CIESC Journal

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富镧稀土镍-苯浆液体系中液相苯加氢反应动力学研究

代世耀a; 徐国华a; 安越a; 陈长聘a; 陈立新b; 王启东b   

  1. a Department of Chemical Engineering,Zhejiang University, Hangzhou,310027,China
    b Department of Materials Science, Zhejiang University, Hangzhou,310027,China
  • 收稿日期:1900-01-01 修回日期:1900-01-01 出版日期:2003-10-28 发布日期:2003-10-28
  • 通讯作者: 代世耀

Kinetics of Liquid-Phase Hydrogenation of Benzene in a Metal Hydride Slurry System Formed
by MlNi5 and Benzene

DAI Shiyaoa; XU Guohuaa; AN Yuea; CHEN Changpina; CHEN Lixinb; WANG Qidongb   

  1. a Department of Chemical Engineering,Zhejiang University, Hangzhou,310027,China
    b Department of Materials Science, Zhejiang University, Hangzhou,310027,China
  • Received:1900-01-01 Revised:1900-01-01 Online:2003-10-28 Published:2003-10-28
  • Contact: DAI Shiyao

摘要: The kinetics of liquid-phase hydrogenation of benzene in misch metal nickel-five (MlNi5)
and benzene slurry system was studied by investigating the influences of the reaction
temperature, pressure, alloy concentration and stirring speed on the mass transfer-reaction
processes inside the slurry. The results show that the whole process is controlled by the
reaction at the surface of the catalyst. The mass transfer resistance at gas-liquid
interface and that from the bulk liquid phase to the surface of the catalyst particles are
negligible. The apparent reaction rate is zero order for benzene concentration and first
order for hydrogen concentration in the liquid phase. The kinetic model obtained fits the
experimental data very well. The apparent activation energy of the hydrogen absorption
reaction of MlNi5-C6H6 slurry system is 42.16 kJ.mol-1.

关键词: hydrogen storage slurry;hydrogen storage alloy;aromatics;hydrogen absorption

Abstract: The kinetics of liquid-phase hydrogenation of benzene in misch metal nickel-five (MlNi5)
and benzene slurry system was studied by investigating the influences of the reaction
temperature, pressure, alloy concentration and stirring speed on the mass transfer-reaction
processes inside the slurry. The results show that the whole process is controlled by the
reaction at the surface of the catalyst. The mass transfer resistance at gas-liquid
interface and that from the bulk liquid phase to the surface of the catalyst particles are
negligible. The apparent reaction rate is zero order for benzene concentration and first
order for hydrogen concentration in the liquid phase. The kinetic model obtained fits the
experimental data very well. The apparent activation energy of the hydrogen absorption
reaction of MlNi5-C6H6 slurry system is 42.16 kJ.mol-1.

Key words: hydrogen storage slurry, hydrogen storage alloy, aromatics, hydrogen absorption