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CFD simulations of bubble column reactors: 1D, 2D and 3D approach

机译:鼓泡塔反应器的CFD模拟:1D,2D和3D方法

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CFD simulations have been carried out for the predictions of flow pattern in bubble column reactors using 1D, 2D and 3D k-epsilon models. An attempt has been made to develop a complete correspondence between the operation of a real column and the simulation. Attention has been focused on the cylindrical bubble columns because of their widespread applications in the industry. All the models showed good agreement with the experimental data for axial liquid velocity and the fractional gas hold-up profiles. However, as regards to eddy diffusivity, only the 3D model predictions agree closely with the experimental data.The CFD model has been extended for the estimation of an axial dispersion coefficient (D-L) using I D, 2D and 3D models. Excellent agreement was found only between the experimental values and the 3D predictions. The 1D and 2D simulations, however, yielded DL values, which were lower by 25-50%. For this, a mechanistic explanation has been provided. (c) 2005 Elsevier Ltd. All rights reserved.
机译:已经使用1D,2D和3Dk-ε模型对CFD模拟进行了气泡塔反应器中流动模式的预测。已经尝试在真实列的操作和模拟之间建立完整的对应关系。由于圆筒形气泡塔在工业上的广泛应用,因此已经引起了人们的关注。所有模型均与轴向液体速度和分数气体滞留曲线的实验数据显示出良好的一致性。然而,关于涡流扩散率,只有3D模型的预测与实验数据非常吻合.CFD模型已扩展为使用I D,2D和3D模型估算轴向弥散系数(D-L)。仅在实验值和3D预测之间找到了极好的一致性。但是,一维和二维模拟得出的DL值降低了25%至50%。为此,提供了机械的解释。 (c)2005 Elsevier Ltd.保留所有权利。

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