• RESEARCH NOTES • Previous Articles     Next Articles

CFD Simulation of Hydrodynamic Characteristics in Stirred Reactors Equipped with Standard
Rushton or 45°-Upward PBT Impeller

WEI Zuojuna; XU shiminb; YUAN Yingjina; XU Songlinb   

  1. a Department of Pharmaceutical Engineering, School of Chemical Engineering and Technology,
    Tianjin University, Tianjin 300072, China
    b National Engineering Research Center for Distillation Technology, Tianjin University,
    Tianjin 300072, China
  • Received:1900-01-01 Revised:1900-01-01 Online:2003-08-28 Published:2003-08-28
  • Contact: WEI Zuojun

采用CFD模拟装备标准透平桨或45°-斜向上桨搅拌反应器内部流体力学特性

未作君a; 徐世民b; 元英进a; 许松林b   

  1. a Department of Pharmaceutical Engineering, School of Chemical Engineering and Technology,
    Tianjin University, Tianjin 300072, China
    b National Engineering Research Center for Distillation Technology, Tianjin University,
    Tianjin 300072, China
  • 通讯作者: 未作君

Abstract: The hydrodynamic characteristics generated by the standard Rushton or 45°-upward pitched-
blade-turbine (PBT) impellers in a baffled reactor are numerically simulated for different
off-bottom clearances (C = 1/3Hand 1/2H) and agitator speeds (100, 150, 200, 250 and
300r.min-1) by using FLUENT code (Version 5.4). Theresults are compared with the
experimental and simulated data in the published papers and good agreement isobserved. The
shapes of the profile of mean velocities seem independent to the speed of agitators under
theexperimental conditions (100-300 r.min-1).

Key words: computational fluid dynamics, hydrodynamics, stirred tank, sliding mesh method

摘要: The hydrodynamic characteristics generated by the standard Rushton or 45°-upward pitched-
blade-turbine (PBT) impellers in a baffled reactor are numerically simulated for different
off-bottom clearances (C = 1/3Hand 1/2H) and agitator speeds (100, 150, 200, 250 and
300r.min-1) by using FLUENT code (Version 5.4). Theresults are compared with the
experimental and simulated data in the published papers and good agreement isobserved. The
shapes of the profile of mean velocities seem independent to the speed of agitators under
theexperimental conditions (100-300 r.min-1).

关键词: computational fluid dynamics;hydrodynamics;stirred tank;sliding mesh method