2009
DOI: 10.1016/j.ijhydene.2009.02.054
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Catalytic performance of a copper–promoted CeO2 catalyst in the CO oxidation: Influence of the operating variables and kinetic study

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Cited by 22 publications
(13 citation statements)
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“…Fig. 5 demonstrates that for every stoichiometric air excess a maximum in CO conversion is registered for an intermediate temperature, in accordance with the literature [32]. This maximum in CO conversion is explained by an increase in overall activity, i.e., both CO and H 2 oxidations, with a diminution of selectivity since H 2 oxidation has higher apparent activation energy [28].…”
Section: Coproxsupporting
confidence: 85%
“…Fig. 5 demonstrates that for every stoichiometric air excess a maximum in CO conversion is registered for an intermediate temperature, in accordance with the literature [32]. This maximum in CO conversion is explained by an increase in overall activity, i.e., both CO and H 2 oxidations, with a diminution of selectivity since H 2 oxidation has higher apparent activation energy [28].…”
Section: Coproxsupporting
confidence: 85%
“…On the other hand, above 160 ºC it is observed for all catalysts that both CO conversion and O 2 selectivity decrease on increasing temperature. Undesired side reactions, H 2 oxidation [67] or the reverse water gas shift [40], are favored on increasing the temperature.…”
Section: Gold Catalystsmentioning
confidence: 99%
“…3 Por outro lado, alguns catalisadores de metais não nobres suportados em óxidos têm se mostrado eficientes aos requisitos da PROX-CO, exibindo também boa atividade e seletividade. 3 O estudo de catalisadores de cobre suportados em óxidos para a PROX-CO tem trazido resultados interessantes e importantes mostrando, muitas vezes, maior eficiência que os catalisadores de metais nobres. Os que apresentam melhores resultados são os suportados em céria.…”
Section: 2unclassified
“…Uma vez que as células PEMFC utilizam como fonte de energia o hidrogênio com elevada pureza, a reação de PROX-CO apresenta-se como um meio de purificar o hidrogênio produzido pelas reações de reforma do metano. [1][2][3][4][5][6][7][8][9][10] O método convencional de produção de hidrogênio combina as reações de reforma a vapor do metano com a reação de deslocamento gás-água (WGS -water gas shift reaction), e os gases gerados apresentam a seguinte composição aproximada: 45% H 2 , 25% CO 2 , 10% H 2 O, 20% N 2 e 0,5-1% CO.…”
Section: Introductionunclassified
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