Influence of the O2/CO ratio and the presence of H2O and CO2 in the feed-stream during the preferential oxidation of CO (PROX) over a CuOx/CeO2-coated microchannel reactor

被引:29
|
作者
Laguna, O. H. [1 ,2 ]
Dominguez, M. I. [1 ,2 ]
Oraa, S. [1 ,2 ]
Navajas, A. [3 ]
Arzamendi, G. [3 ]
Gandia, L. M. [3 ]
Centeno, M. A. [1 ,2 ]
Montes, M. [4 ]
Odriozola, J. A. [1 ,2 ]
机构
[1] Univ Seville, CSIC, Ctr Mixto, Dept Quim Inorgan, Seville 41092, Spain
[2] Univ Seville, CSIC, Ctr Mixto, Inst Ciencia Mat Sevilla, Seville 41092, Spain
[3] Univ Publ Navarra, Dept Quim Aplicada, E-31006 Pamplona, Spain
[4] Univ Basque Country, Fac Ciencias Quim San Sebastian, Dept Quim Aplicada, E-20018 San Sebastian, Spain
关键词
Microchannel reactor; Hydrogen purification; PROX; CO oxidation; Cu-modified ceria; WATER-GAS-SHIFT; CARBON-MONOXIDE; RICH H-2; HYDROGEN; CATALYSTS; CUO/CEO2; TRANSITION; TRANSPORT; ZR;
D O I
10.1016/j.cattod.2012.04.021
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The catalytic performance of a CuOx/CeO2 powder catalyst and that of a microchannel reactor or microreactor (MR) coated with the same solid was determined and compared. The catalytic activity measurements were carried out with varying O-2/CO molar ratios in the feed-stream. In addition, the influence of the presence of CO2 and H2O in the reaction mixture was studied. Some discrepancies were observed between the performances of the powder catalyst and the MR depending on the O-2/CO ratio. The MR presented a very good performance with a superior selectivity for CO conversion. This behaviour was due to a more efficient heat removal in the case of the MR that inhibited the H-2 oxidation reaction and the r-WGS. The isothermicity of the microreactor during the process was demonstrated through the monitoring of the MR inlet and outlet temperatures. Concerning the presence of CO2 or H2O in the feed-stream, both compounds gave rise to a decrease of the CO conversion. The negative effect on the catalytic performance was more marked when both compounds were fed together, although the principal inhibitor effect was associated to the CO2. This seems to be related with the formation of stable carbonates at the catalyst surface. (C) 2012 Elsevier B. V. All rights reserved.
引用
收藏
页码:182 / 187
页数:6
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