期刊文献+

生物反应器内不同桨叶组合计算流体力学模拟 被引量:2

Computational fluid dynamics simulation of different impeller combinations in bioreactor
下载PDF
导出
摘要 运用计算流体力学(CFD)数值模拟方法研究在相同工况下(搅拌桨转速为400 r/min、通气速度为0.86 vvm和操作温度为15℃),4种不同桨叶组合方式对5 L气液生物反应器流场、氧传质系数kLα、空气体积分数、气含率(体积分数)和功率的影响,评判各桨叶组合综合性能。计算结果表明:1号方案上下档均为径向桨,具有最高kLα提供能力;上档为轴向桨,下档为径向桨的2、3号组合,有较好的混合和分散气泡的能力;上下档均为轴向桨的4号方案有着较低能耗,约为0.2 W/L。 The influence of 4 kinds of different impeller combination on flow patterns,oxygen mass transfer coefficient kLα,air volume fraction,gas holdup(volume fraction) and power in a gas-liquid bioreactor was studied under the same operating conditions(rotation rate of impellers 400 r/min,gas rate 0.86 vvm and operating temperature 15 ℃) using computational fluid dynamics(CFD) numerical simulation method.The research results show that the Model 1 which has the radial flow impellers at both the top and bottom sides can provide the highest capacity of kLα.Meanwhile,the Model 2 3 with the assembled axial flow impeller at the top and the radial follow impeller at the bottom,have a better ability to mix the liquid and disperse bubbles.Compared with other three models,the Model 4,with the axial flow impellers at both top and bottom sides has lower power consumption,approximately 0.2 W/L.
出处 《化学工程》 CAS CSCD 北大核心 2011年第2期47-51,共5页 Chemical Engineering(China)
基金 国家"863"计划项目(2008AA10Z338 2006AA020301)
关键词 桨叶组合 气液二相流 生物反应器 CFD数值模拟 impeller combinations gas-liquid two-phase flow bioreactor CFD numerical simulation
  • 相关文献

参考文献5

  • 1XIA Jianye,WANG Yonghong,ZHANG Siliang.Fluid dynamics investigation of variant impeller combinations by simulation and fermentation experiment[J].Biochem Eng J,2009,43(5):252-260.
  • 2DHANASEKHARAN K,SANYAL J,JAIN A,et al.A generalized approach to model oxygen transfer in bioreactors using population balances and computational fluid dynamics[J].Chem Eng Sci,2005,60(1):213-218.
  • 3KHOPKAR A R,KASAT G R,PANDIT A B,et al.CFD simulation of mixing in tall gas-liquid stirred vessel:role of local flow patterns[J].Chem Eng Sci,2006,61(9):2921-2929.
  • 4KERDOUSS F,BANNARI A,PROULX P.CFD modeling of gas dispersion and bubble size in a double turbine stirred tank[J].Chem Eng Sci,2006,61(10):3313-3322.
  • 5KERDOUSS F,BANNARI A,PROULX P.Two-phase mass transfer coefficient prediction in stirred vessel with a CFD model[J].Comput Chem Eng,2008,32(8):1943-1955.

同被引文献12

引证文献2

二级引证文献6

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