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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >A CFD study of a bi-disperse gas-solid fluidized bed: Effect of the EMMS sub grid drag correction
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A CFD study of a bi-disperse gas-solid fluidized bed: Effect of the EMMS sub grid drag correction

机译:双分散气固流化床的CFD研究:EMMS子网格阻力修正的影响

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摘要

For the first time the bubble-based EMMS drag model developed for a mono-disperse system has been extended to simulate a bi-disperse fluidized bed in conjunction with the multi-fluid model. Simulations with the EMMS drag model reveal that the system attains a fluidized state earlier. Furthermore the model predicts bed height and voidage in better agreement with data from the literature. Inclusion of the sub-grid drag correction is found to have a significant effect on the predicted axial pressure drop profile, mixing and segregation behavior, granular temperatures and turbulent kinetic energy. The effect of the specularity coefficient on the mixing index is also investigated. (C) 2015 Elsevier B.V. All rights reserved.
机译:第一次扩展了为单分散系统开发的基于气泡​​的EMMS阻力模型,以结合多流体模型来模拟双分散流化床。用EMMS阻力模型进行的仿真表明,系统较早达到了流化状态。此外,该模型预测床高和空隙与文献数据更好地吻合。发现包括次网格阻力校正对预测的轴向压降分布,混合和偏析行为,颗粒温度和湍动能具有重大影响。还研究了镜面反射系数对混合指数的影响。 (C)2015 Elsevier B.V.保留所有权利。

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