迷惑
计算流体力学
机械
尾水管
流量(数学)
湍流
混合(物理)
连续搅拌釜式反应器
多相流
叶轮
材料科学
相(物质)
动量(技术分析)
热力学
化学
物理
有机化学
物理化学
财务
量子力学
经济
作者
Wang Li-cheng,Mengya Wang,Qi Yu,Yanxing Tian,Yiwei Gao
标识
DOI:10.1021/acs.iecr.0c04587
摘要
The liquid–solid–solid three-phase flow field was established in a stirred reactor with a draft tube and baffles. The solid concentration distribution, mixing time, velocity distribution, flow pattern, and power consumption of the flow field were systematically studied by means of a cold model experiment and computational fluid dynamics (CFD) simulation. The CFD model was based on the Euler multiphase flow model and the RNG k–ε turbulence model. Different momentum exchange coefficient models were taken into account for each phase. It was found that at the same stirring speed, the solid distribution was more uniform and the mixing time was less when the draft tube was equipped. The flow pattern of the flow field was more regular and the velocity distribution of the solid phase was more uniform in the reactor with the draft tube. According to the Nagata correlation, a power consumption formula was derived, and its applicability was verified by comparison of the experimental results.
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