Mo-promoted Ni/Al2O3 catalyst for dry reforming of methane

被引:68
|
作者
Yao, Lu [1 ,2 ]
Galvez, Maria Elena [2 ]
Hu, Changwei [1 ]
Da costa, Patrick [2 ]
机构
[1] Sichuan Univ, Coll Chem, Key Lab Green Chem & Technol, Minist Educ, Chengdu 610064, Sichuan, Peoples R China
[2] Univ Paris 06, UPMC, Inst Jean Le Rond Alembert, Sorbonne Univ, 2 Pl Gare Ceinture, F-78210 St Cyr Lecole, France
关键词
Methane; Carbon dioxide; Hydrogen production; Nickel catalysts; Molybdenum; CARBON-DIOXIDE; BIMETALLIC CATALYSTS; NIMO CATALYSTS; CO2; PERFORMANCE; SYNGAS; CH4; REDUCTION; TEMPERATURE; MOLYBDENUM;
D O I
10.1016/j.ijhydene.2017.03.208
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
Mo-promoted alumina supported Ni catalysts were prepared through a conventional impregnation method and tested in dry reforming of methane (DRM) at temperatures from 550 to 850 degrees C. The catalysts were characterized by means of H-2-temperature programmed reduction (H-2-TPR), CO2-temperature programmed desorption (CO2-TPD), X-ray diffraction (XRD), N-2 physisorption and Raman spectroscopy. Mo-promotion caused a reduction in the DRM catalytic activity. The weaker interaction between NiO species and the alumina support, the formation of a MoNi4 phase, and the lower basicity of this Ni-Mo/Al2O3 catalyst were identified as the main causes for its lower activity. However, pre-reducing the Ni-Mo/Al2O3 catalyst at temperatures lower than 700 degrees C, instead of 900 degrees C, resulted in a considerable increase of its catalytic activity. This was mainly due to the formation of a separate Ni-0 phase that did not interact with Mo and to an increase in medium strength basicity. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:23500 / 23507
页数:8
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