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Effects of reducing the reactor diameter on thedense gas–solid fluidization of very heavyparticles: 3D numerical simulations

机译:减小反应器直径对重颗粒的致密气固流化的影响:3D数值模拟

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摘要

In this study, 3D numerical simulations using an Eulerian n-fluid approach of a gas–solidfluidized bed composed of very dense particles of tungsten (19,300 kg.m−3) were carriedout to examine the behavior of this suspension, especially the effects of the reduction ofthe fluidization column diameter on the fluidization quality. Tungsten was selected as asurrogate material of U(Mo) (Uranium molybdene) which is of interest for new nuclear fuelswith limited enrichment. Comparisons between experiments and computations for the axialpressure profile of a 5 cm diameter column demonstrate the capability of the mathematicalmodels of the NEPTUNE CFD code to simulate the fluidization of this powder located out-side the classification of Geldart. The numerical results show that the mobility into the bedof these very dense particles is very low. The reduction of the fluidization column diam-eter from 5 cm to 2 cm does not have significant effect on the local solid circulation butstrongly decreases the axial and radial mixing of the particles due to wall-particles frictioneffects. These results confirm and allow to better understand the wall effects experimentally evidenced.
机译:在这项研究中,使用欧拉n流体方法对由非常密集的钨颗粒(19,300 kg.m-3)组成的气固流化床进行了3D数值模拟,以检验这种悬浮液的行为,特别是对悬浮液的影响。减小流化塔直径对流化质量的影响。钨被选作U(Mo)(铀钼)的替代材料,这对浓缩程度有限的新型核燃料很感兴趣。对直径为5 cm的色谱柱的轴向压力曲线进行的实验和计算之间的比较表明,NEPTUNE CFD代码的数学模型能够模拟位于Geldart分类之外的这种粉末的流态化。数值结果表明,这些非常致密的颗粒进入床层的迁移率非常低。将流化塔直径从5 cm减小到2 cm不会对局部固体循环产生显着影响,但是由于壁-颗粒的摩擦效应,会大大降低颗粒的轴向和径向混合。这些结果证实并允许更好地理解实验证明的壁效应。

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