In this paper,the particle flow in a combined-moving bed reactor was simulated using the discrete element method(DEM),and the accuracy of DEM simulation was verified by a comparison with the literature results. The effects of rotational speed and open-hole size of two kinds of distributing devices were analyzed. The results showed that:①There are two kinds of flow patterns for the two distributing devices,i.e.,plug flow and funnel flow;②particle mass fluxes increased non-linearly with the increase of rotational speed and open-hole size of the distributing devices;③along the radial direction,particles were distributed more uniformly with increasing the rotational speed and open-hole size,and the distribution showed U and M shapes for the two kinds of distributing devices;④the radial distribution of particles were more uniformly downwardly along the axial direction,with values of the variance coefficient exceeding 1.0 for the fan-shaped hole distributing plate,and 0.5 for another distributing plate.%针对复合移动床反应器内固体颗粒运动，采用离散单元法模型（DEM）考察布料器分别为扇形开口和矩形开口时，布料器转速和开口对颗粒运动的影响，并基于文献结果论证了本文模型的准确性。模拟结果表明：①对于不同布料器，颗粒在移动床中呈现平推流和汇聚流两种流动形态。②随布料器转速及开口的增加，颗粒质量通量非线性增加。③随布料器转速的增加，下落床径向上颗粒分布更均匀；随布料器开口的增大，下落床径向上颗粒分布范围变大，颗粒分布更均匀；对下落床径向上颗粒分布，布料器扇形开口时分布呈 U 形、矩形开口时分布呈M形。④沿反应器轴向向下，颗粒分布有均匀化趋势；扇形开口布料器对颗粒分布的离散系数大于1，矩形开口布料器对颗粒分布的离散系数约为0.5。
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