Highly active and stable Co/La0.7Sr0.3AlO3-δ catalyst for steam reforming of toluene

被引:26
作者
Takise, Kent [1 ]
Higo, Takuma [1 ]
Mukai, Daiki [1 ]
Ogo, Shuhei [1 ]
Sugiura, Yukihiro [1 ,2 ]
Sekine, Yasushi [1 ]
机构
[1] Waseda Univ, Dept Appl Chem, Shinjuku Ku, 3-4-1 Okubo, Tokyo 1698555, Japan
[2] JX Nippon Oil & Energy Corp, Cent Tech Res Lab, 8 Chidoricho, Yokohama, Kanagawa, Japan
关键词
Perovskite oxide; Steam reforming of toluene; Co catalyst; Hydrogen production; Surficial adsorption property; Stable catalytic activity; HYDROTALCITE-LIKE PRECURSORS; NI-BASED CATALYSTS; BIOMASS TAR; HYDROGEN-PRODUCTION; MODEL-COMPOUND; NICKEL-CATALYSTS; FE; CO; RH; ETHANOL;
D O I
10.1016/j.cattod.2015.08.059
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
We investigated steam reforming of toluene as a model compound of aromatic hydrocarbons included in biomass tar over Co supported Co/La0.7Sr0.3AlO3-delta (LSAO), perovskite oxide. Ni-supported LSAO catalyst has shown high activity and coke resistance from the redox property of lattice oxygen in/on the LSAO support. Co is known as an active metal for this reaction, so Co/LSAO catalyst was investigated in this work. Co/LSAO catalyst, which showed high steady-state activity and stability, was characterized using (H2O)-O-18 isotopic transient response tests, STEM, FT-IR, Arrhenius plot and partial pressure dependence to elucidate high and stable catalytic activity. In situ FT-IR measurements revealed that reaction intermediates on Co/LSAO desorbed at 873 K or lower temperatures. Although redox property of lattice oxygen did not change at around 848 K based on isotopic transient tests, the Arrhenius plots indicate that the rate-determining step changed at around 848 K because of reaction intermediate decomposition desorption. Fast reaction and desorption of absorbed intermediates on Co/LSAO enable catalytic stability during toluene steam reforming. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:111 / 117
页数:7
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