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以非晶态合金催化剂SRNA-4为固相的气液固磁稳定床的界面传质研究
引用本文:李韡,宗保宁,李晓芳,孟祥坤,张金利.以非晶态合金催化剂SRNA-4为固相的气液固磁稳定床的界面传质研究[J].中国化学工程学报,2006,14(6):734-739.
作者姓名:李韡  宗保宁  李晓芳  孟祥坤  张金利
作者单位:School of Chemical Engineering Tianjin University,Research Institute of Petroleum Processing,SINOPEC,School of Chemical Engineering,Tianjin University,Research Institute of Petroleum Processing,SINOPEC,School of Chemical Engineering,Tianjin University,Tianjin 300072,China,Beijing 100083,China,Tianjin 300072,China,Beijing 100083,China,Tianjin 300072,China
基金项目:国家自然科学基金,国家重点基础研究发展计划(973计划),中国石油化工集团公司资助项目
摘    要:1 INTRODUCTION Magnetically stabilized beds (MSB) exhibit an unique combination of packed-bed and fluidized-bed properties. Gas-liquid-solid (G-L-S) three-phase MSB has recently attracted more attention in the field of biotechnology processes (such as bioseparation or immobilized enzyme systems) and chemical engi- neering(such as the hydrogenation reaction system). The interphase mass transfer behavior plays an im- portant role in the optimal operation of practical MSB. However, many…

关 键 词:magnetically  stabilized  bed  gas-liquid  mass  transfer  liquid-solid  mass  transfer  SRNA-4  catalyst
收稿时间:8 November 2005
修稿时间: 

Interphase Mass Transfer in G-L-S Magnetically Stabilized Bed with Amorphous Alloy SRNA-4 Catalyst
Wei LI, Baoning ZONG, Xiaofang LI, Xiangkun MENG,Jinli ZHANG,.Interphase Mass Transfer in G-L-S Magnetically Stabilized Bed with Amorphous Alloy SRNA-4 Catalyst[J].Chinese Journal of Chemical Engineering,2006,14(6):734-739.
Authors:Wei LI  Baoning ZONG  Xiaofang LI  Xiangkun MENG  Jinli ZHANG  
Affiliation:

aSchool of Chemical Engineering, Tianjin University, Tianjin 300072, China

bResearch Institute of Petroleum Processing, SINOPEC, Beijing 100083, China

Abstract:Gas-liquid (G-L) and liquid-solid (L-S) mass transfer coefficients were characterized in a gas-liquid-solid(G-L-S) three-phase magnetically stabilized bed (MSB) using amorphous alloy SRNA-4 as the solid phase. Effects such as superficial liquid velocity, superficial gas velocity, magnetic strength, liquid viscosity, and particle size were investigated. Experimental results indicated that the G-L volumetric mass transfer coefficients (KLa) increased along with the magnetic strength, superficial gas and liquid velocities. Proper increase of liquid viscosity promoted KLa only in the range of lower liquid viscosity. The external magnetic field made L-S mass transfer coefficients (Ks)in the G-L-S MSB lower than those of conventional fluidized beds. Ks in the MSB almost kept constant as the superficial liquid velocity and superficial gas velocity increased and decreased with the liquid viscosity and surface tension, while increased with the particle size Ks showed uniform axial and radial distributions except of small decreases close to the wall. Dimensionless correlations were established to estimate KLa and Ks of the MSB with SRNA-4 catalysts, which showed the average error of 5.4% and 2.5% respectively.
Keywords:magnetically stabilized bed  gas-liquid mass transfer  liquid-solid mass transfer  SRNA-4 catalyst
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