...
首页> 外文期刊>Chemical Engineering Science >Numerical description of flow regime transitions in bubble column reactors by a multiple gas phase model [Review]
【24h】

Numerical description of flow regime transitions in bubble column reactors by a multiple gas phase model [Review]

机译:用多气相模型对鼓泡塔反应器中流态转变的数值描述[综述]

获取原文
获取原文并翻译 | 示例
   

获取外文期刊封面封底 >>

       

摘要

The study of the hydrodynamics of bubble column reactors reveals that three main flow regimes can be distinguished. The present study is an original application of standard numerical multiphase models aiming at a better prediction of the transitions and a better description of these regimes. This approach consists of a two-step calculation with, in a first time, the determination of bubble size distributions using coalescence and break-up laws, and in a second time, the implementation of this distribution in a multiple gas phase Euler-Euler model. Calculations are compared with experimental data: liquid velocities and global gas hold-ups. They were obtained in a cylindrical bubble column in which local or uniform aerations were performed. The comparison shows that our approach allows a good prediction of both flow regime transitions and flow characteristics such as hydrodynamics or turbulence. Furthermore, two bubble-induced turbulence models consisting, respectively, of an added viscosity and of two turbulence source terms added in the k-epsilon transport equations have been compared. (C) 2003 Elsevier Science Ltd. All rights reserved. [References: 22]
机译:对鼓泡塔反应器的流体动力学研究表明,可以区分三种主要的流态。本研究是标准数值多相模型的原始应用,旨在更好地预测转变和更好地描述这些制度。此方法包括两步计算,第一次使用合并和破裂定律确定气泡尺寸分布,第二次在多气相Euler-Euler模型中实施该分布。计算结果与实验数据进行了比较:液体速度和整体气体滞留量。它们是在圆柱形鼓泡塔中获得的,在该鼓泡塔中进行了局部或均匀曝气。比较表明,我们的方法可以很好地预测流态转换和流体特性,例如流体动力学或湍流。此外,还比较了两个气泡引起的湍流模型,分别由增加的粘度和在k-ε传输方程中添加的两个湍流源项组成。 (C)2003 Elsevier ScienceLtd。保留所有权利。 [参考:22]

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号