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热等离子体与催化剂协同重整CH4-CO2

魏强 徐艳 张晓晴 赵川川 戴晓雁 印永祥

魏强, 徐艳, 张晓晴, 赵川川, 戴晓雁, 印永祥. 热等离子体与催化剂协同重整CH4-CO2[J]. 燃料化学学报(中英文), 2013, 41(03): 328-334.
引用本文: 魏强, 徐艳, 张晓晴, 赵川川, 戴晓雁, 印永祥. 热等离子体与催化剂协同重整CH4-CO2[J]. 燃料化学学报(中英文), 2013, 41(03): 328-334.
WEI Qiang, XU Yan, ZHANG Xiao-qing, ZHAO Chuan-chuan, DAI Xiao-yan, YIN Yong-xiang. CH4-CO2 reforming by combination of plasma and catalysts[J]. Journal of Fuel Chemistry and Technology, 2013, 41(03): 328-334.
Citation: WEI Qiang, XU Yan, ZHANG Xiao-qing, ZHAO Chuan-chuan, DAI Xiao-yan, YIN Yong-xiang. CH4-CO2 reforming by combination of plasma and catalysts[J]. Journal of Fuel Chemistry and Technology, 2013, 41(03): 328-334.

热等离子体与催化剂协同重整CH4-CO2

详细信息
    通讯作者:

    印永祥,E-mail:hyyxo675@sina.com.

  • 中图分类号: O646.9

CH4-CO2 reforming by combination of plasma and catalysts

  • 摘要: 考察了热等离子体与催化剂协同作用于重整反应过程。实验采用三种不同的模式进行:等离子体单独作用、等离子体与催化剂协同作用、等离子体与催化剂协同作用且部分原料气引入等离子体放电区。结果表明,在模式三下,当原料气的总流量为5 m3/h、CH4/CO2物质的量比为4/6、等离子体的输入功率为14.4 kW时,CH4-CO2重整过程可获得最佳结果,CH4转化率为77.00%、CO2转化率为62.40%、H2选择性为96.70%、CO选择性为88.60%、反应比能为193 kJ/mol、过程的能量转化率为66.4%,该结果已十分接近CH4-H2O(g)重整的技术指标。最佳结果主要得益于模式三下的三种不同的反应路径,放电反应、热化学反应与催化反应。
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出版历程
  • 收稿日期:  2012-08-13
  • 修回日期:  2012-11-21
  • 刊出日期:  2013-03-30

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