Catalytic performance of manganese doped CuO-CeO2 catalysts for selective oxidation of CO in hydrogen-rich gas

被引:114
作者
Guo, Xiaolin [1 ]
Li, Jing [1 ]
Zhou, Renxian [1 ]
机构
[1] Zhejiang Univ, Inst Catalysis, Hangzhou 310028, Zhejiang, Peoples R China
关键词
Hydrogen purification; CO selective oxidation; CuO-MnOx-CeO2; catalysts; Mn doping; Calcination temperature; MIXED-OXIDE CATALYSTS; IN-SITU DRIFTS; PREFERENTIAL OXIDATION; EXCESS HYDROGEN; CALCINATION TEMPERATURE; CARBON-MONOXIDE; METAL; CUO/CEO2; MN; CU;
D O I
10.1016/j.fuel.2015.09.043
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Manganese doped CuO-CeO2 catalysts (CuO-MnOx-CeO2) with Mn/Cu molar ratio of 1: 5 and variable calcination temperatures were prepared by a hydrothermal method and used for selective oxidation of CO in hydrogen-rich gas, characterized by various techniques. An appropriate calcination temperature shows an essential stimulative effect on CuO-MnOx-CeO2 catalysts for the CO-PROX. The catalyst calcined at 500 degrees C displays the highest low-temperature catalytic activity (T-50% = 74 degrees C) and the broadest operating temperature "window" (CO conversion > 99.0%, 110-140 degrees C). XRD and UV-Raman results reveal that an appropriate calcination temperature can promote the formation of Cu-Mn-Ce-O ternary oxide solid solution, adjust the degree of crystallinity of CeO2 and enhance the formation of oxygen vacancies. H-2-TPR and XPS demonstrate that calcining at 500 degrees C improves the active reducing species in both bulk and surface of the catalyst. In situ DRIFTS suggests that Cu+ species which possess strong interaction with ceria also can be facilitated with a suitable calcination temperature. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:56 / 64
页数:9
相关论文
共 37 条
  • [1] Influence of the preparation method on the performance of CuO-CeO2 catalysts for the selective oxidation of CO
    Avgouropoulos, G
    Ioannides, T
    Matralis, H
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 56 (1-2) : 87 - 93
  • [2] CuO-CeO2 mixed oxide catalysts for the selective oxidation of carbon monoxide in excess hydrogen
    Avgouropoulos, G
    Ioannides, T
    Matralis, HK
    Batista, J
    Hocevar, S
    [J]. CATALYSIS LETTERS, 2001, 73 (01) : 33 - 40
  • [3] Effect of synthesis parameters on catalytic properties of CuO-CeO2
    Avgouropoulos, George
    Ioannides, Theophilos
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 67 (1-2) : 1 - 11
  • [4] Comparative in Situ DRIFTS-MS Study of 12CO- and 13CO-TPR on CuO/CeO2 Catalyst
    Bera, Parthasarathi
    Lopez Camara, Antonio
    Hornes, Aitor
    Martinez-Arias, Arturo
    [J]. JOURNAL OF PHYSICAL CHEMISTRY C, 2009, 113 (24) : 10689 - 10695
  • [5] SURFACE-REACTIONS OF CO ON A METAL-SEMICONDUCTOR SYSTEM - CU/ZNO
    BOCCUZZI, F
    GHIOTTI, G
    CHIORINO, A
    [J]. SURFACE SCIENCE, 1985, 162 (1-3) : 361 - 367
  • [6] Low temperature CO oxidation on Ni-promoted CuO-CeO2 catalysts
    Chen Guoxing
    Li Qiaoling
    Wei Yucai
    Fang Weiping
    Yang Yiquan
    [J]. CHINESE JOURNAL OF CATALYSIS, 2013, 34 (02) : 322 - 329
  • [7] Selective oxidation of CO in excess hydrogen over CuO/CexZr1-xO2-Al2O3 catalysts
    Chen, Yin-Zu
    Liaw, Biing-Jye
    Chang, Wei-Chian
    Huang, Ching-Tsuen
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (17) : 4550 - 4558
  • [8] Selective oxidation of CO in excess hydrogen over CuO/CexZr1-xO2 catalysts
    Chen, YZ
    Liaw, BJ
    Chen, HC
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2006, 31 (03) : 427 - 435
  • [9] Yttria-stabilized zirconia supported copper oxide catalyst .2. Effect of oxygen vacancy of support on catalytic activity for CO oxidation
    Dow, WP
    Huang, TJ
    [J]. JOURNAL OF CATALYSIS, 1996, 160 (02) : 171 - 182
  • [10] Water gas shift reaction over Cu-Mn mixed oxides catalysts: Effects of the third metal
    Du, Xiaru
    Yuan, Zhongshan
    Cao, Lei
    Zhang, Chunxi
    Wang, Shudong
    [J]. FUEL PROCESSING TECHNOLOGY, 2008, 89 (02) : 131 - 138