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Highly Selective Co Methanation over Amorphous Ni–Ru–B/Zro2 Catalyst

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Highly Selective Co Methanation over Amorphous Ni–Ru–B/Zro2 Catalyst
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Chinese Chemical Letters 20 (2009) 889–892 www.elsevier.com/locate/cclet

Highly selective CO methanation over amorphous Ni–Ru–B/ZrO2 catalyst
Qi Hai Liu, Xin Fa Dong *, Wei Ming Lin
School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, China Received 15 December 2008

Abstract Amorphous Ni–Ru–B/ZrO2 catalyst was prepared by the means of chemical reduction, and selective CO methanation as a strategy for CO removal in fuel processing applications was investigated over the amorphous Ni–Ru–B/ZrO2 catalyst. The result showed that, at the temperature of 210–230 8C, the catalyst was shown to be capable of reducing CO in a hydrogen-rich reformate to less than 10 ppm, while keeping the CO2 conversion below 1.55% and the hydrogen consumption below 6.50%. # 2009 Xin Fa Dong. Published by Elsevier B.V. on behalf of Chinese Chemical Society. All rights reserved.
Keywords: Selective methanation; CO; Amorphous; Ni–Ru–B/ZrO2 catalyst

Removal of CO from reformed fuels by means of selective methanation for fuel cells has been recently proved to be an effective strategy [1,2], for it does not require any oxygen (air) addition, since the necessary reactants (CO and H2) are already present. The challenge of this means is that the CO2 co-methanation will consume a great amount of hydrogen because of the presence of relative high concentration of CO2 (18–23 vol%). As a result, it was required for the catalyst to have excellent activity and high selectivity for the CO methanation to avoid the co-methanation of CO2. Among all the catalyst investigated previously, crystalline Ni-base and Ru-base catalysts were paid the most attention, such as Ni/ZrO2 [1], Ru/TiO2 [3], Rh-modified Ni–La2O3–Ru/Al2O3 [4] and Ru/Al2O3 [2,5] catalysts. For amorphous catalyst, although it has been proved to be excellent for many hydrogenating reactions [6,7], it has not been considered seriously to be utilized



References: [1] [2] [3] [4] [5] [6] [7] [8] [9] [10] Q.H. Liu, X.F. Dong, X.M. Mo, et al. J. Nat. Gas Chem. 17 (2008) 268. R.A. Dagle, Y. Wang, G. Xia, et al. Appl. Catal. A 326 (2007) 213. S. Takenaka, T. Shimizu, K. Otsuka, Int. J. Hydrogen Energ. 29 (2004) 1065. M.B.I. Choudhury, S. Ahmed, M.A. Shalabi, et al. Appl. Catal. A 314 (2006) 47. P. Panagiotopoulou, D.I. Kondarides, X.E. Verykios, Appl. Catal. A 344 (2008) 45. H.X. Li, Y.D. Wu, J. Zhang, et al. Appl. Catal. A 275 (2004) 199. Y.J. Hou, Y.Q. Wang, F. He, et al. Mater. Lett. 58 (2004) 1267. A. Yokoyama, H. Komiyama, H. Inoue, et al. J. Catal. 68 (1981) 355. H. Habazaki, M. Yamasaki, B. Zhang, et al. Appl. Catal. A 172 (1998) 131. Z.Z. Yuan, J.M. Chen, Y. Lu, et al. J. Alloys Compd. 450 (2008) 245.

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