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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Effects of turbulence modeling on the prediction of flow characteristics of mixing non-Newtonian fluids in a stirred vessel
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Effects of turbulence modeling on the prediction of flow characteristics of mixing non-Newtonian fluids in a stirred vessel

机译:湍流建模对搅拌容器混合非牛顿液体流动特性预测的影响

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摘要

Mixing characteristics of the non-Newtonian fluid in a stirred vessel with a side-entry novel propeller was investigated by using computational fluid dynamics (CFD). The SST model (SST), standard k-omega (SKO), Reynold stress model (RSM), standard k-epsilon (SKE), Realizable k-epsilon (KER), RNG k-epsilon (RNG) were evaluated for nine generalized Reynolds numbers operating at different flow conditions. In order to determine the estimated trait generalized Reynolds number at the end of the laminar regime, both the laminar and turbulent model simulations were conducted. Those results were validated with the published literature experimental results and different simulated results. By comparing the simulated and experimental literature results, the SST and RSM models are found to be more accurate than the other four turbulence models in predicting the torque. The power consumption and power numbers curves calculated from the SST and RSM models are highly consistent with the experimental results. To verify the effect of the applied turbulence models on predictive accuracy, both the velocity field, streamlines distributions, and the velocity profiles are evaluated. The RSM model was found to be more realizable for capturing mixing behavior in lower concentration solutions and with lower rotation speeds. However, this model has some drawbacks for modeling stirred vessels, such as a large number of modeled revolutions and mesh statistical required to obtain good quantities. In contrasts with the RSM model, the SST model is more reliable to predict velocity profiles and flow patterns in higher concentration solutions, especially in the near wall region. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:采用计算流体动力学(CFD)研究了具有侧进入新型螺旋桨的搅拌容器中的非牛顿流体的混合特性。 SST模型(SST),标准K-OMEGA(SKO),雷诺应力模型(RSM),标准K-EPSILON(SKE),可实现的K-EPSILON(KER),RNG K-EPSILON(RNG)被九广泛化Reynolds数字在不同的流动条件下运行。为了确定层状区域末端的估计性状雷诺数,进行了层流和湍流模拟模拟。这些结果与发表的文献实验结果和不同的模拟结果验证。通过比较模拟和实验文献结果,发现SST和RSM模型比预测扭矩的其他四种湍流模型更准确。从SST和RSM模型计算的功耗和功率编号曲线与实验结果非常一致。为了验证所应用的湍流模型对预测精度的影响,评估速度场,流线分布和速度分布。发现RSM模型更加可实现,以便在较低浓度的解决方案中捕获混合行为并具有较低的旋转速度。然而,该模型具有用于建模搅拌血管的缺点,例如大量建模转的转速和网眼统计以获得良好的数量。相反,与RSM模型相比,SST模型更可靠地预测较高浓度解决方案中的速度分布和流动模式,特别是在近壁区域。 (c)2019化学工程师机构。 elsevier b.v出版。保留所有权利。

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