Two-phase (water and air) flow in the forced-air mechanically-stirred Dorr-Oliver machine has been investigated using computational fluid dynamics (CFD). A 6 m 3 model is considered. The flow is modeled by the Euler-Euler approach, and transport equations are solved using software ANSYS-CFX5. Unsteady simulations are conducted in a 180-degree sector with periodic boundary conditions. Air is injected into the rotor at the rate of 2.63 m 3/min, and a uniform bubble diameter is specified. The effects of bubble diameter on velocity field and air volume fraction are determined by conducting simulations for three diameters of 0.5, 1.0, and 2.0 mm. Air volume fraction contours, velocity profiles, and turbulent kinetic energy profiles in different parts of the machine are presented and discussed. Results have been compared to experimental data, and good agreement is obtained for the mean velocity and turbulent kinetic energy profiles in the rotor-stator gap and in the jet region outside stator blades.
References
[1]
Salem-Said, A.; Fayed, H.; Ragab, S. CFD Simulation of a Dorr-Oliver Flotation Cell. In Proceedings of the SME Annual Meeting and Exhibit, Denver, CO, USA, 28 February–2 March 2011.
[2]
Fayed, H.; Ragab, S. CFD Analysis of Two-Phase Flow in a Self Aerated Flotation Machine. In Proceedings of the SME Annual Meeting and Exhibit, Seattle, WA, USA, 19–22 February 2012.
[3]
Ragab, S.; Fayed, H. CFD-Based Flotation Model for Prediction of Pulp Recovery Rate. In Proceedings of the SME Annual Meeting and Exhibit, Seattle, WA, USA, 19–22 February 2012.
[4]
Fayed, H.; Ragab, S. CFD Analysis of Two-Phase Flow in WEMCO 300 m3 Supercell. In Proceedings of the SME Annual Meeting and Exhibit, Denver, CO, USA, 24–27 February 2013.
[5]
Koh, P.T.L.; Schwarz, P.; Zhu, Y.; Bourke, P. Development of CFD Models of Mineral Flotation Cells. In Proceedings of the 3rd International Conference on CFD in the Minerals and Process Industries, Melborne, Australia, 10–12 December 2003; pp. 171–175.
[6]
Tiitinen, J.; Koskinen, K.; Ronkainen, S. Numerical Modeling of an Outokumpu Flotation Cell. In Proceedings of the Centenary of Flotation Symposium, Brisbane, Australia, 6–9 June 2005.
[7]
Koh, P.T.L.; Schwarz, M.P. CFD modeling of bubble-particle attachments in flotation cells. Miner. Eng. 2006, 19, 619–626, doi:10.1016/j.mineng.2005.09.013.
[8]
Koh, P.T.L.; Schwarz, M.P. CFD model of a self-aerating flotation cell. Int. J. Miner. Process. 2007, 85, 16–24, doi:10.1016/j.minpro.2007.08.006.
[9]
Evans, G.; Doroodchi, E.; Lane, G.; Koh, P.; Schwarz, P. Mixing and Gas Dispersion in Mineral Flotation Cells. In Proceedings of the 6th International Symposium on Mixing Industrial Process Industries (ISMIP VI), Niagara on the Lake, Canada, 17–21 August 2008.
[10]
Koh, P.T.L.; Schwarz, M.P. Models of Microcell and Jameson Flotation Cells. In Proceedings of the 7th International Conference on CFD in the Minerals and Process Industries, Melbourne, Australia, 9–11 December 2009.
[11]
Kerdouss, F.; Bannari, A.; Proulx, P. CFD modeling of gas dispersion and bubble size in a double turbine stirred tank. Chem. Eng. Sci. 2006, 61, 3313–3322, doi:10.1016/j.ces.2005.11.061.
[12]
Prosperetti, A.; Tryggvason, G. Computational Methods for Multiphase Flow; Cambridge University Press: Cambridge, UK, 2007.
[13]
Van den Akker, H.E.A. Toward a truly multiscale computational strategy for simulating turbulent two-phase flow processes. Ind. Eng. Chem. Res. 2010, 49, 10780–10797, doi:10.1021/ie1006382.
[14]
Clift, R.; Grace, J.R.; Weber, M.E. Bubbles, Drops and Particles; Dover Publications: Mineola, NY, USA, 2005.
[15]
Yang, Y.; Telionis, D. Turbulence Measurements in a Flotation Cell Using Fast-Response Probe. In Proceedings of the 2011 SME Annual Meeting, Denver, CO, USA, 28 February–2 March 2011.
[16]
Yang, Y. Experimental Study of Multi-Phase Flow Hydrodynamics in Stirring Tanks. Ph.D. Thesis, Virginia Tech, Blacksburg, VA, USA, 4 February 2011.