期刊文献+

双层半圆管盘式涡轮桨搅拌槽气液分散特性的数值模拟 被引量:6

Numerical simulation of gas-liquid flow in a dual CD-6 impeller stirred tank
下载PDF
导出
摘要 采用基于气泡聚并和破碎机理的群体平衡(PBM-MUSIG)模型,对双层半圆管盘式涡轮桨搅拌槽内的气液分散特性进行了数值模拟;考察了不同通气量和操作转速下气液搅拌槽内流体流动,局部气含率和气泡尺寸的分布规律。模拟结果表明:通气工况下搅拌槽内的液相流场具有双循环流动形式;采用PBM-MUSIG模型预测的局部气含率分布与文献实验数据吻合较好;搅拌槽内气泡尺寸随转速增加而减小,随气量增加而增大;桨叶排出流区域内气泡尺寸较小,近壁区和循环区内气泡尺寸较大。 The gas dispersion characteristics in a dual CD-6 impeller stirred tank have been numerically simulated using the population balance model(PBM) combined with the multiple size group(MUSIG) model,which is based on the principle of bubble coalescence and breakup.The effects of varying the gas flow rate and rotation speed on the fluid field,local void fraction distribution and bubble size distribution have been investigated.The results show that the liquid flow adopts a dual loop flow pattern under gas dispersion operating conditions.The local void fraction distributions simulated using the PBM-MUSIG model are in good agreement with the experimental data from the literature.Bubble size decreases as the rotation speed increases,and increases as the gas flow rate increases.The bubble size is smaller in the impeller discharge region,and larger in the near-wall and circulation regions.
出处 《北京化工大学学报(自然科学版)》 CAS CSCD 北大核心 2011年第2期1-6,共6页 Journal of Beijing University of Chemical Technology(Natural Science Edition)
基金 国家自然科学基金(20576009/20821004)
关键词 气液搅拌槽 数值模拟 半圆管盘式涡轮桨 气泡尺寸 群体平衡模型 gas-liquid stirred tank numerical simulation CD-6 impeller bubble size PBM-MUSIG
  • 相关文献

参考文献13

  • 1Moucha T, Linek V, Prokopova E. Gas hold-up, mixing time and gas-liquid volumetric mass transfer coefficient of various multiple-impeller configurations: Rushton turbine, pitched blade and techmix impeller and their combinations[J]. Chemical Engineering Science, 2003, 58: 1839-1846.
  • 2Gao Z M, Smith J M, Muller-Steinhagen H. Void fraction distribution in sparged and boiling reactors with modern impeller configuration [ J ]. Chemical Engineering and Processing, 2001, 40: 489-497.
  • 3刘敏珊,张丽娜,董其伍.圆盘涡轮式搅拌槽的数值模拟[J].郑州大学学报(工学版),2007,28(1):122-124. 被引量:8
  • 4朱向哲,苗一,谢禹钧.双层涡轮搅拌桨三维流场数值模拟[J].石油化工设备,2005,34(4):26-29. 被引量:13
  • 5宋月兰,高正明,李志鹏.多层新型桨搅拌槽内气-液两相流动的实验与数值模拟[J].过程工程学报,2007,7(1):24-28. 被引量:31
  • 6孙会.搅拌罐内气液两相流场的数值研究[J].上海电机学院学报,2008,11(3):189-192. 被引量:5
  • 7Laakoner M, Moilanen P, Alopaeus V, et al. Modelling local gas-liquid mass transfer in agitate vessels [ J ]. Chemical Engineering Research and Design, 2007, 85 ( A5 ) : 665-675.
  • 8Gimbun J, Rielly C D, Nagy Z K. Modelling of mass transfer in gas liquid stirred tanks agitated by Rushton turbine an CD-6 impeller: a scale-up study[ J]. Chemical Engineering Research and Design, 2009, 87: 437- 451.
  • 9Lane G L, Schwarz M P, Evans G M, Numerical modelling of gas-liquid flow in stirred tanks[ J]. Chemical Engineering Science, 2005, 60: 2203-2214.
  • 10Lane G L, Schwarz M P, Evans G M. Predicting gas-liq-uid flow in a mechanically stirred tank [ J ]. Applied Mathematical Modelling,, 2006, 26 : 223-235.

二级参考文献27

  • 1陈凯,王嘉骏,顾雪萍,冯连芳,王凯.双层搅拌器组合的气液分散性能研究[J].化学工程,2004,32(3):24-27. 被引量:13
  • 2郝志刚,包雨云,高正明.多层组合桨搅拌槽内气-液分散特性的研究[J].高校化学工程学报,2004,18(5):547-552. 被引量:42
  • 3龙建刚,包雨云,高正明.搅拌槽内不同桨型组合的气-液分散特性[J].北京化工大学学报(自然科学版),2005,32(5):1-5. 被引量:17
  • 4[1]Kelly W,Gigas B.Using CFD to Predict the Behavior of Power Law Fluids Near Axial-flow Impellers Operating in the Transitional Flow Regime[J].Chem.Eng.Sci.,2003,58 (10):2141-2152.
  • 5[3]Gentric C,Mignon D,Bousquet J,et al.Comparison of Mixing in Two Industrial Gas-liquid Reactors Using CFD Simulations[J].Chem.Eng.Sci.,2005,60(8-9):2253-2272.
  • 6[4]Lane G L,Schwarz M P,Evans G M.Predicting Gas-liqnid flow in a Mechanically Stirred Tank[J].Applied Mathematical Modelling,2002,26 (2):223-235.
  • 7[5]Ranade V V,Perrard M,Xuereb C,et al.Influence of Gas Flow Rate on the Structure of Trailing Vortices of a Rushton Turbine:PIV Measurements and CFD Simulations[J].Chem.Eng.Res.Des.,2001,79(8):957-964.
  • 8[6]Khopkar A R,Rammohan A R,Ranade V V,et al.Gas-liquid Flow Generated by a Rushton Turbine in Stirred Vessel:CARPT/CT Measurements and CFD Simulations[J].Chem.Eng.Sci.,2005,60 (8-9):2215-2229.
  • 9[7]Morud K E,Hjertager B H.LDA Measurements and CFD Modeling of Gas-liquid flow in a Stirred Vessel[J].Chem.Eng.Sci.,1996,51 (2):233-249.
  • 10[8]Barigou M,Greaves M.Bubble-size Distributions in a Mechanically Agitated Gas-liquid Contactor[J].Chem.Eng.Sci.,1992,47 (8):2009-2025.

共引文献52

同被引文献66

引证文献6

二级引证文献14

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