Comparison of reducibility and stability of alumina-supported Ni catalysts prepared by impregnation and co-precipitation

被引:341
作者
Li, GH [1 ]
Hu, LJ [1 ]
Hill, JM [1 ]
机构
[1] Univ Calgary, Dept Chem & Petr Engn, Calgary, AB T2N 1N4, Canada
关键词
nickel catalysts; alumina; reducibility; co-precipitation; impregnation; catalyst preparation; stability; sol-gel synthesis;
D O I
10.1016/j.apcata.2005.11.013
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
Three Ni-Al2O3 catalysts, with nickel loadings of 10-13 wt.%, were prepared by co-precipitation (Ni-Al co-precip), impregnation on an in-house sol-gel derived alumina (Ni/sol-gel Al2O3), and impregnation on a commercial gamma-Al-2-O-3 (Ni/-gamma-Al2O3). The catalysts were characterized by N-2 physisorption, H-2 chemisorption, TPR, XRD, SEM and TEM. The Ni species, Ni particle size, and Ni reducibility depended on the preparation method. The Ni-Al co-precip and Ni/sol-gel Al2O3 catalysts contained NiAl2O4 species after calcination, while the Ni/-gamma-Al2O3 catalyst contained NiO and NiAl2O4 species after calcination. Although the Ni/gamma-Al2O3 catalyst was the easiest to reduce, according to TPR, this catalyst had the lowest hydrogen uptake over a 100 h temperature-staged reduction experiment. The Ni-Al co-precip and Ni/sol-gel Al2O3 catalysts had Ni dispersions of over 7% with reduction at 550 degrees C for 31 h, and maximum dispersions of similar to 10%, after reduction at 650 degrees C for 7 h. After reduction at 550 degrees C, the Ni particles were not evident by TEM examination. The results suggest that the formation of a surface NiAl2O4 spinet phase during preparation is beneficial for a high Ni dispersion in the reduced catalyst. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:16 / 24
页数:9
相关论文
共 62 条
[1]  
Areán CO, 2001, COLLOID SURFACE A, V180, P253
[2]   On-board fuel conversion for hydrogen fuel cells:: comparison of different fuels by computer simulations [J].
Avci, AK ;
Önsan, ZI ;
Trimm, DL .
APPLIED CATALYSIS A-GENERAL, 2001, 216 (1-2) :243-256
[3]   Crystallization of sol-gel boehmite via hydrothermal annealing [J].
Bokhimi, X ;
Sánchez-Valente, J ;
Pedraza, F .
JOURNAL OF SOLID STATE CHEMISTRY, 2002, 166 (01) :182-190
[4]   Structures of surface- and bulk-dispersion phases of NiO/Al2O3 [J].
Cai, XH ;
Ren, ZG ;
Hu, TD ;
Xie, YC .
SURFACE AND INTERFACE ANALYSIS, 2001, 32 (01) :293-295
[5]   Preparation and characterization of several high-area NiAl2O4 spinels.: Study of their reducibility [J].
Cesteros, Y ;
Salagre, P ;
Medina, F ;
Sueiras, JE .
CHEMISTRY OF MATERIALS, 2000, 12 (02) :331-335
[6]   Role of support in CO2 reforming of CH4 over a Ni/γ-Al2O3 catalyst [J].
Cheng, ZX ;
Zhao, XG ;
Li, JL ;
Zhu, QM .
APPLIED CATALYSIS A-GENERAL, 2001, 205 (1-2) :31-36
[7]   Production of COx-free hydrogen for fuel cells via step-wise hydrocarbon reforming and catalytic dehydrogenation of ammonia [J].
Choudhary, TV ;
Sivadinarayana, C ;
Goodman, DW .
CHEMICAL ENGINEERING JOURNAL, 2003, 93 (01) :69-80
[8]   Grafted NiO on natural olivine for dry reforming of methane [J].
Courson, C. ;
Udron, L. ;
Petit, C. ;
Kiennemann, A. .
SCIENCE AND TECHNOLOGY OF ADVANCED MATERIALS, 2002, 3 (03) :271-282
[9]   STUDY OF NI-MO-GAMMA-AL2O3 CATALYSTS BY X-RAY PHOTOELECTRON AND RAMAN-SPECTROSCOPY - COMPARISON WITH CO-MO-GAMMA-AL2O3 CATALYSTS [J].
DUFRESNE, P ;
PAYEN, E ;
GRIMBLOT, J ;
BONNELLE, JP .
JOURNAL OF PHYSICAL CHEMISTRY, 1981, 85 (16) :2344-2351
[10]   THE CHEMISTRY OF METHANE REFORMING WITH CARBON-DIOXIDE AND ITS CURRENT AND POTENTIAL APPLICATIONS [J].
EDWARDS, JH ;
MAITRA, AM .
FUEL PROCESSING TECHNOLOGY, 1995, 42 (2-3) :269-289