Design of a gas–liquid unbaffled stirred tank with a concave blade impeller

被引:3
作者
Devi T.T. [1 ]
Kumar B. [1 ]
机构
[1] Institute of Technology Guwahati, Guwahati
关键词
Concave blade impeller; Gas holdup; Impeller clearance; Mass transfer; Power number; Stirred tank;
D O I
10.1007/s10891-015-1169-7
中图分类号
学科分类号
摘要
Experimental investigation of unbaffled multiphase (gas–liquid) stirred tanks is conducted with the use of a concave blade impeller to analyze mass transfer, gassed power, and gas holdup. The experiments are carried out with various impeller diameter to tank diameter ratios and impeller clearances. The design criterion for the mass transfer rate is proposed, and its prediction capability is found to be satisfactory. The results show that the gassed power is dependent on the impeller diameter to tank diameter ratio and impeller clearance. The design criteria for gassed power to ungassed power ratio and gas holdup are also introduced. Multiphase modeling is done by employing the computational fluid dynamics (CFD) techniques to observe the characteristic flow pattern transition and to carry out a qualitative analysis of the mass transfer rate. © 2015 Springer Science + Business Media New York.
引用
收藏
页码:76 / 87
页数:11
相关论文
共 49 条
[1]  
Liu Y.S., Wu J.Y., Ho K.P., Characterization of oxygen transfer conditions and their effects on phaffia rhodozyma growth and carotenoid production in shake-flask cultures, Biochem. Eng. J, 27, pp. 331-335, (2006)
[2]  
Amaral P., Freire M.G., Leao M.H., Marrucho I.M., Coutinho J.A., Coelho M.A., Optimization of oxygen mass transfer in a multiphase bioreactor with perfluorodecalin as a second liquid phase, Biotechnol. Bioeng, 99, pp. 588-598, (2008)
[3]  
Karimi A., Golbabaei F., Neghab M., Mehrnia M.R., Mohammad K., Pourmand M.R., Nikpey A., Investigation of oxygen transfer in a two-phase partition stirred tank bioreactor in the presence of silicone oil, Chem. Biochem. Eng. Q, 25, pp. 209-219, (2011)
[4]  
Chunmei P., Jian M., Xinhong L., Zhengming G., Investigation of fluid flow in a dual Rushton impeller stirred tank using particle image velocimetry, Chin. J. Chem. Eng, 16, pp. 693-699, (2008)
[5]  
Zadghaffari R., Moghaddas J.S., Revstedt J., Large-eddy simulation of turbulent flow in a stirred tank driven by a Rushton turbine, Comput. Fluids, 39, pp. 1183-1190, (2010)
[6]  
Li Z., Bao Y., Gao Z., PIV experiments and large eddy simulations of single-loop flow fields in Rushton turbine stirred tanks, Chem. Eng. Sci, 66, pp. 1219-1231, (2011)
[7]  
Taghavi M., Zadghaffari R., Moghaddas J., Moghaddas Y., Experimental and CFD investigation of power consumption in a dual Rushton turbine stirred tank, Chem. Eng. Res. Des, 89, pp. 280-290, (2011)
[8]  
Saito F., Nienow A.W., Chatwin S., Moore I.P., Power, gas dispersion and homogenization characteristics of Scaba SRGT and Rushton turbine impellers, J. Chem. Eng, 25, pp. 281-287, (1992)
[9]  
Cooke M., Middleton J.C., Bush J.R., Bioreactor Fluid Dynamics, In: Proc. 2Nd Bioreactor Conf, pp. 37-64, (1988)
[10]  
Chen Z.D., Chen J.J., Comparison of mass transfer performance for various single and twin impellers, Chem. Eng. Res. Des, 77, pp. 104-109, (1999)