Lithium and lanthanum promoted Ni-Al2O3 as an active and highly coking resistant catalyst layer for solid-oxide fuel cells operating on methane

被引:48
作者
Wang, Wei [1 ]
Ran, Ran [1 ]
Shao, Zongping [1 ]
机构
[1] Nanjing Univ Technol, State Key Lab Mat Oriented Chem Engn, Coll Chem & Chem Engn, Nanjing 210009, Peoples R China
关键词
Solid-oxide fuel cells; Anode; Catalyst layer; Methane; Carbon deposition; ALKALI-METAL OXIDE; PARTIAL OXIDATION; CARBON-DIOXIDE; NI/AL2O3; CATALYSTS; THERMAL-STABILITY; NATURAL-GAS; ANODE; SOFC; PERFORMANCE; SYNGAS;
D O I
10.1016/j.jpowsour.2010.07.033
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
Ni-Al2O3 catalyst is modified with Li2O3, La2O3 and CaO promoters to improve its resistance to coking. These catalysts are used as the materials of the anode catalyst layer in solid-oxide fuel cells operating on methane. Their catalytic activity for the partial oxidation, steam reforming and CO2 reforming of methane at 600-850 degrees C is investigated. Their catalytic stability and carbon deposition properties are also studied. The LiLaNi-Al2O3 catalyst shows a catalytic activity that is comparable to those of LaNi-Al2O3 and LiNi-Al2O3 catalysts for all three reactions. However, it displays a higher catalytic activity than those of CaLaNi-Al2O3 and CaNi-Al2O3 catalysts. Among the various catalysts, the LiLaNi-Al2O3 catalyst presents the highest catalytic stability. O-2-TPO profiles indicate that the modification of the Ni-Al2O3 catalyst with Li and La greatly reduces carbon deposition under pure methane atmosphere. The LiLaNi-Al2O3 catalyst is applied as the anode functional layer of a Ni + ScSZ anode-supported fuel cell. The cell is operated on methane-O-2, methane-H2O or methane-CO2 gas mixtures and yields peak power densities of 538,532 and 529 mW cm(-2) at 850 degrees C, respectively, comparable to that of hydrogen fuel. In sum, the LiLaNi-Al2O3 is highly promising as a highly coking resistant catalyst layer for solid-oxide fuel cells. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:90 / 97
页数:8
相关论文
共 61 条
[1]   Development of coking-resistant Ni-based catalyst for partial oxidation and CO2-reforming of methane to syngas [J].
Chen, P ;
Zhang, HB ;
Lin, GD ;
Tsai, KR .
APPLIED CATALYSIS A-GENERAL, 1998, 166 (02) :343-350
[2]   High temperature thermal stabilization of alumina modified by lanthanum species [J].
Chen, XY ;
Liu, Y ;
Niu, GX ;
Yang, ZX ;
Bian, MY ;
He, A .
APPLIED CATALYSIS A-GENERAL, 2001, 205 (1-2) :159-172
[3]   Nickel catalyst prepared via glycine nitrate process for partial oxidation of methane to syngas [J].
Chen, Yazhong ;
Zhou, Wei ;
Shao, Zongping ;
Xu, Nanping .
CATALYSIS COMMUNICATIONS, 2008, 9 (06) :1418-1425
[4]   Effects of promoters and preparation procedures on reforming of methane with carbon dioxide over Ni/Al2O3 catalyst [J].
Cheng, ZX ;
Wu, QL ;
Li, JL ;
Zhu, QM .
CATALYSIS TODAY, 1996, 30 (1-3) :147-155
[5]   Characterization of gamma-alumina doped with Li and K by infrared studies of CO adsorption and Al-27-NMR [J].
de Miguel, Sergio R. ;
Scelza, Osvaldo A. ;
Castro, Alberto A. ;
Soria, Javier .
TOPICS IN CATALYSIS, 1994, 1 (1-2) :87-94
[6]   Influence of calcium content in Ni/CaO/γ-Al2O3 catalysts for CO2-reforming of methane [J].
Dias, JAC ;
Assaf, JM .
CATALYSIS TODAY, 2003, 85 (01) :59-68
[7]   SOFC system and technology [J].
Dokiya, M .
SOLID STATE IONICS, 2002, 152 :383-392
[8]   Effect of Li2-doping on surface and catalytic properties of Co3O4-MoO3/Al2O3 system [J].
El-Shobaky, GA ;
Ghozza, AM ;
Mohamed, GM .
APPLIED CATALYSIS A-GENERAL, 2003, 241 (1-2) :235-245
[9]  
GAUDILLERE C, CATAL TODAY IN PRESS
[10]   Catalytic and electrocatalytic behavior of Ni-based cermet anodes under internal dry reforming of CH4+CO2 mixtures in SOFCs [J].
Goula, G. ;
Kiousis, V. ;
Nalbandian, L. ;
Yentekakis, I. V. .
SOLID STATE IONICS, 2006, 177 (19-25) :2119-2123