| A MULTIPHASE GRAY-SCALE LATTICE BOLTZMANN MODEL |
| Pereira, G.G. (CSIRO
) |
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| A NOVEL DISCRETE PARTICLE MODEL OF BLAST FURNACE IRONMAKING PROCESS |
| Hou, Q.F., E, D.Y., Kuang, S.B., Li, Z.Y. and Yu, A.B. (Laboratory for Simulation and Modelling of Particulate Systems, Monash University) |
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| APPLICATION OF A DISCRETE PHASE MODELLING APPROACH TO INDUSTRIAL SCALE PARTICLE FLOWS |
| Love, A.I.J. (Doosan Boiler R&D Centre) |
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| CFD FLUID FLOW MODELLING IN AMD LIME NEUTRALISATION TANKS: IDENTIFYING THE FLOW CHARACTERISTICS THAT FACILITATE SCALE FORMATION |
| Kenny, E.K., Couperthwaite, S.C. and Millar, G.M. (Queensland University of Technology) |
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| COMPARING THE PERFORMANCE OF A BLACK COAL AND AN UPGRADED BROWN COAL BY BRIQUETTING IN IRONMAKING BLAST FURNACE |
| Liao, J.H., Shen, Y.S., Yu, A.B., Li, Y.T. and Zhu, J.M. (Laboratory for Simulation and Modelling of Particulate Systems,Monash University) |
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| COMPARISON OF A TWO-FLUID MODEL AND AN EULER-LAGRANGE MODEL FOR SIMULATION OF DENSE GAS-FLUIDIZED BEDS |
| Yang, L., Padding, J.T. and Kuipers, J.A.M. (Eindhoven University of Technology) |
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| DIRECT NUMERICAL SIMULATIONS OF FLUID DRAG FORCES OF NON-SPHERICAL PARTICLES |
| Sanjeevi, S.K.P., Padding, J.T. and Kuipers, J.A.M. (Technical University of Eindhoven) |
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| DISCRETE ELEMENT MODELING OF PARTICLE FLOW BEHAVIORS IN A GAS-SOLID BUBBLING FLUIDIZED BED USING DYNAMIC RESTITUTION COEFFICIENT |
| Liu, G.L., Yu, F., Lu, H.L., Wang, S., Sun, L.Y. and Zhang, Y.N. (Harbin Institute of Technology) |
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| EFFECT OF OPERATING PRESSURE ON PARTICLE TEMPERATURE DISTRIBUTION IN A FLUIDIZED BED WITH HEAT PRODUCTION |
| Li, Z., van Sint Annaland, M. and Kuipers, J.A.M. (Eindhoven University of Technology; Dutch Polymer Institute (DPI)) |
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| GAS - LIQUID FLOW IN WET ELECTROSTATIC PRECIPITATORS |
| Guo, B.Y., Su, Y.B., Yang, D. and Yu, A.B. (University of New South Wales) |
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| BUBBLE-EMULSION HEAT TRANSFER COEFFICIENT IN GAS-SOLID FLUIDIZED BED USING TWO FLUID MODEL |
| Banaei, M., van Sint Annaland, M., Kuipers, J.A.M. and Deen, N.G. (Eindhoven University of Technology; Dutch Polymer Institute (DPI)) |
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| MASS TRANSFER PHENOMENA IN FLUIDIZED BEDS WITH VERTICALLY AND HORIZONTALLY IMMERSED MEMBRANES
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| Voncken, R.J.W., Roghair, I., Gallucci, F. and van Sint Annaland, M. (Eindhoven University of Technology) |
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| NUMERICAL AND EXPERIMENTAL CHARACTERIZATION OF PARTICLE CLUSTERS IN RISER FLOW |
| Varas, C.A.E., Peters, E.A.J., Deen, N.G. and Kuipers, J.A.M. (Eindhoven University of Technology) |
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| NUMERICAL VALIDATION OF THE EISFELD AND SCHNITZLEIN PRESSURE DROP CORRELATION FOR SMALL ASPECT RATIO PACKED BEDS |
| Kruger, J.H., Du Toit, C.G. and Van der Merwe, W.J.S. (North-West University, South Africa) |
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| OPEN SOURCE CFD-DEM MODELLING FOR PARTICLE-BASED PROCESSES |
| Goniva, C.G., Blais, B.B., Radl, S.R. and Kloss, C.K. (DCS Computing GmbH, Linz, AUSTRIA) |
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| OPERATING PARAMETER EFFECTS ON THE SOLID CIRCULATION RATE IN A DUAL FLUIDIZED-BED GASIFICATION SYSTEM |
| Liu, H.L., Cattolica, R.J.C. and Seiser, R.S. (University of California San Diego) |
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| PRELIMINARY CFD STUDIES OF A CONTINUOUS INDUSTRIAL SCALE FLUIDIZED BED ROASTER |
| Dash, S., Soni, R.K., Mohanty, S. and Mishra, B.K. (CSIR-Institute of Minerals and Material Technology) |
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| QUALITATIVE ASSESSMENT OF BUBBLE BEHAVIOUR FOR CENTRAL AND ASYMMETRIC INJECTION IN 2D GAS-SOLID FLUIDIZED BED USING IMAGE ANALYSIS TECHINIQUE AND CFD MODELLING
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| Kumar, V., Das, S., Kumar, A., Fabijanic, D. and Hodgson, P. (Institute of Frontier Materials, Deakin University) |
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| STUDY OF PARTICLE ROTATION IN PSEUDO 2D FLUIDIZED BEDS |
| Buist, K.A., Yang, L., Deen, N.G., Padding, J.T. and Kuipers, J.A.M. (Eindhoven University of Technology) |
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| THE NETL MFIX SUITE OF MULTIPHASE FLOW MODELS: APPLICATIONS TO FOSSIL ENERGY TECHNOLOGIES |
| Rogers, W.A.R., Syamlal, M.S., Dietiker, J.D., Li, T.L., Musser, J.M. and Shahnam, M.S. (U.S. Department of Energy, NETL) |
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| TRANSIENT SIMULATION OF ACCUMULATING PARTICLE DEPOSITION ON A CYLINDER IN CROSS-FLOW |
| Hewett, J.N. and Sellier, M. (Department of Mechanical Engineering, University of Canterbury) |
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CFD