3D CFD modeling of acetone hydrogenation in fixed bed reactor with spherical particles  

作　　者：Xiaoming Zhou Yanjun Duan Xiulan Huai Xunfeng Li 

机构地区：[1]Institute of Engineering Thermophysics,Chinese Academy of Sciences

出　　处：《Particuology》2013年第6期715-722,共8页颗粒学报（英文版）

基　　金：supported by the National Natural Science Foundation of China(No.51276181);the National Basic Research Program of China(No.2011CB710705);the National Natural ScienceFoundation of China(No.51106158)

摘　　要：Acetone hydrogenation in a fixed bed reactor packed with spherical catalyst particles was simulated to study the effects of inlet gas velocity and particle diameter on hydrogenation reaction. Computational results show that the catalyst particles in the reactor are almost isothermal, and the high isopropanol concentration appears at the lee of the particles. With the increase of inlet velocity, the outlet isopropanol mole fraction decreases, and the total pressure drop increases drastically. Small diameter catalyst particles are favorable for acetone hydrogenation, but result in large pressure drop.Acetone hydrogenation in a fixed bed reactor packed with spherical catalyst particles was simulated to study the effects of inlet gas velocity and particle diameter on hydrogenation reaction. Computational results show that the catalyst particles in the reactor are almost isothermal, and the high isopropanol concentration appears at the lee of the particles. With the increase of inlet velocity, the outlet isopropanol mole fraction decreases, and the total pressure drop increases drastically. Small diameter catalyst particles are favorable for acetone hydrogenation, but result in large pressure drop.

关 键 词：Fixed bed reactor Chemical heat pump Acetone hydrogenation Spherical particles CFD 

分 类 号：TQ021[化学工程]