CIESC Journal

• Volume 1 • 上一篇    下一篇

DIFFUSION AND REACTION OF BENZENE HYDROGENATION OVER POROUS Ni/γ-Al_2O_3 CATALYST

葛庆峰; 李绍芬; 廖晖   

  1. Department of Chemical Engineering, Tianjin University, Tianjin 300072, China
  • 收稿日期:1992-05-04 修回日期:1992-10-29 出版日期:1993-12-28 发布日期:1993-12-28
  • 通讯作者: 葛庆峰

DIFFUSION AND REACTION OF BENZENE HYDROGENATION OVER POROUS Ni/γ-Al_2O_3 CATALYST

GE Qingfeng; LI Shaofen; LIAO Hui   

  1. Department of Chemical Engineering, Tianjin University, Tianjin 300072, China
  • Received:1992-05-04 Revised:1992-10-29 Online:1993-12-28 Published:1993-12-28
  • Contact: GE Qingfeng

摘要: The macro-kinetics of benzene hydrogenation over porous Ni/γ-Al_2O_3 catalyst was measured with asingle-pellet diffusion reactor.Based on the dusty-gas model,the differential equations by taking into account ofthe variation of effective diffusivities with the composition were derived to describe the diffusion and reactionprocesses of reacting species over porous catalyst.Using the tortuosity factors determined under the condition ofsteady physical diffusion,the global reaction rates were calculated by solving the equations,and the results are ingood agreement with the experimental data obtained.

关键词: diffusion-reaction;kinetics;benzene hydrogenation;multicomponent diffusion

Abstract: The macro-kinetics of benzene hydrogenation over porous Ni/γ-Al_2O_3 catalyst was measured with asingle-pellet diffusion reactor.Based on the dusty-gas model,the differential equations by taking into account ofthe variation of effective diffusivities with the composition were derived to describe the diffusion and reactionprocesses of reacting species over porous catalyst.Using the tortuosity factors determined under the condition ofsteady physical diffusion,the global reaction rates were calculated by solving the equations,and the results are ingood agreement with the experimental data obtained.

Key words: diffusion-reaction, kinetics, benzene hydrogenation, multicomponent diffusion