References
- ASME shale shaker committee, Drilling fluids processing handbook.
- CD-adapco, 2014, User guide STAR-CCM+ Version 9.02.
- Darelius, A., Rasmuson, A., vanWachem, B., Bjorn, I.N. and Folestad, S., 2008, CFD simulation of the high shear mixing process using kinetic theory of granular flowand frictional stress models. Chem. Eng. Sci., 63(8), 2188-2197. https://doi.org/10.1016/j.ces.2008.01.018
- DING, J. and Gidaspow, G., 1990, A bubbling fluidisation model using kinetic theory of granular flow. AIChE Journal, 36(4), 523-538. https://doi.org/10.1002/aic.690360404
- Eesa, M., 2009, CFD studies of complex fluid flows in pipes. Ph.D. thesis, The university of Birmingham.
- Ekambara, K., Sean Sanders, R., Nandakumar, K. and Masliyah, J.H., 2009, Hydrodynamic Simulation of Horizontal Slurry Pipeline Flow Using ANSYS-CFX. Ind. Eng. Chem. Res., 48, 8159-8171. https://doi.org/10.1021/ie801505z
- Gidaspow D., 1994, Multiphase Flow and Fluidization - Continuum and Kinetic Theory Descriptions. Academic Press.
- Gillies, R.G. and Shook, C.A., 2000, Modelling High Concentration Slurry Flows. Can. J. Chem. Eng., 78, 709-716. https://doi.org/10.1002/cjce.5450780413
- Gillies, R.G., Shook, C.A., Xu, J., 2004, Modelling Heterogeneous SlurryFlows at High Velocities. Can. J. Chem. Eng., 82, 1060- 1065.
- Guida, A., Fan, X., Parker, D.J., Nienow, A.W. and Barugou, M., 2009, Positron emission particle tracking in a mechanically agitated solid-liquid suspension of coarse particles. IChemE, 87, 421-429. https://doi.org/10.1016/j.cherd.2008.12.001
- Guida, A., 2010, Positron emixxion particle tracking applied to solid-liquid mixing in mechanically agitated vessels, Ph.D. thesis, The university of Birmingham.
- Kaushal, D.R. and Tomita, Y., 2012, Experimental Investigation of Near-Wall Lift of Coarser Particles in Slurry Pipeline Using Gamma-ray Densitometer. Powder Technol., 172, 177-187.
- Kim, G.S., 2012, Eulerian-Granular model. STAR Korean conference 2012, Busan, Korea.
- Kim, H.J., 2012, Multiphase modelling in STAR-CCM+, STAR Korean conference 2012, Busan, Korea.
- Krampa, F.N., 2009, Two-fluid modeling of heterogeneous coarse particle slurry flows. Ph.D. thesis, The university of saskatchewan.
- Kubicki, D., and Lo, S., 2012, Slurry transport in a pipeline - Comparison of CFD and DEM models. 9th international conference on CFD in the minerals and process industires, CSIRO, Melbourne, Australia.
- Lo, S. 2012, Multiphase flow models in STAR-CCM+. STAR Japanese conference 2012, Tokyo, Japan.
- Lo, S. and Kubicki, D., 2012, Modeling industrial multiphase flows with STAR-CCM+. STAR global conference 2012, Duin, Netherlands.
- Papoulias, D. and Lo, S. 2015, Advances in CFD modelling of multiphase flows in cyclone seperators. Chemical Engineering Transaction, 43, 1603-1608.
- Roco, M.C. and Shook, C.A., 1983, Modeling of Slurry Flow: The Effect of Particle Size. Can. J. Chem. Eng., 61, 494-503.
- Schaan, J., Sumner, R.J., Gillies, R.G. and Shook, C.A., 2000, The Effect of Particle Shape on Pipeline Friction for Newtonian Slurries of Fine Particles. Can. J. Chem. Eng., 78, 717-725. https://doi.org/10.1002/cjce.5450780414
- Schiller, L., and Naumann, A., 1933, Uber die grundlegenden Berechnungen bei der Schwerkraftaufbereitung, VDI Zeits, 77(12), pp. 318-320.
- Syamlal, M. and O'Brien, T.J., 1987, The derivation of a drag coefficient formula from velocity-voidage correlations. Technical Note, U.S. Department of energy, Office of Fossil Energy, NETL, Morgantown, WV.
- Tong, L.Z., Chare K., Asa, F. and Sugiura, Y., 2010, CFD analysis of eductor agitation in electroplating tank. Trans. Inst. Met. Finish., 88(4), 185-190. https://doi.org/10.1179/002029610X12694310989008
- Zhang, J., Xu, S. and Li, W., 2012, High shear mixers: A review of typical applications and studies on power draw, flow pattern, energy dissipation and transfer properties. Chem. Eng. Process., 57-58, 25-41.
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