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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received January 26, 2009
Accepted March 5, 2009
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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CFD simulation of gas-solid bubbling fluidized bed containing FCC particles

Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan 98164-161, Iran
hosseini@mail.usb.ac.ir
Korean Journal of Chemical Engineering, September 2009, 26(5), 1405-1413(9), 10.1007/s11814-009-0220-9
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Abstract

The hydrodynamics of a bubbling gas-solid fluidized bed of 57.4 μm FCC particles was simulated by using a state-of-the-art two-fluid model integrating the kinetic theory of granular flow for particulate phase stresses. The overestimation of the bed expansion was resolved by using a suitable scale factor in the drag model as suggested by McKeen and Pugsley (T.R. McKeen, T.S. Pugsley, Powder Technol., 129, 139 (2003)). This study showed that the method was_x000D_ appropriate in simulation of a gas-solid fluidized bed of Geldart A particles at high gas velocities (0.3 to 0.61 m/s). The reduction of computational time especially for simulation of large-scale systems was achieved. The time-averaged local voidage was compared with the experimental data and the trend of varying several parameters on the hydrodynamic of the bed was investigated. The simulation results showed both qualitative and quantitative agreement with the literature.

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