Numerical Comparison of Rushton Turbine and CD-6 Impeller in Non-Newtonian Fluid Stirred Tank
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Numerical Comparison of Rushton Turbine and CD-6 Impeller in Non-Newtonian Fluid Stirred Tank

Authors: Akhilesh Khapre, Basudeb Munshi

Abstract:

A computational fluid dynamics simulation is done for non-Newtonian fluid in a baffled stirred tank. The CMC solution is taken as non-Newtonian shear thinning fluid for simulation. The Reynolds Average Navier Stocks equation with steady state multi reference frame approach is used to simulate flow in the stirred tank. The turbulent flow field is modelled using realizable k-ε turbulence model. The simulated velocity profiles of Rushton turbine is validated with literature data. Then, the simulated flow field of CD-6 impeller is compared with the Rushton turbine. The flow field generated by CD-6 impeller is less in magnitude than the Rushton turbine. The impeller global parameter, power number and flow number, and entropy generation due to viscous dissipation rate is also reported.

Keywords: Computational fluid dynamics, non-Newtonian, Rushton turbine, CD-6 impeller, power number, flow number, viscous dissipation rate.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1097247

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[1] Y. Kawase, K. Shimizu, T. Araki and T. Shimodaira, “Hydrodynamics in three-phase stirred tank reactors with non-Newtonian fluids,” Industrial & Engineering Chemistry Research, vol. 36, no. 1, pp. 270–276, 1997.
[2] H. Ameur, M. Bouzit and M. Helmaoui, “Numerical study of fluid flow and power consumption in a stirred vessel with a Scaba 6SRGT impeller,” Chemical and Process Engineering, vol. 32, no. 4, pp. 351– 366, 2011.
[3] E. Koutsakos and A.W. Nienow, Effects of rheological properties of simulated fermentation broths on flows in stirred bioreactors: A laser anemometry study, Rheology of food, pharmaceutical and biological martials with general rheology, R.E. Carter (ed.), pp. 284–303, 1990.
[4] J. Nouri and J. Whitelaw, “Flow characteristics of stirred reactors with Newtonian and non-Newtonian fluids,” AIChE Journal, vol. 36, no. 4, pp. 627–629, 1990.
[5] J. Solomon, T. Elson and A. W. Nienow, “Cavern sizes in agitated fluids with a yield stress,” Chemical Engineering Communication, vol. 11, no. 1-3, pp. 143-164, 1981.
[6] B. Venneker, J. Derksen and H. E. A. Van den Akker, “Turbulent flow of shear-thinning liquids in stirred tanks-The effects of Reynolds number and flow index,” Chemical Engineering Research and Design, vol. 88, no. 7A, pp. 827–843, 2010.
[7] H. Ameur and M. Bouzit, “Mixing in shear thinning fluids,” Brazilian Journal of Chemical Engineering, vol. 29, no. 2, pp. 349–358, 2012.
[8] M. Dular, T. Bajcar, L. Slemenik-Perse, M. Zumer and B. Sirok, “Numerical simulation and experimental study of non-Newtonian mixing flow with a free surface,” Brazilian Journal of Chemical Engineering, vol. 23, no. 4, pp. 473–486, 2006.
[9] P. Tanguy, M. Heniche, C. Rivera, C. Devals and K. Takenaka, “Recent developments in CFD applied to viscous and non-Newtonian mixing in agitated vessels,” Paper presented at 5th International Conference on CFD in the Process Industries, CSIRO, Melbourne, Australia, 2006.
[10] W. Kelly and B. Gigas, “Using CFD to predict the behaviour of power law liquids near axial-flow impellers operating in the transitional flow regime,” Chemical Engineering Science, vol. 58, no. 10, pp. 2141-2152, 2003.
[11] W. Binxin, “CFD investigation of turbulence models for mechanical agitation of non-Newtonian fluids in anaerobic digesters,” Water Research, vol. 45, no. 5, pp. 2082-2094, 2011.
[12] S. Masiuk and H. Lacki, “Power consumption and mixing times for Newtonian and non-Newtonian liquids mixing in a ribbon mixer,” The Chemical Engineering Journal, vol. 52, no. 1, pp. 13–17, 1993.
[13] J. Netusil and F. Rieger, “Power consumption of screw and helical ribbon agitators in highly viscous pseudoplastic fluids,” The Chemical Engineering Journal, vol. 52, no. 1, pp. 9–12, 1993.
[14] M. Ammar, W. Chtourou, Z. Driss, M. S. Abid, “Numerical investigation of turbulent flow generated in baffled stirred vessels equipped with three different turbines in one and two stage system,” Energy, vol. 36, no. 8, pp. 5081–5093, 2011.
[15] N. Dohi, T. Takahashi, K. Minekawa, Y. Kawase, “Power consumption and solid suspension performance of large-scale impellers in gas-liquidsolid three phase stirred tank reactors,” Chemical Engineering Journal, vol. 97, no. 2-3, pp. 103–114, 2004.
[16] A. R. Khopkar and P. A. Tanguy, “CFD simulation of gas-liquid flows in stirred vessel equipped with Rushton turbines: influence of parallel, merging and diverging flow configuration,” Chemical Engineering Science, vol. 63, no. 14, pp. 3810–3820, 2008.
[17] G. F. Naterer and O. B. Adeyinka, “Magnetic Stirring Tank and Parallel Channel Flow,” Entropy, vol. 11, no. 3, pp. 334–350, 2009.
[18] Z. Driss, S. Karray, W. Chtourou, H. Kchaou and M. S. Abid, “A study of mixing structure in stirred tanks equipped with multiple four-blade Rushton impellers,” The Archive of Mechanical Engineering, vol. 59, no. 1, pp. 53–72, 2012.
[19] Ansys Fluent 13, Theory Guide, Ansys Inc., U.S.A., 2011.
[20] A. Bakker, A new gas dispersion impeller with vertically asymmetric blades, The Online CFM Book, 2000. http://www.bakker.org/cfm
[21] A. B. Metzner and R. E. Otto, “Agitation of non-Newtonian fluids,” AIChE Journal, vol. 3, no. 1, pp. 3-10, 1957.
[22] T. Cebeci and P. Bradshaw, Physical and computational aspects of convective heat transfer, New York: Springer, 1984.
[23] F. Kock and H. Herwig, “Entropy production calculation for turbulent shear flows and their implementation in cfd codes,” International Journal of Heat and Fluid Flow, vol. 26, no. 4, pp. 672–680, 2005.
[24] S.V. Patankar, Numerical heat transfer and fluid flow, Series in Computational Methods in Mechanics and Thermal Sciences, Hemisphere, Washington, DC, 1980.
[25] D. Deglon and C. Meyer, “CFD modeling of stirred tanks: Numerical considerations,” Minerals Engineering, vol. 19, no. 10, pp. 1059–1068, 2006.
[26] R. L. Bates, P. L. Fondy and R. R. Corpstein, “An examination of some geometrical parameters of impeller power,” Industrial & Engineering Chemistry Process Design and Development, vol. 2, no. 4, pp. 310–314, 1963.