Hydrogen production from ethanol over Ir/CeO2 catalysts : A comparative study of steam reforming, partial oxidation and oxidative steam reforming

Steam reforming, partial oxidation, and oxidative steam reforming of ethanol over Ir/CeO2 catalysts were studied to elucidate the reaction pathway and determine catalytic stability. Temperature-programmed desorption and surface reaction revealed that ethoxy species were immediately formed on ethanol...

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Veröffentlicht in:Journal of catalysis 2008-07, Vol.257 (1), p.96-107
Hauptverfasser: WEIJIE CAI, FAGEN WANG, ENSHENG ZHAN, VAN VEEN, A. C, MIRODATOS, Claude, WENJIE SHEN
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container_end_page 107
container_issue 1
container_start_page 96
container_title Journal of catalysis
container_volume 257
creator WEIJIE CAI
FAGEN WANG
ENSHENG ZHAN
VAN VEEN, A. C
MIRODATOS, Claude
WENJIE SHEN
description Steam reforming, partial oxidation, and oxidative steam reforming of ethanol over Ir/CeO2 catalysts were studied to elucidate the reaction pathway and determine catalytic stability. Temperature-programmed desorption and surface reaction revealed that ethoxy species were immediately formed on ethanol adsorption at room temperature, and were mainly further oxidized to acetate and carbonate species that finally decomposed into CH4/CO and CO2, respectively. Under reaction conditions, acetaldehyde was the primary product below 673 K, which decomposed mainly to methane and carbon monoxide at higher temperatures, whereas methane reforming and the water-gas shift were the major reactions above 773 K. The Ir/CeO2 catalyst demonstrated rather high stability for the reactions at 823 and 923 K with no apparent deactivation for 60 h on stream; the mean size of Ir particles was stable at around 2-3 nm, but the ceria particles sintered significantly from 6-8 to 14-27 nm. CeO2 likely prevented the highly dispersed Ir particles from sintering and inhibited coke deposition through strong Ir-CeO2 interactions. [PUBLICATION ABSTRACT]
doi_str_mv 10.1016/j.jcat.2008.04.009
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Under reaction conditions, acetaldehyde was the primary product below 673 K, which decomposed mainly to methane and carbon monoxide at higher temperatures, whereas methane reforming and the water-gas shift were the major reactions above 773 K. The Ir/CeO2 catalyst demonstrated rather high stability for the reactions at 823 and 923 K with no apparent deactivation for 60 h on stream; the mean size of Ir particles was stable at around 2-3 nm, but the ceria particles sintered significantly from 6-8 to 14-27 nm. CeO2 likely prevented the highly dispersed Ir particles from sintering and inhibited coke deposition through strong Ir-CeO2 interactions. 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Under reaction conditions, acetaldehyde was the primary product below 673 K, which decomposed mainly to methane and carbon monoxide at higher temperatures, whereas methane reforming and the water-gas shift were the major reactions above 773 K. The Ir/CeO2 catalyst demonstrated rather high stability for the reactions at 823 and 923 K with no apparent deactivation for 60 h on stream; the mean size of Ir particles was stable at around 2-3 nm, but the ceria particles sintered significantly from 6-8 to 14-27 nm. CeO2 likely prevented the highly dispersed Ir particles from sintering and inhibited coke deposition through strong Ir-CeO2 interactions. [PUBLICATION ABSTRACT]</abstract><cop>Amsterdam</cop><pub>Elsevier</pub><doi>10.1016/j.jcat.2008.04.009</doi><tpages>12</tpages></addata></record>
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subjects Catalysis
Catalysts
Chemical Sciences
Chemistry
Comparative studies
Ethanol
Exact sciences and technology
General and physical chemistry
Hydrogen
Oxidation
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title Hydrogen production from ethanol over Ir/CeO2 catalysts : A comparative study of steam reforming, partial oxidation and oxidative steam reforming
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