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Received June 22, 2015
Accepted April 15, 2016
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Numerical simulation of flow field characteristics in a gas-liquid-solid agitated tank
Key Laboratory of Testing Technology for Manufacturing Process of Ministry of Education, School of Manufacturing Science and Engineering, Southwest University of Science and Technology, Mianyang, Sichuan 621010, P. R. China
tchllc@126.com
Korean Journal of Chemical Engineering, July 2016, 33(7), 2007-2017(11), 10.1007/s11814-016-0105-7
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Abstract
Computational fluid dynamics simulation was carried out to investigate flow field characteristics in a gasliquid-solid agitated tank. The Eulerian multifluid model along with standard k-ε turbulence model was employed in the simulation. A multiple reference frame approach was used to treat the impeller rotation. Liquid velocity, gas holdup and solid holdup distributions in the agitated tank were obtained. The effect of operating conditions on gas and solid distributions was investigated. The predicted flow pattern was compared with results in literature. The simulation results indicate that local hydrodynamic behaviors such as velocity, gas and solid holdup distribution, are strongly influenced by operating conditions. Within the scope of our study, increasing gas inlet rate caused liquid circulation to be weakened and was not in favor of gas dispersion. Solid holdup in the upper part of the tank, especially near the wall region decreased. Adding solid loadings resulted in liquid mean velocity near the surface region decreased, gas dispersion and solid suspension becoming worse.
Keywords
References
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Lane GL, Schwarz MP, Evans GM, Appl. Mathematical Modeling, 26, 223 (2002)
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Panneerselvam R, Savithri S, Surender GD, Chem. Eng. Res. Des., 86(12A), 1331 (2008)
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Schiller L, Naumann Z, Z. Ver. Deutsch. Ing., 77, 318 (1935)
Elgobashi SE, Rizk MA, Int. J. Multiph. Flow, 15, 119 (1989)
Lupasteanu AM, Galaction AI, Cascaval D, Romanian Society of Biological Sciences, 13, 3821 (2008)
Qi NN, Wu GY, Wang H, Zhang K, Zhang H, J. Chem. Industry Eng., 61, 2305 (2010)
Wadnerkar D, Utikar RP, Tade MO, Pareek VK, Adv. Powder Technol., 23(4), 445 (2012)
Qi NN, Zhang H, Zhang K, Xu G, Yang YP, Particuology, 11, 317 (2013)
Li Z, Experimental investigation and numerical simulation of flow characteristics in vessels stirred by disc turbines, Beijing: Beijing University of Chemical Technology (2007).
Aubin J, Le Sauze N, Bertrand J, Fletcher DF, Xuerer C, Exp. Therm. Fluid Sci., 28, 447 (2004)
Geisler RK, Mersmann AB, Local velocity distribution and power dissipation rate of suspension in stirred vessels, 6th European Conference on Mixing, Pavia, Italy, 267 (1988).