工业级脉冲折流板萃取柱CFD模拟研究

CFD Simulation of Pulsed Disc and Doughnut Solvent Extraction Column on Industrial Grade

  • 摘要: 以工业级脉冲折流板萃取柱为研究对象,建立了液液两相流体CFD数学模型,利用CFD模型研究了分散相持液量、轴向扩散、湍流耗散率以及板间距对萃取柱的影响。结果表明:CFD模型预测的持液量与实验所测结果吻合良好,所建立的CFD模型有效,且CFD模型的持液量较经验公式预测结果更为准确。萃取柱轴向扩散系数随脉冲强度的增大而增大,在工程应用中脉冲强度不易过高。同时相比于分散相速度,连续相速度对轴向扩散系数的影响更大。利用CFD模型对Kummar提出的湍流耗散率经验公式常数进行了修正,常数修正为0.81,从而提高了计算结果的准确性。最后对比了不同板间距萃取柱水力学计算结果,发现萃取柱在工程设计时选取50 mm板间距更为合理。

     

    Abstract: A CFD mathematical model was established for an industrial pulsed disc and doughnut extraction column. The effects of liquid holdup, axial diffusion, turbulent energy dissipation rate and plate spacing on the extraction column were studied by using the CFD model. The results show that the predicted liquid holdup of CFD model is in good agreement with the experimental results, and the established CFD model is effective. Compared with the empirical formula, the predicted liquid holdup of CFD model is more accurate. The axial diffusion coefficient of the extraction column increases with the pulse intensity, so the pulse intensity is not easy to be too high in engineering application. At the same time, the velocity of continuous phase has more effect on the axial diffusion coefficient than that of dispersed phase. The empirical formula constant of turbulent energy dissipation rate proposed by Kummar was corrected by CFD model, and the correction constant is 0.81, which improves the accuracy of calculation results. Finally, by comparing the hydraulic calculation results of extraction column with different plate spacing, it is more reasonable to select 50 mm plate spacing for engineering design.

     

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