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Research on separation mechanism of waste palladium catalyst in a structure-optimized compound dry separator based on DEM-CFD

机译:基于DEM-CFD的结构优化化合物干燥分离器中废钯催化剂的分离机理研究

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摘要

Recovery of precious metals from waste catalysts is necessary. The compound dry separator provides a new method for the recycling of waste catalysts with special morphology. The bed surface structure was modified in consideration of the unique properties of spent palladium catalyst in petrochemical industry. The solid-fluid coupling method (DEM-CFD) was used to study the distribution of airflow on the bed surface and the motion characteristics of particle swarm with different combinations of properties. The results showed that the best size of the apertures of bed surface was 2 mm and the optimum installation angle (beta) of the lattice bars on bed surface was 50 degrees. The velocity of air flow was small in the backplane region, but relatively large in the region far away from the backplane. And so was the case with dynamic pressure. The dynamic pressure was the largest in the central wind apertures and decreased gradually along the upward direction. The key factor influencing the distribution and movement of the aggregate on the bed surface was the shape of particles, while the effect of density was relatively weak. The separation efficiency (E-f) in numerical simulation was 99.83%, which coincided with the actual experimental result (99.57%).
机译:从废催化剂中回收贵金属是必要的。复合干燥分离器提供了一种具有特殊形态的废催化剂的再循环方法。考虑到石化工业中废钯催化剂的独特性能进行修饰床面结构。使用固体流体耦合方法(DEM-CFD)研究床面上气流的分布及粒子群的运动特性,具有不同的性质组合。结果表明,床面孔的最佳尺寸为2mm,床面上的晶格棒的最佳安装角度(β)为50度。背板区域的气流速度小,但在远离背板的区域中相对较大。这种情况是动态压力的情况。动态压力在中央风孔中最大,沿向上方向逐渐下降。影响床面上骨料分布和运动的关键因素是颗粒的形状,而密度的效果相对较弱。数值模拟中的分离效率(E-F)为99.83%,恰逢实际实验结果(99.57%)。

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