期刊文献+

Hydrogen and syngas production from two-step steam reforming of methane using CeO_2 as oxygen carrier 被引量:4

Hydrogen and syngas production from two-step steam reforming of methane using CeO_2 as oxygen carrier
下载PDF
导出
摘要 CeO2 oxygen carrier was prepared by precipitation method and tested by two-step steam reforming of methane (SRM). Two-step SRM for hydrogen and syngas generation is investigated in a fixed-bed reactor. Methane is directly converted to syngas at a H2/CO ratio close to 2 : 1 at a high temperature (above 750 °C) by the lattice oxygen of CeO2; methane cracking is found when the reduction degree of CeO2 was above 5.0% at 850 °C in methane isothermal reaction. CeO2?δ obtained from methane isothermal reaction can split water to generate CO-free hydrogen and renew its lattice oxygen at 700 °C; simultaneously, deposited carbon is selectively oxidized to CO2 by steam following the reaction (C+2H2O→CO2+2H2). Slight deactivation in terms of amounts of desired products (syngas and hydrogen) is observed in ten repetitive two-step SRM process due to the carbon deposition on CeO2 surface as well as sintering of CeO2. CeO2 oxygen carrier was prepared by precipitation method and tested by two-step steam reforming of methane (SRM). Two-step SRM for hydrogen and syngas generation is investigated in a fixed-bed reactor. Methane is directly converted to syngas at a H2/CO ratio close to 2 : 1 at a high temperature (above 750 °C) by the lattice oxygen of CeO2; methane cracking is found when the reduction degree of CeO2 was above 5.0% at 850 °C in methane isothermal reaction. CeO2?δ obtained from methane isothermal reaction can split water to generate CO-free hydrogen and renew its lattice oxygen at 700 °C; simultaneously, deposited carbon is selectively oxidized to CO2 by steam following the reaction (C+2H2O→CO2+2H2). Slight deactivation in terms of amounts of desired products (syngas and hydrogen) is observed in ten repetitive two-step SRM process due to the carbon deposition on CeO2 surface as well as sintering of CeO2.
出处 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2011年第3期281-286,共6页 天然气化学杂志(英文版)
基金 supported by the National Natural Science Foundation of China (NO. 51004060) the Natural Science Foundation of Yunnan Province (NO. 2008E030M, 2010ZC108) the Research Foundation for the Doctoral Program of Higher Education of China (NO. 20095314120005) the Analysis and Test Foundation of Kunming University of Science and Technology (KUST) the 2010 Innovation Foundation of KUST
关键词 two-step steam reforming of methane CEO2 HYDROGEN SYNGAS redox cycle two-step steam reforming of methane CeO2 hydrogen syngas redox cycle
  • 相关文献

参考文献26

  • 1Steinfeld A. Sol Energy, 2005, 78(5): 603.
  • 2Holladay J D, Hu J, King D L, Wang Y. Catal Today, 2009, 139(4): 244.
  • 3Pregger T, Graf D, Krewitt W, Sattler C, Roeb M, M611er S. lnt J Hydrogen Energy, 2009, 34(10): 4256.
  • 4Steinfeld A, Kuhn P, Karni J. Energy, 1993, 18(3): 239.
  • 5Alizadeh R, Jamshidi E, Zhang G E J Nat Gas Chem, 2009,18(2): 124.
  • 6Evdou A, Zaspalis V, Nalbandian L. Fuel, 2010, 89(6): 1265.
  • 7Go K S, Son S R, Kim S D, Kang K S, Park C S. IntJHydrogen Energy, 2009, 34(3): 1301.
  • 8Kodama T, Ohtake H, Matsumoto S, Aoki A, Shimizu T, Ki- tayama Y. Energy, 2000, 25(5): 411.
  • 9Shimizu T, Shimizu K, Kitayama Y, Kodama T. Sol Energy, 2001, 71(5): 315.
  • 10Forster M. Energy, 2004, 29(5-6): 789.

同被引文献26

引证文献4

二级引证文献31

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部