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首页> 外文期刊>International Journal of Agricultural and Biological Engineering >Numerical simulation and experimental study on eggshell membrane separation device
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Numerical simulation and experimental study on eggshell membrane separation device

机译:蛋壳膜分离装置的数值模拟与实验研究

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In order to provide theoretical guidance for separating egg membrane from eggshell by using mechanical agitation, CFD was used to explore the flow characteristics in stirred tank, using the Sliding Grid method to deal with the impeller rotational velocity zone in flow field, and using the Euler model to deal with liquid-solid two-phase flow. This study explored the influence of dish-shape bottom or flat-shape bottom, the clearance size between baffle and the side wall, and the axial height of impeller to bottom on suspension state of particles, solids holdup distribution, solid phase velocity and power number by CFD. Simulation results showed that better particles suspension effect in dish-shape tank can reduce particles accumulation at the bottom and power consumption. If there was a small clearance size (S) between the baffle and the side wall of the stirred tank, it would reduce particles accumulation at the bottom, and reduce the power consumption. However, too large S would decrease the suspension height of particles, not only cannot strengthen the main flow, but also lead to most fluid through clearance forming tangential flow, simulation results showed that S=6 mm was perfect. While decreased axial height of impeller (C) to bottom, particles accumulation at the bottom was decreased, but power consumption would increase, simulation results showed that C=H/5 (H is height of liquid surface) was perfect. According to the simulation results, the structure of the stirring tank was optimized. At the same time, the influences of stirring rotational velocity, stirring time, solid-liquid ratio and separating medium temperature on egg membrane recovery were also studied by experiment, and optimal parameter combination of factors was obtained. The experiment results showed while the stirring time was 17.1 min, stirring rotational velocity was 350 r/min, solid-liquid ratio was 1:17 g/mL, the separating medium temperature was 32°C, the membrane recovery rate can reach above 89%. The device improves the recovery and utilization of discarded eggshell, and provides a reference for the solid-liquid two-phase flow and related study.
机译:为了为通过机械搅拌将蛋膜从蛋壳中分离提供理论指导,使用CFD探索搅拌槽中的流动特性,使用滑动网格法处理流场中的叶轮转速区域,并使用Euler模型处理液固两相流。本研究探讨了碟形底部或平板形底部,挡板与侧壁之间的间隙尺寸以及叶轮到底部的轴向高度对颗粒悬浮状态,固含率分布,固相速度和功率数的影响。通过差价合约。仿真结果表明,在碟形罐中更好的颗粒悬浮效果可以减少底部的颗粒积聚和功耗。如果挡板和搅拌槽的侧壁之间的间隙尺寸(S)小,则会减少颗粒在底部的积聚,并降低功耗。然而,太大的S会降低颗粒的悬浮高度,不仅不能增强主流,而且会导致大部分流体通过间隙形成切向流,模拟结果表明S = 6 mm是理想的。当叶轮(C)到底部的轴向高度减小时,底部的颗粒积聚减少,但功耗会增加,模拟结果表明C = H / 5(H是液面高度)是理想的。根据仿真结果,优化了搅拌槽的结构。同时,通过实验研究了搅拌转速,搅拌时间,固液比和分离介质温度对蛋膜回收率的影响,获得了各因素的最优参数组合。实验结果表明,搅拌时间为17.1 min,搅拌转速为350 r / min,固液比为1:17 g / mL,分离介质温度为32°C,膜回收率可达89以上。 %。该装置提高了废弃蛋壳的回收利用效率,为固液两相流及相关研究提供参考。

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