Using ultrasonic Doppler velocimetry and CFD modeling to investigate the mixing of non-Newtonian fluids possessing yield stress

The aim of this work was to investigate the mixing of pseudoplastic fluids possessing yield stress by studying the effect of power consumption, yield stress, impeller type, and impeller clearance on the mixing time. Using these results, it was desired to put together a proposal for mixing system configuration that would form the basis for mixing system optimization. To that end, computational fluid dynamics (CFD) modeling and experiments were performed. In order to determine the capability of CFD to forecast the mixing process, ultrasonic Doppler velocimetry (UDV), which is a non-invasive flow measurement technique for both opaque and transparent fluids, was used to measure fluid velocity. It was observed that the numerical results were in good agreement with the experimental data.

[1]  G. Montante,et al.  CFD simulations and experimental validation of homogenisation curves and mixing time in stirred Newtonian and pseudoplastic liquids , 2005 .

[2]  Farhad Ein-Mozaffari,et al.  Mixing time in an agitated multi-lamp cylindrical photoreactor using electrical resistance tomography , 2008 .

[3]  Farhad Ein-Mozaffari,et al.  Using computational fluid dynamics modeling and ultrasonic doppler velocimetry to study pulp suspension mixing , 2007 .

[4]  Yasushi Takeda,et al.  Velocity profile measurement by ultrasound Doppler shift method , 1986 .

[5]  A. B. Metzner Agitation of non‐Newtonian fluids , 1957 .

[6]  Anupam Dewan,et al.  Fluid dynamics and mixing of single-phase flow in a stirred vessel with a grid disc impeller: Experimental and numerical investigations , 2006 .

[7]  Farhad Ein-Mozaffari,et al.  Simulation of mixing dynamics in agitated pulp stock chests using CFD , 2006 .

[8]  Catherine Xuereb,et al.  CFD analysis of industrial multi-staged stirred vessels , 2006 .

[9]  Marko Zlokarnik,et al.  Stirring: Theory and Practice , 2001 .

[10]  A. Nienow,et al.  Mixing of Highly Viscous Simulated Xanthan Fermentation Broths with the Lightnin A‐315 Impeller , 1992 .

[11]  Tron Solberg,et al.  Flow Generated by an Aerated Rushton Impeller: Two‐phase PIV Experiments and Numerical Simulations , 2008 .

[12]  E. L. Paul,et al.  Handbook of Industrial Mixing: Science and Practice , 2003 .

[13]  Philip K. Chan,et al.  Using electrical resistance tomography and computational fluid dynamics modeling to study the formation of cavern in the mixing of pseudoplastic fluids possessing yield stress , 2008 .

[14]  Farhad Ein-Mozaffari,et al.  Using CFD and Ultrasonic velocimetry to Study the Mixing of Pseudoplastic Fluids with a Helical Ribbon Impeller , 2007 .

[15]  Guy A. Dumont,et al.  Performance and design of agitated pulp stock chests , 2003 .

[16]  Alvin W. Nienow,et al.  A new mathematical model to predict cavern diameters in highly shear thinning, power law liquids using axial flow impellers , 1998 .

[17]  Catherine Xuereb,et al.  Effect of Axial Agitator Configuration (Up-Pumping, Down-Pumping, Reverse Rotation) on Flow Patterns Generated in Stirred Vessels , 2001 .

[18]  Philippe A. Tanguy,et al.  Mixing analysis in a coaxial mixer , 2006 .

[19]  Fernando J. Muzzio,et al.  Extensive validation of computed laminar flow in a stirred tank with three Rushton turbines , 2001 .

[20]  M. Kraume 11th European Conference on Mixing , 2004 .

[21]  Catherine Xuereb,et al.  Scale-up in laminar and transient regimes of a multi-stage stirrer, a CFD approach , 2002 .

[22]  René David,et al.  Effects of the Stirred Tank's Design on Power Consumption and Mixing Time in Liquid Phase , 2000 .

[23]  A. W. Nienow,et al.  CAVERN SIZES IN AGITATED FLUIDS WITH A YIELD STRESS , 1981 .

[24]  Alvin W. Nienow,et al.  X-ray studies of cavern sizes and mixing performance with fluids possessing a yield stress , 1986 .

[25]  W. Kelly,et al.  Using CFD to predict the behavior of power law fluids near axial-flow impellers operating in the transitional flow regime , 2003 .

[26]  Yasushi Takeda,et al.  Development of an ultrasound velocity profile monitor , 1991 .

[27]  S. Masiuk,et al.  Power consumption and mixing time for newtonian and non-newtonian liquids mixing in a ribbon mixer , 1993 .

[28]  Alberto Brucato,et al.  Numerical prediction of flow fields in baffled stirred vessels: A comparison of alternative modelling approaches , 1998 .

[29]  F. Ein-Mozaffari,et al.  Using dynamic tests to study the continuous mixing of xanthan gum solutions , 2008 .

[30]  M. Povey,et al.  Ultrasonic characterization of a food emulsion , 1990 .

[31]  Alvin W. Nienow,et al.  Hydrodynamics of a shear thinning fluid in a tank with axial flow impellers , 1993, Other Conferences.

[32]  Jamshid M. Nouri,et al.  Scalar mixing measurements in batch operated stirred tanks , 1997 .

[33]  Y. Hirata,et al.  Formation and growth of cavern in yield stress fluids agitated under baffled and non-baffled conditions , 1996 .

[34]  Alvin W. Nienow,et al.  A study of an up‐ and a down‐pumping wide blade hydrofoil impeller: Part I. LDA measurements , 1998 .

[35]  Guy A. Dumont,et al.  Measuring Flow Velocity in Pulp Suspension Mixing Using Ultrasonic Doppler Velocimetry , 2007 .

[36]  Philippe A. Tanguy,et al.  Comparison of mixing in two industrial gas–liquid reactors using CFD simulations , 2005 .

[37]  J. Joshi,et al.  Liquid-phase mixing in stirred vessels: turbulent flow regime , 2003 .

[38]  Catherine Xuereb,et al.  Determination of 3-D flow fields in agitated vessels by laser-Doppler velocimetry : Effect of impeller type and liquid viscosity on liquid flow patterns , 1996 .

[39]  Jyeshtharaj B. Joshi,et al.  LIQUID PHASE MIXING IN MECHANICALLY AGITATED VESSELS , 1988 .

[40]  Jyeshtharaj B. Joshi,et al.  Relation between flow pattern and blending in stirred tanks , 1999 .

[41]  Yasushi Takeda,et al.  Velocity profile measurement by ultrasonic doppler method , 1993 .

[42]  Jyeshtharaj B. Joshi,et al.  Effect of impeller design on the flow pattern and mixing in stirred tanks , 2006 .