首页 | 本学科首页   官方微博 | 高级检索  
     

曳力模型和湍流模型对内环流反应器数值模拟的影响
引用本文:张佳宝,崔丽杰,杨宁. 曳力模型和湍流模型对内环流反应器数值模拟的影响[J]. 化工学报, 2018, 69(1): 389-395. DOI: 10.11949/j.issn.0438-1157.20170830
作者姓名:张佳宝  崔丽杰  杨宁
作者单位:1.中国科学院大学化学科学学院, 北京 100049;2.中国科学院过程工程研究所多相复杂系统国家重点实验室, 北京 100190
基金项目:国家重点研发计划项目(2017YFB0602500);国家自然科学基金项目(91434121,91634203)。
摘    要:研究了曳力模型和湍流模型对气升式内环流反应器流体力学参数的影响,进一步证实了DBS-Local曳力模型在气升式内环流反应器中的适用性。结果表明:曳力模型决定了是否可以模拟出下降管中的气体;而曳力模型和湍流模型共同作用,决定了气含率模拟结果的准确性。Schiller-Naumann、Tomiyama、Grace、Ishii-Zuber这4种曳力模型均无法预测出下降管含气这一现象,而DBS-Local曳力模型能够模拟出下降管中的气体。DBS-Local曳力模型与standard k-ε mixture湍流模型组合,对气含率的预测值与实验值较为接近,而与RNG k-ε dispersed湍流模型组合,对轴向液速的预测值与实验值更为接近。

关 键 词:计算流体力学  内环流反应器  气液两相流  曳力模型  湍流模型  气含率  
收稿时间:2017-06-28
修稿时间:2017-08-03

Effects of drag model and turbulence model on simulation of air-lift internal-loop reactor
ZHANG Jiabao,CUI Lijie,YANG Ning. Effects of drag model and turbulence model on simulation of air-lift internal-loop reactor[J]. Journal of Chemical Industry and Engineering(China), 2018, 69(1): 389-395. DOI: 10.11949/j.issn.0438-1157.20170830
Authors:ZHANG Jiabao  CUI Lijie  YANG Ning
Affiliation:1.School of Chemical Sciences, University of Chinese Academy of Sciences, Beijing 100049, China;2.State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
Abstract:The influence of drag models and turbulence models on the hydrodynamic parameters in an air-lift internal-loop reactor is evaluated. Drag models determine the existence of gas in downcomer, and drag models and turbulence models jointly determine the accuracy of the simulation of gas holdup. Using uniform size bubbles, the Schiller-Naumann, Tomiyama, Grace and Ishii-Zuber drag models are only suitable for lower superficial gas velocity, and there is no gas in downcomer. The capability of DBS-Local drag model was confirmed. Compared with the other four drag models, only DBS-Local drag model can predict the existence of gas in downcomer. DBS-Local drag model combining with the standard k-ε mixture turbulence model can well predict gas holdup, and combining with RNG k-ε dispersed turbulence model can better predict liquid velocity.
Keywords:CFD  internal-loop reactor  gas-liquid flow  drag model  turbulence model  gas holdup  
点击此处可从《化工学报》浏览原始摘要信息
点击此处可从《化工学报》下载免费的PDF全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号