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CFD simulation of jet behaviour and voidage profile in a gas-solid fluidized bed

机译:气固流化床中射流行为和空隙率分布的CFD模拟

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摘要

Based on an Eulerian-Eulerian approach, a computational fluid dynamic (CFD) model for gas-solid system has been developed to investigate the hydrodynamics in fluidized beds. With this model, jet penetration height, jet frequency, time-averaged axial gas velocity profile, and time-averaged voidage profile have been simulated in a two-dimensional bed. The computational results indicate that the jet penetration height increases with increasing the jet gas velocity. The jet frequency decreases with increasing the jet gas velocity and decreasing particle diameter. The time-averaged axial gas velocity profile becomes 'lower' and 'wider' and the time-averaged voidage decreases with increasing distance from the jet nozzle. These conclusions appear in good agreement with the experimental and simulated data in the literature.
机译:基于欧拉-欧拉方法,开发了一种用于气固系统的计算流体动力学(CFD)模型,以研究流化床中的流体动力学。使用此模型,已在二维床中模拟了射流穿透高度,射流频率,时间平均轴向气体流速分布和时间平均空隙率分布。计算结果表明,射流穿透高度随射流气体速度的增加而增加。喷射频率随着喷射气体速度的增加和粒径的减小而降低。时间平均轴向气体速度曲线变得“较低”和“较宽”,并且时间平均空隙率随着与喷嘴的距离增加而减小。这些结论与文献中的实验和模拟数据非常吻合。

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