期刊文献+

基于径向力平衡的鼓泡塔二维流体力学模型 被引量:6

2-D hydrodynamic model of bubble column based on lateral-force balance
下载PDF
导出
摘要 提出了一种鼓泡塔二维轴对称流体力学模型,模型中将气泡所受的升力以及湍动扩散力作为形成塔内气含率稳定分布的主要机制。采用Fluent6.3流体力学软件求解模型,能得到稳定的二维流场,气含率与液速分布与实验值吻合良好,模型能准确反映表观气速(O.12~0.62m·s^-1)以及塔径(φ200mm、φ500m、φ800mm)对流型的影响。利用该模型对更大直径鼓泡塔的流动参数进行了预测,结果与文献给出的经验关联式相符。 A 2-D axisymmetric hydrodynamic model of bubble column was developed, by considering lift force and turbulent dispersion force on bubbles as main mechanism of stable distribution of gas holdup. A commercial code Fluent 6.3 was used for calculation, and the model gave a stable 2-D flow pattern, in which distributions of gas holdup and liquid velocity were in good agreement with experimental data. The model correctly demonstrated the influence of superficial gas velocity (0.12--0.62 m · s^-1) and column diameter (φ200 mm, φ500 mm, φ800 mm) on flow pattern. Furthermore, hydrodynamic variables predicted by the model in larger scale columns agreed with published empirical correlations.
出处 《化工学报》 EI CAS CSCD 北大核心 2014年第11期4222-4230,共9页 CIESC Journal
基金 国家高技术研究发展计划项目(2011AA05A205) 国家自然科学基金项目(U1162125 U1361112)~~
关键词 鼓泡塔 流体力学模型 表观气速 塔径 bubble column hydrodynamic model superficial gas velocity column diameter
  • 相关文献

参考文献25

  • 1Shaikh A, Al-Dahhan M. Scale-up of bubble column reactors: a review of current state-of-the-art [J]. Industrial & Engineering Chemistry Research, 2013, 52:8091-8108.
  • 2Forret A, Schweitzer J M, Gauthier T, Krishna R, Schweich D. Scale up of slurry bubble reactors [J]. Oil & Gas Science and Technology, 2006, 61 (3): 443-458.
  • 3Dhotre M T, Niceno B, Smith B L. Large eddy simulation of a bubble colunm using dynamic sub-grid scale model [J]. Chemical Engineering Journal, 2008, 136:337-348.
  • 4Joshi J B. Computational flow modeling and design of bubble column reactors [J]. ChemicalEngineering Science, 2001, 56:5893-5933.
  • 5Ekambara K, Dhotre M T, Joshi J B. CFD simulations of bubble column reactors: 1D, 2D and 3D approach [J]. Chemical Engineering Science, 2005, 60: 6733- 6746.
  • 6Nayak A K, Borka Z, Patrtmo L E, Sporleder F, Dorao C A, Jakobsen H A. A combined multifluid-population balance model for vertical gas-liquid bubble-driven flows considering bubble column operating conditions [J]. Industrial & Engineering Chemical Research, 2011, 50:1786-1798.
  • 7Jakobsen H A. Chemical Reactor Modeling: Multiphase Reactive Flows [M]. Berlin Heidelberg: Springer, 2008.
  • 8Wang Tiefeng, Wang Jinfu, Jin Yong. A CFD-PBM coupled model for gas-liquid flows [J]. AIChEJournal, 2006, 52:125-140.
  • 9Vitanker V S, Joshi J B. A comprehensive one-dimensional model for prediction of flow pattern in bubble columns [J]. Chemical Engineering Science, 2002, 80:499-511.
  • 10张煜,李红波,李兆奇,王丽军,李希.湍动浆态床流体力学研究(Ⅳ)带垂直列管束的浆态床流体力学模型与模拟[J].化工学报,2011,62(12):3373-3380. 被引量:7

二级参考文献71

共引文献53

同被引文献68

引证文献6

二级引证文献31

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部