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Comparison of mixing efficiency of different impellers for agitation of slurry in anaerobic digester

机译:不同叶轮混合效率对厌氧消化器浆液搅拌的搅拌效率

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Adequate mixing is one of prominent factors which can enhance the biogas production. Uniform distribution of velocity and viscosity at lower impeller speeds is biggest challenge. Correspondingly, in this study CFD simulations of Rushton turbine, anchor impeller and disc mixer were carried out using SC tetra program. The rotational speed of the mixers was kept between 40 to 100 rpm. The average velocity of the slurry particles in case of Rushton turbine, anchor impeller and disc impeller were noted as 0.054, 0.091 and 0.14 ms~(-1) respectively. The results demonstrated that the disc mixer performed best as compared to other impellers in terms of better distribution of velocity and lesser number of dead zones. Lower mixing intensities are best to enhance biogas production rates in actual experiments by using appropriate impeller geometry and lower rpm.
机译:足够的混合是可以增强沼气生产的突出因素之一。 较低叶轮速度下的速度和粘度的均匀分布是最大的挑战。 相应地,在本研究中,使用SC Tetra程序进行Rushton涡轮机,锚叶轮和盘混合器的CFD模拟。 混合器的转速保持在40至100rpm之间。 拉什腾涡轮机,锚叶轮和盘叶轮的情况下,浆料颗粒的平均速度分别指出为0.054,0.091和0.14ms〜(-1)。 结果表明,与更好的速度分布和较少的死区的分布相比,光盘混合器与其他叶轮相比表现最佳。 通过使用适当的叶轮几何形状和较低的RPM,较低的混合强度最好提高实际实验中的沼气生产率。

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