A Comparative CFD Study on Laminar and Turbulent Flow Fields in Dual-Rushton Turbine Stirred Vessels

被引:6
作者
Li, L. C. [1 ]
Chen, N. [2 ]
Xiang, K. F. [1 ]
Xiang, B. P. [1 ]
机构
[1] Southwest Univ Sci & Technol, Key Lab Testing Technol Mfg Proc, Minist Educ, Mianyang 621010, Sichuan, Peoples R China
[2] Yinhe Construct & Chem Grp Co Ltd, Anxian 622656, Sichuan, Peoples R China
关键词
Stirred vessel; Dual-impeller; Numerical simulation; Laminar and turbulent flow; Flow pattern; MIXING TIMES; CELL-DAMAGE; SIMULATION; TANK;
D O I
10.29252/jafm.13.02.30061
中图分类号
O414.1 [热力学];
学科分类号
摘要
A computational fluid dynamics(CFD) simulation was carried out to study on flow field characteristics in dual-Rusthton turbine stirred vessels in laminar and turbulent regimes. Model validation was conducted using experimental data in the literature. The simulation results show that flow pattern and dimensionless velocity distribution vary with Reynolds number in laminar regime, while these parameters remain almost unchanged for different Reynolds numbers in turbulent regime. For vessels with a certain geometrical configuration, flow pattern, dimensionless velocity distribution and impeller power number depend mainly on Reynolds number, and are little affected by working medium and enlargement scale. By changing impeller spacing and off-bottom clearance of lower impeller, it is obtained the parallel, merging and diverging flow patterns in turbulent regime, and the changing processes of flow patterns in laminar regime for the three configurations. Total power number has the order of parallel>diverging>merging for the three configurations at the same Reynolds number. With increasing of Reynolds number, the power number of merging configuration shows the largest drop, followed by diverging configuration, and the lowest drop for parallel configuration in laminar regime, while power number rises slightly for the three configurations in turbulent regime.
引用
收藏
页码:413 / 427
页数:15
相关论文
共 41 条
[1]  
Abrardi V., 1988, 6 EUR C MIX PAV IT, P329
[2]   A 3D CFD simulation of a self inducing Pitched Blade Turbine Downflow [J].
Achouri, Ryma ;
Mokni, Ines ;
Mhiri, Hatem ;
Bournot, Philippe .
ENERGY CONVERSION AND MANAGEMENT, 2012, 64 :633-641
[3]   Unconventional configuration studies to improve mixing times in stirred tanks [J].
Ascanio, G ;
Brito-Bazán, M ;
Brito-De La Fuente, E ;
Carreau, PJ ;
Tanguy, PA .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 80 (04) :558-565
[4]  
Bakker A, 1996, CHEM ENG RES DES, V74, P485
[5]   PHYSICAL-MECHANISMS OF CELL-DAMAGE IN MICROCARRIER CELL-CULTURE BIOREACTORS [J].
CHERRY, RS ;
PAPOUTSAKIS, ET .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 32 (08) :1001-1014
[6]  
Croughan MS, 2000, BIOTECHNOL BIOENG, V67, P841, DOI 10.1002/(SICI)1097-0290(20000320)67:6<841::AID-BIT19>3.0.CO
[7]  
2-K
[8]   CFD modelling of stirred tanks: Numerical considerations [J].
Deglon, D. A. ;
Meyer, C. J. .
MINERALS ENGINEERING, 2006, 19 (10) :1059-1068
[9]  
Fan L, 2004, CHINESE J CHEM ENG, V12, P324
[10]   Mixing times in coaxial mixers with Newtonian and non-Newtonian fluids [J].
Foucault, S ;
Ascanio, G ;
Tanguy, PA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (01) :352-359