Transient kinetic model of CO oxidation over a nanostructured Cu0.1Ce0.9O2-y catalyst

被引:112
作者
Sedmak, G
Hocevar, S
Levec, J
机构
[1] Natl Inst Chem, Lab Catalysis & React Engn, SI-1000 Ljubljana, Slovenia
[2] Univ Ljubljana, Dept Chem & Chem Technol, SI-1000 Ljubljana, Slovenia
关键词
transient kinetics; kinetic model; Cu0.1Ce0.9O2-y catalyst; CO oxidation; redox process; lattice oxygen diffusion; PROX; fuel cell;
D O I
10.1016/j.jcat.2003.10.006
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 oxidation of carbon monoxide under dynamic conditions was studied over a novel nanostructured Cu0.1Ce0.9O2-y catalyst. CO temperature-programmed reduction provides a qualitative picture of the reducibility of that catalyst. Step-change experiments in CO concentration in the temperature range between 50 and 250 degreesC allowed us to estimate the oxygen storage capacity of the catalyst as a function of temperature. The measured CO and CO2 responses were used to construct a detailed transient kinetic model based on elementary reaction steps. In the modeling, elementary reaction steps such as the adsorption of CO on oxidized and reduced catalyst active sites, diffusion of subsurface lattice oxygen to the surface, reoxidation of reduced catalyst active sites by the subsurface lattice oxygen, and the surface reaction of CO to CO2 were considered. The calculated activation energies for various surface reaction steps were in the range from 9.7 to 39.6 kJ mol(-1), for the catalyst reoxidation step 72.9 kJ mol(-1), and for the lattice oxygen diffusion in the Cu0.1Ce0.9O2-y catalyst 40.0 kJ mol(-1). These values are discussed in detail. The bulk oxygen diffusion coefficient is equal to 3.2 x 10(-12) cm(2) s(-1) at 250 degreesC. This value is in the range of bulk diffusion coefficients measured over other oxide catalysts. (C) 2003 Elsevier Inc. All rights reserved.
引用
收藏
页码:87 / 99
页数:13
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