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Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analysesud

机译:用于流化分析的无量纲化和三维流态图 ud

摘要

This article is on the dimensional analysis and the classification of fluidization from the viewpoint of numerical analysis. At first, the governing equations used in the DEM (Discrete Element Method) and CFD (Computational Fluid Dynamics) coupling model was non-dimensionalized with the method of Hellums and Churchill (1964). From the resulting dimensionless equations, it was concluded that the five dimensionless numbers, i.e. Re: Reynolds number, Ar: Archimedes number, Ga: Galilei number, Fr: Froude number and �*: ratio of particle density divided by fluid density, can be derived and hydrodynamically dominant on the fluid behaviors. Further, these can illustrate the dimensionless numbers proposed in the previous studies. Secondary, a three-dimensional flow regime map of homogeneous, bubbling and turbulent fluidizations was proposed with these dimensionless numbers using the DEM-CFD simulations. Finally, the plane of the minimum bubbling fluidization velocity umb in the map can be proposed and expressed as,�Re�_mb=0.263�^(*-0.553) �Ar�^0.612. umb can be estimated using this equation for various conditions.ud
机译:本文从数值分析的角度对流态化进行了尺寸分析和分类。首先,使用Hellums和Churchill(1964)的方法对DEM(离散元法)和CFD(计算流体动力学)耦合模型中使用的控制方程进行了无量纲化处理。根据产生的无量纲方程,可以得出以下五个无量纲数,即Re:雷诺数,Ar:阿基米德数,Ga:伽利略数,Fr:弗洛德数和**:颗粒密度除以流体密度的比率,可以推导流体力学行为,并在流体力学上占主导地位。此外,这些可以说明先前研究中提出的无量纲数。其次,使用DEM-CFD模拟,利用这些无量纲数,提出了均质,起泡和湍流化的三维流态图。最终,可以提出图中最小起泡流化速度umb的平面并将其表示为ReReRe_mb =0.263Ï(*-0.553)Arã^ 0.612。可以使用此公式针对各种条件估算umb。 ud

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