规整填料塔液相流动的计算流体力学模拟  

CFD SIMULATIONS OF LIQUID PHASE FLOW IN STRUCTURED PACKED COLUMN

作　　者：张鹏[1] 刘春江[1] 袁希钢[1] 余国琮[1] 

机构地区：[1]化学工程联合国家重点实验室(天津大学),天津大学化学工程研究所,天津300072

出　　处：《化工学报》2004年第8期1369-1373,共5页CIESC Journal

基　　金：国家自然科学基金项目 (No 2 0 2 0 60 2 1);天津市自然科学基金项目 (No 0 2 3 60 6711)~~

摘　　要：Liquid flow behavior, such as velocity distribution, in the packed column is of considerable importance in determining column performance. Using the volume-averaged method, a computational fluid dynamics(CFD) model was proposed to describe the liquid flow behavior in a structured packing column where the gas phase is stationary.A column packed with Mellapak 350Y had an inside diameter of 150 mm and a height of 1000 mm was simulated by solving the flow equations.A commercial CFD code, PHOENICS 3.3, was used to predict the fluid dynamics behavior of the liquid phase flow.The simulated profiles of pressure, velocity and concentration of the tracer were presented.The axial backmixing coefficients evaluated by the CFD results were presented and compared with the experimental data and the relative deviation was 3.8%—36.8%.Liquid flow behavior, such as velocity distribution, in the packed column is of considerable importance in determining column performance. Using the volume-averaged method, a computational fluid dynamics (CFD) model was proposed to describe the liquid flow behavior in a structured packing column where the gas phase is stationary. A column packed with Mellapak 350Y had an inside diameter of 150 mm and a height of 1000 mm was simulated by solving the flow equations. A commercial CFD code, PHOENICS 3.3, was used to predict the fluid dynamics behavior of the liquid phase flow. The simulated profiles of pressure, velocity and concentration of the tracer were presented. The axial backmixing coefficients evaluated by the CFD results were presented and compared with the experimental data and the relative deviation was 3.8%-36.

关 键 词：规整填料 计算流体力学 模拟 

分 类 号：TQ028.1[化学工程]