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首页> 外文期刊>Chemical Engineering & Technology: Industrial Chemistry -Plant Equipment -Process Engineering -Biotechnology >Effect of Drag Models on the Numerical Simulations of Bubbling and Turbulent Fluidized Beds
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Effect of Drag Models on the Numerical Simulations of Bubbling and Turbulent Fluidized Beds

机译:影响阻力模型的数值模拟冒泡和湍流流化床

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摘要

Granular option enabled two-fluid model coupled with different homogeneous and heterogeneous drag correlations,i.e.,Gidaspow,Syamlal and O'Brien,Beetstra,Brucato,Gibilaro,energy minimization multiscale method(EMMS),and Tenneti,are employed for the prediction of bubbling and turbulent fluidized-bed characteristics.Numerically predicted results are validated against the literature data in terms of bubble shape and diameter,axial and radial variation of timeaveraged void fraction,pressure drop,and bed expansion.The Gidaspow,Syamlal and O'Brien drag model-predicted mean void fraction and bubble shapes are close to the experiments in bubbling and turbulent fluidized beds with both the 2D and 3D geometries.All drag models overpredicted the pressure drop at low superficial gas velocities in a turbulent fluidized bed.
机译:细粒度的选择启用双流体模型耦合与不同的同类和异类阻力相关性,即。最小化多尺度方法(EMMS)Tenneti,用于预测冒泡和湍流流化床特征。根据文献数据进行验证的泡沫形状和直径,轴向和径向变化timeaveraged空隙率、压力下降,和床上扩张。O ' brien阻力模型预测平均空隙率和泡沫形状接近于实验冒泡和湍流流化床2 d和3 d几何图形。overpredicted低的压降表面的气体湍流速度流化床。

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