Carbon nanotube-supported Ni-CeO2 catalysts. Effect of the support on the catalytic performance in the low-temperature WGS reaction

被引:41
|
作者
Dongil, A. B. [1 ]
Pastor-Perez, L. [2 ]
Escalona, N. [3 ,4 ]
Sepulveda-Escribano, A. [2 ]
机构
[1] Univ Concepcion, Dept Fis Quim, Lab Catalisis Met, Edmundo Larenas 129, Concepcion, Chile
[2] Univ Alicante, Lab Mat Avanzados, Dept Quim Inorgan, Inst Univ Mat Alicante, Apartado 99, E-03080 Alicante, Spain
[3] Pontificia Univ Catolica Chile, Escuela Ingn, Dept Ingn Quim & Bioproc, Avenida Vicuna Mackenna 4860, Santiago, Chile
[4] Pontificia Univ Catolica Chile, Fac Ciencias Quim, Santiago, Chile
关键词
WATER-GAS SHIFT; BIMETALLIC CATALYSTS; NI/AL2O3; CATALYSTS; NI; CO; CU; HYDROGENATION; DEACTIVATION; MECHANISM; PROMOTION;
D O I
10.1016/j.carbon.2016.01.103
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 low temperature water-gas shift (WGS) reaction has been studied over two commercial multiwall carbon nanotubes-supported nickel catalysts promoted by ceria. For comparison purposes, activated carbon-supported catalysts have also been studied. The catalytic performance and the characterization by N-2 adsorption analysis, powder X-ray diffraction (XRD), temperature-programmed reduction with H-2 (TPR-H-2), X-ray photoelectron spectroscopy (XPS) and transmission electron microscopy (TEM) analysis showed that the surface chemistry has an important effect on the dispersion of ceria. As a result, ceria was successfully dispersed over the carbon nanotubes (CNTs) with less graphitic character, and the catalyst afforded better activity in WGS than the catalyst prepared over massive ceria. Moreover, a 20 wt.% CeO2 loading over this support was more active than the analogous catalyst with a 40 wt.% loading. The ceria nanoparticles were smaller when the support was previously oxidized, however this resulted in a decrease of the activity. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:296 / 304
页数:9
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