Impeller Geometry Effect on Velocity and Solids Suspension

The effect of varying impeller geometrical parameters, including impeller type, number of impeller blades, blade pitch angle and blade thickness, on the turbulent velocity fields in mixing tanks has been studied through LDV measurements. Pitch bladed turbines and disc turbines were used in the experiments. It was found that universal time-mean velocity profiles exist for both pitch bladed turbines and disc turbines. Flow number correlations based on power number for both pitch bladed turbines and disc turbines are presented. It was found that there is a link between impeller pumping capacity and the S parameter in the Zwietering correlation, and this can be expressed as NQ × S = K, where NQ is the impeller flow number and K is a non-dimensional constant independent of the solid/liquid material property and impeller geometry.

[1]  Michael Schäfer,et al.  Detailed LDV Measurements for Visualization of the Flow Field Within a Stirred-Tank Reactor Equipped with a Rushton Turbine , 1997 .

[2]  A. Nienow,et al.  Chapter 16 – The suspension of solid particles , 1992 .

[3]  Jie Wu,et al.  Performance analysis of axial‐flow mixing impellers , 2000 .

[4]  Yonggang Zhu,et al.  Solids suspension with axial‐flow impellers , 2000 .

[5]  Carl M. Stoots,et al.  Mean velocity field relative to a Rushton turbine blade , 1995 .

[6]  Jamshid M. Nouri,et al.  Flow characteristics of stirred reactors with newtonian and non‐newtonian fluids , 1990 .

[7]  Michael Yianneskis,et al.  An experimental study of the steady and unsteady flow characteristics of stirred reactors , 1987, Journal of Fluid Mechanics.

[8]  Alvin W. Nienow,et al.  An LDA study of turbulent flow in a baffled vessel agitated by a pitched blade turbine , 1991 .

[9]  Alvin W. Nienow,et al.  An LDA study of the radial discharge velocities generated by a Rushton turbine : Newtonian fluids, Re ≥ 5 , 1993 .

[10]  Alvin W. Nienow,et al.  An LDA study of the turbulent flow field in a baffled vessel agitated by an axial, down-pumping hydrofoil impeller , 1996 .

[11]  M. F. Edwards,et al.  Mixing in the process industries , 1985 .

[12]  Th.N. Zwietering Suspending of solid particles in liquid by agitators , 1958 .

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

[14]  Michael T. Hicks,et al.  CLOUD HEIGHT IN SOLIDS SUSPENSION AGITATION , 1997 .