CFD Simulation of Solid-Liquid Stirred Tank with Rushton Turbine and Propeller Impeller
Stirred tanks have applications in many chemical
processes where mixing is important for the overall performance of
the system. In present work 5%v of the tank is filled by solid particles
with diameter of 700 m that Rushton Turbine and Propeller impeller
is used for stirring. An Eulerian-Eulerian Multi Fluid Model coupled
and for modeling rotating of impeller, moving reference frame
(MRF) technique was used and standard-k- model was selected for
turbulency. Flow field, radial velocity and axial distribution of solid
for both of impellers was investigation and comparison. Comparisons
of simulation results between Rushton Turbine and propeller impeller
shows that final quality of solid-liquid slurry in different rotating
speed for propeller impeller is better than the Rushton Turbine.
[1] Brucato, A., M. Ciofalo, F. Grisafi and G. Micale, "Numerical prediction
of flow fields in based stirred essels: A comparison of alternative
modelling approaches", Chem. Eng. Sci. 53, 1998, pp. 3653-3684.
[2] Micale, G., Montante, G., Grisafi, F., Brucato, A. & Godfrey, J. "CFD
Simulation of Particle Distribution in Stirred Vessels". Chemical
Engineering Research and Design, 78, 2000. pp. 435-444.
[3] Micale, G., Grisafi, F., Rizzuti, L. & Brucato, A. "CFD Simulation of
Particle Suspension Height in Stirred Vessels". Chemical Engineering
Research and Design, 82, 2004, pp.1204-1213.
[4] Ochieng, A. & Lewis, A. E. "CFD simulation of solids off-bottom
suspension and loud height". Hydrometallurgy, 82, 2006. pp. 1-12.
[5] Ding, J. & Gidaspow, D. "A bubbling fluidization model using kinetic
theory of ranular flow". AIChE Journal, 36, 1990. pp. 523-538.
[6] F.Satio, A.W.Nienow, S.Chatwin, I.P.T.Moore, "Power, gas dispersion
and homogenisation characteristics of Scaba SRGT and Rushton turbine
impellers", J Chem Eng Japan, 25(3), 1992, pp.281- 287.
[7] A.Bakker, K.J.Myers, and J.M.Smith, "How to disperse gases in
liquids", Chem Eng, 101(12), 1994, pp.98-104.
[8] A. W. Nienow, "Gas-liquid mixing studies: a comparison of Rushton
turbines with some modern impellers", Chem Eng Res Des, 74, 1996,
pp.417-423.
[9] A.Bakker, "Impeller assembly with asymmetric Concave blades", US
Patent 5791780, 1998.
[1] Brucato, A., M. Ciofalo, F. Grisafi and G. Micale, "Numerical prediction
of flow fields in based stirred essels: A comparison of alternative
modelling approaches", Chem. Eng. Sci. 53, 1998, pp. 3653-3684.
[2] Micale, G., Montante, G., Grisafi, F., Brucato, A. & Godfrey, J. "CFD
Simulation of Particle Distribution in Stirred Vessels". Chemical
Engineering Research and Design, 78, 2000. pp. 435-444.
[3] Micale, G., Grisafi, F., Rizzuti, L. & Brucato, A. "CFD Simulation of
Particle Suspension Height in Stirred Vessels". Chemical Engineering
Research and Design, 82, 2004, pp.1204-1213.
[4] Ochieng, A. & Lewis, A. E. "CFD simulation of solids off-bottom
suspension and loud height". Hydrometallurgy, 82, 2006. pp. 1-12.
[5] Ding, J. & Gidaspow, D. "A bubbling fluidization model using kinetic
theory of ranular flow". AIChE Journal, 36, 1990. pp. 523-538.
[6] F.Satio, A.W.Nienow, S.Chatwin, I.P.T.Moore, "Power, gas dispersion
and homogenisation characteristics of Scaba SRGT and Rushton turbine
impellers", J Chem Eng Japan, 25(3), 1992, pp.281- 287.
[7] A.Bakker, K.J.Myers, and J.M.Smith, "How to disperse gases in
liquids", Chem Eng, 101(12), 1994, pp.98-104.
[8] A. W. Nienow, "Gas-liquid mixing studies: a comparison of Rushton
turbines with some modern impellers", Chem Eng Res Des, 74, 1996,
pp.417-423.
[9] A.Bakker, "Impeller assembly with asymmetric Concave blades", US
Patent 5791780, 1998.
@article{"International Journal of Chemical, Materials and Biomolecular Sciences:51458", author = "M. H. Pour and V. M. Nansa and M. Saberi and A. M. Ghanadi and A. Aghayari and M. Mirzajanzadeh", title = "CFD Simulation of Solid-Liquid Stirred Tank with Rushton Turbine and Propeller Impeller", abstract = "Stirred tanks have applications in many chemical
processes where mixing is important for the overall performance of
the system. In present work 5%v of the tank is filled by solid particles
with diameter of 700 m that Rushton Turbine and Propeller impeller
is used for stirring. An Eulerian-Eulerian Multi Fluid Model coupled
and for modeling rotating of impeller, moving reference frame
(MRF) technique was used and standard-k- model was selected for
turbulency. Flow field, radial velocity and axial distribution of solid
for both of impellers was investigation and comparison. Comparisons
of simulation results between Rushton Turbine and propeller impeller
shows that final quality of solid-liquid slurry in different rotating
speed for propeller impeller is better than the Rushton Turbine.", keywords = "CFD, Particle Velocity, Propeller Impeller, Rushton Turbine.", volume = "7", number = "6", pages = "366-4", }