MnOx/Pt/Al2O3 catalysts for CO oxidation in H2-rich streams

被引:82
作者
Ayastuy, J. L. [1 ]
Gonzalez-Marcos, M. P. [1 ]
Gonzalez-Velasco, J. R. [1 ]
Gutierrez-Ortiz, M. A. [1 ]
机构
[1] Univ Basque Country, Fac Sci, Dept Chem Engn, Grp Chem Technol Environm Sustainabil, E-48080 Bilbao, Spain
关键词
CO oxidation; selective CO oxidation; Pt catalyst; selectivity; MnOx;
D O I
10.1016/j.apcatb.2006.01.028
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 catalytic activity of Pt on alumina catalysts, with and without MnOx incorporated to the catalyst formulation, for CO oxidation in H-2-free as well as in H-2-rich stream (PROX) has been studied in the temperature range of 25-250 degrees C. The effect of catalyst preparation (by successive impregnation or by co-impregnation of Mn and Pt) and Mn content in the catalyst performance has been studied. A low Mn content (2 wt.%) has been found not to improve the catalyst activity compared to the base catalyst. However, catalysts prepared by successive impregnation with 8 and 15 wt.% Mn have shown a lower operation temperature for maximum CO conversion than the base catalyst with an enhanced catalyst activity at low temperatures with respect to Pt/Al2O3. A maximum CO conversion of 89.8%, with selectivity of 44.9% and CO yield of 40.3% could be reached over a catalyst with 15 wt.% Mn operating at 139 degrees C and lambda = 2. The effect of the presence of 5 vol.% CO2 and 5 vol.% H2O in the feedstream on catalysts performance has also been studied and discussed. The presence Of CO2 in the feedstream enhances the catalytic performance of all the studied catalysts at high temperature, whereas the presence of steam inhibits catalysts with higher MnOx content. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:532 / 541
页数:10
相关论文
共 50 条
  • [21] Neural network aided design of Pt-Co-Ce/Al2O3 catalyst for selective CO oxidation in hydrogen-rich streams
    Gunay, M. Erdem
    Yildirim, Ramazan
    [J]. CHEMICAL ENGINEERING JOURNAL, 2008, 140 (1-3) : 324 - 331
  • [22] CO oxidation from syngas (CO and H2) using nanoporous Pt/Al2O3 catalyst
    Bae, Jong-Soo
    Park, Joo-Won
    Kim, Jae-Ho
    Lee, Jae-Goo
    Kim, Younghun
    Han, Choon
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2010, 27 (05) : 1458 - 1461
  • [23] Effect of phase composition between nano γ- and χ-Al2O3 on Pt/Al2O3 catalyst in CO oxidation
    Vleephoka, Chatchai
    Chaisuk, Choowong
    Samparnpiboon, Panida
    Praserthdam, Piyasan
    [J]. CATALYSIS COMMUNICATIONS, 2008, 9 (04) : 546 - 550
  • [24] CO oxidation from syngas (CO and H2) using nanoporous Pt/Al2O3 catalyst
    Jong-Soo Bae
    Joo-Won Park
    Jae-Ho Kim
    Jae-Goo Lee
    Younghun Kim
    Choon Han
    [J]. Korean Journal of Chemical Engineering, 2010, 27 : 1458 - 1461
  • [25] Improved Low-Temperature Activity of CuO-CeO2-ZrO2 Catalysts for Preferential Oxidation of CO in H2-Rich Streams
    Shi, Limin
    Zhang, Guo
    [J]. CATALYSIS LETTERS, 2016, 146 (08) : 1449 - 1456
  • [26] Selective CO oxidation in a hydrogen-rich stream over Au/γ-Al2O3 catalysts
    Bethke, GK
    Kung, HH
    [J]. APPLIED CATALYSIS A-GENERAL, 2000, 194 : 43 - 53
  • [27] Oscillatory CO Oxidation Over Pt/Al2O3 Catalysts Studied by In situ XAS and DRIFTS
    Alexey Boubnov
    Andreas Gänzler
    Sabrina Conrad
    Maria Casapu
    Jan-Dierk Grunwaldt
    [J]. Topics in Catalysis, 2013, 56 : 333 - 338
  • [28] Oscillatory CO Oxidation Over Pt/Al2O3 Catalysts Studied by In situ XAS and DRIFTS
    Boubnov, Alexey
    Gaenzler, Andreas
    Conrad, Sabrina
    Casapu, Maria
    Grunwaldt, Jan-Dierk
    [J]. TOPICS IN CATALYSIS, 2013, 56 (1-8) : 333 - 338
  • [29] Influence of ammonia on CO and methanol oxidation over Pt/γ-Al2O3 catalysts modified by Mg
    Arnby, K
    Törncrona, A
    Skoglundh, M
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 49 (01) : 51 - 59
  • [30] A transient in situ FTIR and XANES study of CO oxidation over Pt/Al2O3 catalysts
    Carlsson, PA
    Österlund, L
    Thormählen, P
    Palmqvist, A
    Fridell, E
    Jansson, J
    Skoglundh, M
    [J]. JOURNAL OF CATALYSIS, 2004, 226 (02) : 422 - 434