneous catalytic systems.…”
Section: Introductionmentioning
confidence: 99%
“…El soporte puede jugar un papel importante, ayudando en la eliminación de carbón o en la supresión de su formación. Para aumentar la velocidad de la reacción de gasificación de carbón, ya sea favoreciendo la adsorción de agua o neutralizando los sitios ácidos responsables de la polimerización de etileno, se han realizado estudios focalizados en la modificación de las propiedades ácido/base del soporte mediante la adición de dopantes como: metales alcalinos [136][137][138][139][140], metales alcalinotérreos [141][142][143] u óxidos de tierras raras [144][145][146]. Sin embargo, hay que señalar que la adición de dopantes puede afectar las propiedades electrónicas del centro catalítico, y bloquear o modificar los centros específicos de adsorción.…”
Section:  Reformado Autotérmicounclassified