帮助 关于我们

返回检索结果

Rushton搅拌釜内的气含率分布及其流动特性的模拟
Simulation for gas hold-up distribution and flow behavior in Rushton stirred tank

查看参考文献15篇

文摘 利用雷诺应力模型结合多参考系法模拟了Rushton气液搅拌釜内的气液流动特性,得到了不同截面处气含率大小分布规律,并与γ射线CT实验所测得的结果做了比较,发现除排出流区CFD模拟值与实验值相差较大外,上循环区与下循环区都吻合得较好;结果表明排出流区的气含率最高,在搅拌桨高速旋转下,流体沿叶片端面急速排出,湍动也十分强烈。通过比较液相速度的径向分布侧形与轴向分布侧形可知:单相流的径向速度峰值更接近搅拌叶片的尖端,而两相流的径向速度峰值向外发生了平移;当达到临界状态后,自叶片端面向外的径向位置,通气量对液相速度的分布侧形几乎没有影响,但搅拌转速的影响却不能忽略;在叶片端面位置时,搅拌转速与通气量对径向速度的轴向分布影响较大,且通气量对液相径向速度变化的影响效果更加显著。
其他语种文摘 Reynolds stress model was combined with the multiple reference frame(MRF)approach to simulate gas-liquid flow characteristics in a stirred vessel agitated by a Rushton turbine, and an array of gas hold-up distribution in different cross sectional places was obtained.The numerical simulation results were compared with the experimental data measured by a developed gamma ray computed tomography(CT)system.The CFD simulation results are in reasonable agreement with the experimental data except the discharge flow region.It is indicated that the gas hold-up distribution in the discharge flow region is higher than that in other regions.At high speed of rotary agitator, the fluid discharges rapidly along the surface of blade-tips, and the turbulent dispersion is extraordinarily intense.Radial and axial velocity distribution profiles of the liquid phase under different experimental conditions have been discussed.It is demonstrated that the maximum radial velocity of single-phase flow is closer to mixing blade-tips, while the maximum radial velocity of the two-phase flow has a small outward translation.After reached the critical condition, from the outward blade-tips to the wall, the velocity distribution profile of liquid phase is barely influenced by gas flow rate along radial position, but the influence of impeller rotation speed can not be neglected.On the blade-tip surface, both impeller rotation speed and gas flow rate have serious influence on the axial distribution of radial liquid velocity, and the effect of gas flow rate is more significant than impeller rotation speed.
来源 化工学报 ,2011,62(10):2691-2698 【核心库】
DOI 10.3969/j.issn.0438-1157.2011.10.003
关键词 雷诺应力模型 ; 气液流动 ; 气含率分布 ; 速度分布
地址

湘潭大学化工学院, 湖南, 湘潭, 411105

语种 中文
文献类型 研究性论文
ISSN 0438-1157
学科 化学工业
基金 国家自然科学基金项目 ;  湖南省高校环境友好催化与绿色化工工艺科技创新团队支持计划 ;  湖南省高校绿色催化与反应工程重点实验室开发基金项目
文献收藏号 CSCD:4354860

参考文献 共 15 共1页

1.  Laakkonen M. Local bubble size distributions, gas-liquid interfacial areas and gas holdups in a stirred vessel with particle image velocimetry. Chemical Engineering Journal,2005,109:37-47 被引 11    
2.  Khopkar A R. Gas-liquid flow generated by a Rushton turbine in stirred vessel: CARPT/CT measurements and CFD simulations. Chemical Engineering Science,2005,60:2215-2229 被引 18    
3.  Lane G L. Numerical modelling of gas-liquid flow in stirred tanks. Chemical Engineering Science,2005,60:2203-2214 被引 20    
4.  孙海燕. 各向异性k-ε湍流模型在Rushton浆搅拌槽三维流场整体数值模拟中的应用. 化工学报,2002,53(11):1153-1159 被引 9    
5.  Khopkar Avinash R. CFD simulation of gas-liquid flows in stirred vessel equipped with dual rushton turbines: influence of parallel, merging and diverging flow configurations. Chemical Engineering Science,2008,63:3810-3820 被引 14    
6.  Han Luchang. The effect of eddy-bubble interaction model on the turbulent dispersion of gas bubbles in stirred tanks. Chinese Journal of Chemical Engineering,2001,18(1):1-7 被引 1    
7.  刘心洪. 采用大涡PIV方法研究搅拌槽内湍流动能耗散率. 过程工程学报,2008,8(3):425-431 被引 8    
8.  Sun Haiyan. Experimental and numerical study of gas hold-up in surface aerated stirred tanks. Chemical Engineering Science,2006,61:4098-4110 被引 7    
9.  Prince M J. Bubble coalescence and break-up in air-sparged bubble columns. AIChE J.,1990,36:1485-1499 被引 71    
10.  Luo H. Theoretical model for drop and bubble breakup in turbulent dispersions. AIChE J.,1996,42:1225-1233 被引 80    
11.  Wang Weijing. Experimental and numerical investigation on gas holdup and flooding in an aerated stirred tank with Rushton impeller. Ind. Eng. Chem. Res.,2006,45:1141-1151 被引 7    
12.  Liu Y J. Measurement of gas hold-up distribution and digital color image reconstruction for standard gas-liquid Rushton stirred tank with Cs-137 γ-CT. Journal of Chemical Engineering of Chinese Universities,2006,20(4):648-652 被引 1    
13.  Wu H. LDA measurements of turbulent flow parameters in a stirred mixer. Chemical Engineering Science,1989,44(10):2207-2221 被引 46    
14.  Ranade V V. Flow generated by a disc turbine. Trans. I Chem. E,1990,68(A):19-50 被引 1    
15.  Stoots C M. Mean velocity field relative to a Rushton turbine blade. AIChE J.,1995,41(1):1-11 被引 6    
引证文献 6

1 陈佳 侧进式搅拌釜内气液两相流的数值模拟 化工学报,2013,64(7):2344-2352
被引 3

2 魏文礼 气泡浮力羽流动力特性三维数值模拟研究 西北农林科技大学学报. 自然科学版,2014,42(5):229-234
被引 4

显示所有6篇文献

论文科学数据集
PlumX Metrics
相关文献

 作者相关
 关键词相关
 参考文献相关

版权所有 ©2008 中国科学院文献情报中心 制作维护:中国科学院文献情报中心
地址:北京中关村北四环西路33号 邮政编码:100190 联系电话:(010)82627496 E-mail:cscd@mail.las.ac.cn 京ICP备05002861号-4 | 京公网安备11010802043238号