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首页> 外文期刊>Fuel >Plasma-catalytic reforming of CO2-rich biogas over Ni/gamma-Al2O3 catalysts in a rotating gliding arc reactor
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Plasma-catalytic reforming of CO2-rich biogas over Ni/gamma-Al2O3 catalysts in a rotating gliding arc reactor

机译:Ni /γ-Al2O3催化剂在旋转滑动电弧反应器中等离子体催化重整富含CO2的沼气

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摘要

The combination of plasma and heterogeneous catalysis has been considered as an attractive and promising process for the synthesis of fuels and chemicals. In this work, plasma-catalytic reforming of biogas is carried out over Ni/gamma-Al2O3 catalysts with different Ni loadings (6 wt.%, 8 wt.% and 10 wt.% Ni) in a novel rotating gliding arc (RGA) plasma reactor. In the plasma reforming of biogas without a catalyst, the CH4 conversion can reach up to 52.6% at a CH4/CO2 molar ratio of 3: 7 and a total flow rate of 6 L/min. The combination of the RGA with the Ni/gamma-Al2O3 catalysts enhances the performance of the plasma biogas reforming: increasing Ni loading enhances the conversion of CH4 and the maximum CH4 conversion of 58.5% is achieved when placing the 10 wt.% Ni/gamma-Al2O3 catalyst in the downstream of the RGA reactor. The presence of the 10 wt.% Ni/gamma-Al2O3 catalyst in the RGA reactor also increases the H-2 yield by 17.6% compared to the reaction in the absence of a catalyst. A comparison of biogas reforming using different plasma technologies shows that the RGA plasma provides a higher conversion, significantly enhanced processing capacity and reduced energy cost for biogas conversion and syngas production. In addition, compared to biogas reforming using other non-thermal plasmas (e. g. dielectric barrier discharge), the RGA reforming process produces much cleaner gas products in which syngas is the major one. (C) 2017 Elsevier Ltd. All rights reserved.
机译:等离子体和非均相催化的结合已经被认为是用于合成燃料和化学物质的有吸引力且有希望的方法。在这项工作中,在新颖的旋转滑动电弧(RGA)中,在具有不同Ni含量(6%(重量),8%(重量)和10%(重量))的Ni /γ-Al2O3催化剂上进行沼气的等离子体催化重整。等离子反应器。在没有催化剂的沼气的等离子体重整中,CH4 / CO2摩尔比为3:7,总流速为6 L / min时,CH4转化率可以达到52.6%。 RGA与Ni /γ-Al2O3催化剂的结合可增强等离子体沼气重整的性能:增加Ni的负载量可提高CH4的转化率,当放置10 wt。%的Ni /γ时,CH4的最大转化率达到58.5%。 RGA反应器下游的-Al2O3催化剂。与不存在催化剂的反应相比,在RGA反应器中存在10重量%的Ni /γ-Al2 O 3催化剂也使H-2的产率提高了17.6%。使用不同等离子体技术进行的沼气重整的比较表明,RGA等离子体可提供更高的转化率,显着提高了处理能力,并降低了沼气转化和合成气生产的能源成本。另外,与使用其他非热等离子体的沼气重整(例如介电势垒放电)相比,RGA重整过程产生了更清洁的气体产物,其中合成气是主要产物。 (C)2017 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Fuel》 |2017年第1期|430-437|共8页
  • 作者单位

    Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China;

    Zhejiang Univ Technol, Inst Energy & Power Engn, Coll Mech Engn, Hangzhou 310014, Zhejiang, Peoples R China;

    Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China;

    Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China;

    Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China;

    Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China;

    Univ Liverpool, Dept Elect Engn & Elect, Liverpool L69 3GJ, Merseyside, England;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Rotating gliding arc (RGA); Plasma-catalysis; Biogas reforming; Syngas;

    机译:旋转滑弧;等离子体催化;沼气重整;合成气;

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