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A four-zone drag model based on cluster for simulating gas-solids flow in turbulent fluidized beds

机译:基于集群的四区拖曳模型,用于模拟湍流流化床中的气固流量

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摘要

Gas-solids drag model is crucial for the accurate prediction of gas-solids flow in turbulent fluidized bed (TFB). A four-zone drag model based on cluster was proposed to describe the gas-solids interactions in TFB. The model considers the cluster effect in the bottom dense bubbling zone while regards the particles as discrete ones in the top dilute dispersed zone. The structural parameter model was used to calculate the equivalent cluster diameter in the drag model. Validations against experiments show that the drag model can accurately simulate the gas-solids flow characteristics in TFBs with Geldart A and B particles. Besides, the non-uniform flow structures resulting from gas voids and particle clusters were successfully captured with the model. Compared with the bubbling fluidized bed, more small bubbles with a more uniform size distribution exist in TFB and the variation of operating conditions has little effect on gas voids characteristics in TFB.
机译:气固阻力模型对于湍流流化床(TFB)中的气固流动精确预测是至关重要的。 提出了一种基于集群的四区拖曳模型来描述TFB中的气体固体相互作用。 该模型考虑底部致气泡中的簇效应,同时将颗粒视为顶部稀释分散区中的离散区域。 结构参数模型用于计算拖动模型中的等效簇直径。 对实验的验证表明,拖曳模型可以用Geldart A和B颗粒准确地模拟TFB中的气体固体流动特性。 此外,用模型成功捕获由气体空隙和颗粒簇产生的不均匀流动结构。 与鼓泡流化床相比,TFB中存在具有更均匀尺寸分布的更小的气泡,并且操作条件的变化对TFB中的气体空隙特性几乎没有影响。

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