Porous nickel based catalysts for partial oxidation of methane to synthesis gas

被引:27
|
作者
Kirillov, V. A. [1 ]
Fedorova, Z. A. [1 ]
Danilova, M. M. [1 ]
Zaikovskii, V. I. [1 ]
Kuzin, N. A. [1 ]
Kuzmin, V. A. [1 ]
Krieger, T. A. [1 ]
Mescheryakov, V. D. [1 ]
机构
[1] Boreskov Inst Catalysis SB RAS, Novosibirsk, Russia
关键词
Nickel catalysts; Partial oxidation of methane; Synthesis gas; CARBON-DIOXIDE; CO2; OXIDE; CONVERSION; MECHANISM; SYNGAS; STEAM; H-2; CH4;
D O I
10.1016/j.apcata.2011.05.018
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
The phase composition and texture of nickel catalysts supported on ribbon porous nickel with a magnesium oxide underlayer were investigated by X-ray diffraction, low-temperature nitrogen adsorption, and electron microscopy combined with energy dispersive X-ray microanalysis. The MgO underlayer was obtained by impregnation the porous nickel with a Mg(NO3)(2) solution followed by calcination at 550 degrees C; nickel was supported additionally by impregnation with a Ni(NO3)(2) solution followed by calcination at 450 degrees C. In the supported reduced nickel catalysts (800-900 degrees C, H-2) the phases of Ni and a solid solution of NiO in MgO were observed; a considerable part of nickel crystallites was epitaxially bound with MgO. The partial oxidation of methane to synthesis gas (800 degrees C, O-2/C = 0.65, GHSV = 127 L/g h) over porous nickel based catalysts was studied. The activity of initial nickel support decreased considerably during the partial oxidation of methane; the value of methane conversion decreased slightly after 100 h of testing on the supported nickel catalysts. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:170 / 175
页数:6
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