CFD prediction of liquid homogenisation in a gas–liquid stirred tank

Abstract In this work, simulations of liquid homogenisation were performed for a two-phase gas–liquid stirred tank using computational fluid dynamics (CFD). The predictions were compared with experimental results obtained in a baffled cylindrical vessel stirred by a pitched-blade impeller with constant impeller speed for various volumetric gas flow rates. The CFD simulations were performed in 3D using the FLUENT 6.3 numerical software. The influence of different techniques for simulation of impeller motion (the multiple reference frames and sliding mesh models) on predictions of gas–liquid flow field and tracer distribution was investigated. For the solution, a simplified numerical setup of mono-dispersed bubbles and the k–ɛ mixture turbulence model have been applied. Despite the assumed simplifications, the numerical predictions exhibit a good agreement with the experimental data.

[1]  Jos Derksen,et al.  Population Balance Modeling of Aerated Stirred Vessels Based on CFD , 2002 .

[2]  H.E.A. van den Akker,et al.  Gas-liquid contacting with axial flow impellers , 1994 .

[3]  M. Jahoda,et al.  CFD Prediction of Flow and Homogenization in a Stirred Vessel: Part II Vessel with Three and Four Impellers , 2005 .

[4]  Alvin W. Nienow,et al.  CFD Study of Homogenization with Dual Rushton Turbines—Comparison with Experimental Results: Part II: The Multiple Reference Frame☆ , 2000 .

[5]  Milan Jahoda,et al.  Homogenization of liquids in tanks stirred by multiple impellers , 1994 .

[6]  Alvin W. Nienow,et al.  Blending of Miscible Liquids , 2004 .

[7]  Ville Alopaeus,et al.  Modelling local bubble size distributions in agitated vessels , 2007 .

[8]  Jos Derksen,et al.  Mixing times in a turbulent stirred tank by means of LES , 2006 .

[9]  A. Nienow,et al.  CFD Study of Homogenization with Dual Rushton Turbines—Comparison with Experimental Results: Part I: Initial Studies☆ , 2000 .

[10]  E. L. Paul,et al.  Handbook of Industrial Mixing , 2003 .

[11]  A. Nienow Hydrodynamics of Stirred Bioreactors , 1998 .

[12]  J. Joshi,et al.  CFD simulations of gas-liquid-solid stirred reactor: prediction of critical impeller speed for solid suspension , 2007 .

[13]  Mattias Ljungqvist,et al.  Numerical Simulation of the Two-Phase Flow in an Axially Stirred Vessel , 2001 .

[14]  G. Montante,et al.  Experimental Analysis and Computational Modelling of Gas–Liquid Stirred Vessels , 2007 .

[15]  Alessandro Paglianti,et al.  Gas–liquid flow and bubble size distribution in stirred tanks , 2008 .

[16]  Vivek V. Ranade,et al.  CFD simulation of mixing in tall gas-liquid stirred vessel: Role of local flow patterns , 2006 .

[17]  G. Micale,et al.  Experiments and CFD predictions of solid particle distribution in a vessel agitated with four pitched blade turbines , 2001 .

[18]  Franco Magelli,et al.  MODELLING OF NON-STANDARD MIXERS STIRRED WITH MULTIPLE IMPELLERS† , 1982 .

[19]  M. Špidla,et al.  Solid particle distribution of moderately concentrated suspensions in a pilot plant stirred vessel , 2005 .

[20]  Alberto Brucato,et al.  Modelling and Simulation of Gas–Liquid Hydrodynamics in Mechanically Stirred Tanks , 2007 .

[21]  M. Jahoda,et al.  CFD modelling of liquid homogenization in stirred tanks with one and two impellers using large eddy simulation , 2007 .

[22]  Alvin W. Nienow,et al.  On impeller circulation and mixing effectiveness in the turbulent flow regime , 1997 .