Journal of South China University of Technology (Natural Science Edition) ›› 2009, Vol. 37 ›› Issue (12): 44-48,69.

• Chemistry & Chemical Engineering • Previous Articles     Next Articles

Purification of CO via Selective Methanation Using Microchannel Reactor

Dong Xin-fa  Liu Wen-yue  Gao Jun  Lin Wei-ming   

  1. School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, Guangdong, China
  • Received:2008-11-05 Revised:2009-02-19 Online:2009-12-25 Published:2009-12-25
  • Contact: 董新法(1964-),男,教授,主要从事氢能源及技术研究. E-mail:cexfdong@scut.edu.cn
  • About author:董新法(1964-),男,教授,主要从事氢能源及技术研究.
  • Supported by:

    国家自然科学基金资助项目(20576023);广东省自然科学基金资助项目(06025660)

Abstract:

In order to effectively remove the small-quantity CO in hydrogen-rich reformed gas, 4Ni-2Ru/ZrO2 bimetallic catalyst was homogeneously coated on a microchannel reactor, and the method of selective methanation was used to purify CO. Then, the effects of calcination temperature, coating method, CTAB/Zr molar ratio and space velocity on the catalyst performance were investigated. Experimental results show that (1) when the calcination is performed at 350 ℃ after each slurry loading with a CTAB/Zr molar ratio of 0.35 and with a space velocity of 14286 h- 1, 4Ni-2Ru/ZrO2 catalyst is of excellent performance in low temperature, and the volume fraction of CO at the outlet reduces to 0. 0013 % at 260 ℃; and (2) a space velocity of 13000 -20000 h- 1 is suitable for the catalyst calcined at 350 ℃ after each slurry loading with a CTAB/Zr molar ratio of 0.35

Key words: CO purification, selective methanation, hydrogen-rich reformed gas, microchannel reactor