2009
DOI: 10.1016/j.jcat.2009.06.021
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Study of active sites and mechanism responsible for highly selective CO oxidation in H2 rich atmospheres on a mixed Cu and Ce oxide catalyst

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Cited by 180 publications
(134 citation statements)
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“…Thus, differences between the CO oxidation activities under CO-PROX conditions for this type of catalyst is related to the extent of support promotion of such partial (to Cu + ) CuO reduction at interfacial sites which is attained in each case. It is worth noting that the correlation between the intensity of the Cu + -carbonyl and CO oxidation activity over samples of this type was also independently demonstrated later by Baertsch et al [63]. On the other hand, the reaction mechanism under which this type of catalyst operates for CO oxidation has been proposed to be of a redox, generally speaking, of the Mars-van Krevelen [64,65], type [6].…”
Section: Nature Of Active Sites/entities and Further Hints On Catalytmentioning
confidence: 68%
“…Thus, differences between the CO oxidation activities under CO-PROX conditions for this type of catalyst is related to the extent of support promotion of such partial (to Cu + ) CuO reduction at interfacial sites which is attained in each case. It is worth noting that the correlation between the intensity of the Cu + -carbonyl and CO oxidation activity over samples of this type was also independently demonstrated later by Baertsch et al [63]. On the other hand, the reaction mechanism under which this type of catalyst operates for CO oxidation has been proposed to be of a redox, generally speaking, of the Mars-van Krevelen [64,65], type [6].…”
Section: Nature Of Active Sites/entities and Further Hints On Catalytmentioning
confidence: 68%
“…The isotherm of the catalysts at different wt% CU loading reveals a typical type IV sorption behavior, representing the predominant mesoporous structure characteristic as shown in Figure 2. The volume of N 2 adsorbed on the catalyst surface decreases with increasing CuO up to 40 wt%, which indicates that coverage of CuO decreases the specific surface area of the sample [9].The S BET of CuO/CeO 2 -Co 3 O 4 catalysts were calculated by Brunauer EmmettTeller (BET) method using data from N 2 adsorptiondesorption isotherm with in between 0.05-0.35 and the results are reported in Table 1.…”
Section: Catalyst Characterizationmentioning
confidence: 99%
“…24 Polster et al relatam ainda que existem diferentes espécies de oxigênio da céria e do óxido de cobre que se reduzem a diferentes temperaturas no sólido CuO x -CeO 2 , mas estas são as mesmas espécies de oxigênio em cada óxido puro. 25 O perfil de RTP da titânia, mostrado na Figura 4, apresenta pequenas ondulações nas temperaturas de 500 e 600 ºC, não chegando a caracterizar um pico. Isto indica que, em toda a faixa experimental observada, a titânia não foi reduzida, resultados estes que coincidem com os relatados por Zhu et al 20 O perfil de RTP da céria/titânia, exibido na Figura 5, mostra um pico de redução a 858 ºC e três pequenos ombros a 368, 518 e 602 ºC.…”
Section: Redução a Temperatura Programadaunclassified