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Interphase Mass Transfer in G-L-S Magnetically Stabilized Bed with Amorphous Alloy SRNA-4 Catalyst 被引量:1

Interphase Mass Transfer in G-L-S Magnetically Stabilized Bed with Amorphous Alloy SRNA-4 Catalyst
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摘要 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 su- perficial 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 de- creases 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. 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 su- perficial 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 de- creases 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.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2006年第6X期734-739,共6页 中国化学工程学报(英文版)
基金 the National Natural Science Foundation of China (No.20206023, No.20676096) the Special Funds for MajorState Basic Research Program of China (973 Program, 2006CB202500) SINOPEC (X504029).
关键词 magnetically stabilized bed GAS-LIQUID MASS TRANSFER liquid-solid MASS TRANSFER SRNA-4 CATALYST magnetically stabilized bed, gas-liquid mass transfer, liquid-solid mass transfer, SRNA-4 catalyst
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  • 1Hausmann, R.,Reichert, C.,Franzreb, M.,Holl, W. H.“Liquid-phase mass transfer of magnetic ion exchangers in magnetically fluidized beds II. AC field”[].React Funct Polym.2004
  • 2Franzreb, M.,Hausmann, R.,Hoffmann, C.,Holl, W.H.“Liquid-phase mass transfer of magnetic ion exchangers in magnetically fluidized beds I. DC fields”[].React Funct Polym.2001
  • 3Jovanovic, G.,Al-Mulhim M.“Liquid-solid mass trans- fer in magnetically stabilized fluidized beds”[].Annual Meeting Miami Beach CA (.1995
  • 4Webb, C.,Kang, H.K.,Moffat, G.,Williams, R.A.“Magnetically stabilized fluidized bed bioreactor: A tool for improved mass transfer in immobilized enzyme sys- tems”[].Chem Eng Biochem Eng.1996
  • 5Chen, C.M.,Leu, L.P.“Hydrodynamics and mass trans- fer in three-phase magnetic fluidized beds”[].Powder Technol.2001
  • 6Song, J,Hyndman, C. L,,Kantzas, A.“Effect of particle tethering and scale-up on solid-liquid mass transfer in three-phase fluidized beds of light particles”[].Can J Chem Eng.2001
  • 7Cheng, C.Y.,Yung, K.“Effect of magnetic field on heat and mass transfer by natural convection from vertical surfaces in porous media-an integral approach”[].Int Comm Heat Mass Transfer.1999
  • 8Meng, X.K.,Mu, X.H.,Zong, B.N.,Min, E.Z.,Zhu, Z.H.,Fu, S.B.,Luo, Y.B.“Purification of caprolactam in magnetically stabilized bed reactor”[].Catal Today.2003
  • 9Rao, V.G,,Drinkenburg, A.A.H.“Solid-liquid mass trans- fer in packed beds with cocurrent gas-liquid downflow”[].AIChE J.1985
  • 10Muroyama, K.,Yoshikawa, T.,Takakura, S.,Yamanaka, Y.“Mass transfer from an immersed cylinder in three-phase systems with fine suspended particles”[].Chem Eng Sci.1997

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