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CFD-PBM simulation of bubble coalescence and breakup in top blown-rotary agitated reactor

作     者:Pin Shao Shi-xu Liu Xin-cheng Miao Pin Shao;Shi-xu Liu;Xin-cheng Miao

作者机构:School of Materials and MetallurgyUniversity of Science and Technology LiaoningAnshan114051LiaoningChina 

出 版 物:《Journal of Iron and Steel Research International》 (J. Iron Steel Res. Int.)

年 卷 期:2022年第29卷第2期

页      面:223-236页

核心收录:

学科分类:080602[工学-钢铁冶金] 08[工学] 0806[工学-冶金工程] 

基  金:The authors wish to express thanks to the National Natural Science Foundation of China(51604147 and 51774178)for supporting this work 

主  题:Top blown-rotary agitated reactor Bubble coalescence Bubble breakup Bubble size CFD-PBM Numerical simulation 

摘      要:Gas–liquid flow and bubble coalescence and breakup behavior were studied in a top blown-rotary agitated reactor for *** important models of bubble coalescence and breakup mechanisms were considered and compared,and water model experiment was carried out to verify and optimize the mathematical *** influence of different operating parameters including paddle arrangement,stirring speed and top blowing flow rate on the bubble size and distribution was *** results show that the predicted bubble size and distribution present a good agreement with the experimental results using the improved Luo–Laakkonen combination *** the position of the stirring paddle moves from the center to the side wall,the bubble distribution in the reactor becomes more uniform,and the bubble size gradually *** the increase in the paddle rotation speed,the bubble size ***,this effect begins to weaken when the paddle rotation speed exceeds 150 r/*** the top blowing flow rate will increase the bubble size in the reactor,but it has a weak effect on bubble *** the top blowing rate exceeds 2.0 m^(3)/h,the bubble size in the bath is basically not less than 5 mm.

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