Structure and activity of Ni/La0.7Sr0.3AlO3-δ catalyst for hydrogen production by steam reforming of toluene

被引:30
|
作者
Mukai, Daiki [1 ]
Tochiya, Satoshi [1 ]
Murai, Yuki [1 ]
Imori, Masaya [1 ]
Sugiura, Yukihiro [1 ,2 ]
Sekine, Yasushi [1 ]
机构
[1] Waseda Univ, Dept Appl Chem, Shinjuku Ku, Tokyo 1698555, Japan
[2] JX Nippon Oil & Energy Corp, Cent Tech Res Lab, Naka Ward, Yokohama, Kanagawa, Japan
关键词
Steam reforming of toluene; Ni catalyst; Perovskite-type oxide support; Lattice oxygen mobility; GAS SHIFT REACTION; SUPPORTED-RH; MODEL-COMPOUND; H-2; PRODUCTION; NAPHTHALENE; TAR; METHANE; PHENOL; COBALT; CONVERSION;
D O I
10.1016/j.apcata.2013.05.023
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
We investigated catalytic steam reforming of aromatic hydrocarbon using toluene as a model compound. Ni/La0.7Sr0.3AlO3-delta catalyst showed high catalytic activity and low coke formation. Although the lattice oxygen in a perovskite-type support plays an important role for oxidizing CHx and coke precursor, the role of interaction between Ni and the support has not been clarified. In this study, Ni/La0.7Sr0.3AlO3-delta catalyst calcined at various temperatures (1073, 1173, 1273 and 1373 K) was prepared and used to elucidate the effect of Ni particle size on the lattice oxygen mobility. The Ni particle size increased concomitantly with increased calcination temperature, and the C-1 yield decreased from 72.9 to 15.5%. Enhancement of lattice oxygen mobility by the decrease of Ni particle size was observed by transient response tests using (H2O)-O-18 over Ni/La0.7Sr0.3AlO3-delta calcined at various temperatures. The interface between Ni and perovskite support played an important role for oxidizing coke precursor by lattice oxygen. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:78 / 86
页数:9
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