Cartesian grid simulations of bubbling fluidized beds with a horizontal tube bundle |
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Authors: | Tingwen Li,Jean-Franç ois Dietiker,Yongmin Zhang,Mehrdad Shahnam |
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Affiliation: | aNational Energy Technology Laboratory, Department of Energy, Morgantown, WV 26505, USA;bURS Corp., Morgantown, WV 26505, USA;cWest Virginia University Research Corporation, Morgantown, WV 26506, USA;dState Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China |
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Abstract: | In this paper, the flow hydrodynamics in a bubbling fluidized bed with submerged horizontal tube bundle was numerically investigated with an open-source code: Multiphase Flow with Interphase eXchange (MFIX). A newly implemented cut-cell technique was employed to deal with the curved surface of submerged tubes. A series of 2D simulations were conducted to study the effects of gas velocity and tube arrangement on the flow pattern. Hydrodynamic heterogeneities on voidage, particle velocity, bubble fraction, and frequency near the tube circumferential surface were successfully predicted by this numerical method, which agrees qualitatively with previous experimental findings and contributes to a sounder understanding of the non-uniform heat transfer and erosion around a horizontal tube. A 3D simulation was also conducted. Significant differences between 2D and 3D simulations were observed with respect to bed expansion, bubble distribution, voidage, and solids velocity profiles. Hence, the 3D simulation is needed for quantitative prediction of flow hydrodynamics. On the other hand, the flow characteristics and bubble behavior at the tube surface are similar under both 2D and 3D simulations as far as the bubble frequency and bubble phase fraction are concerned. Comparison with experimental data showed that qualitative agreement was obtained in both 2D and 3D simulations for the bubble characteristics at the tube surface. |
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Keywords: | CFD Tube bundle Fluidized beds Gas&ndash solids flow Hydrodynamics Erosion |
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