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CFD Simulation on Gas-Liquid Hydrodynamics in a Dual-Impeller Stirred Reactor

机译:双叶轮搅拌反应器中气液流体动力学的CFD模拟

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Multiphase mixtures occur very frequently in process industries. The paper deals with the study of liquid and gas flow behavior in a gas sparged tank equipped with multiple impellers, i.e. combination of Rushton turbine and upflow pitched-blade turbine. Single-phase flow is investigatedrnusing Laser Doppler Velocimetry (LDV) and computational fluid dynamics (CFD). Gas - liquidrnhydrodynamics are simulated with three-dimensional CFD model, in which a multiple frames of reference method is used to account for the relative movement between impeller and baffles. Fluid flow is calculated with a two-fluid model along with standard k-ε turbulence model using finite-volume method. The velocity distribution for single phase in mixing tanks measured by LDV is used to validate the results of CFD. The simulation results for gas-liquid flow are compared with other available experimental data. In addition, two alternative drag coefficient approaches are tested for studying their influence on gas-liquid hydrodynamics. Further work is needed to improve the quantitative agreement with experimental data.
机译:在过程工业中,多相混合物经常发生。本文研究了在装有多个叶轮的气体鼓风罐(即Rushton涡轮和上流斜叶涡轮的组合)中的液体和气体流动行为的研究。利用激光多普勒测速(LDV)和计算流体动力学(CFD)研究了单相流。用三维CFD模型模拟了气液流体动力学,其中使用了多个参考框架来解释叶轮和挡板之间的相对运动。使用有限体积方法,使用双流体模型和标准k-ε湍流模型计算流体流量。通过LDV测量的混合罐中单相的速度分布用于验证CFD结果。气液流动的模拟结果与其他可用的实验数据进行了比较。此外,还测试了两种替代的阻力系数方法,以研究它们对气液流体动力学的影响。需要做进一步的工作来改善与实验数据的定量一致性。

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