首页> 外文会议>China-Japan Symposium on Fluidization; 20061218-20; Beijing(CN) >CFD Simulation of Bed Collapse in 3D Fluidized Beds
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CFD Simulation of Bed Collapse in 3D Fluidized Beds

机译:3D流化床中床崩塌的CFD模拟

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Multiphase Computational Fluid Dynamics (CFD) has become an alternative method to experiments for understanding the fluid dynamics in gas-solid fluidized beds. A two-fluid model, which contains additional terms in both the gas- and solid-phase momentum balances, is employed to investigate the bed collapse process in three-dimensional beds. In this model, only a correlation for drag force is necessary to close the governing equations. Transient calculations have been made in the platform of CFX 4.4 by adding User-defined Fortran subroutines. A case study for sand with a density of 2500 kg/m~3 and a mean diameter of 610 urn, belonging to Geldart B classification, is simulated in a rectangular duct of 0.2 m (long) × 0.2 m (wide) × 0.5 m (high). The collapse process is numerically analyzed by considering the standard deviation of the surface between the dense phase and freeboard, which is generally in fair agreement with the classic theory of Geldart.
机译:多相计算流体动力学(CFD)已成为用于理解气固流化床中流体动力学的实验的替代方法。采用二维流体模型,该模型在气相和固相动量平衡中均包含其他项,用于研究三维床中的床塌陷过程。在该模型中,仅需与阻力相关即可关闭控制方程。通过添加用户定义的Fortran子例程,在CFX 4.4平台中进行了瞬态计算。以0.2 m(长)×0.2 m(宽)×0.5 m的矩形风管为例,模拟了属于Geldart B分类的密度为2500 kg / m〜3且平均直径为610 urn的沙子(高)。考虑致密相和干舷之间的表面标准偏差,对塌陷过程进行了数值分析,这与格尔德经典理论基本吻合。

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