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http://dx.doi.org/10.9713/kcer.2012.50.5.913

Characteristic of Mass Transfer Volumetric Coefficient and Sauter Mean Diameter in a Liquid-Liquid Agitated Vessel  

Lee, Young-Sei (School of Nano & Materials Science and Engineering, Kyungpook National University)
Publication Information
Korean Chemical Engineering Research / v.50, no.5, 2012 , pp. 913-922 More about this Journal
Abstract
Grasp of characteristics within liquid-liquid agitated vessel are very important to environment and chemical industry. Mass transfer volumetric coefficient and the Sauter mean diameter of near the droplet were measured by varying the impeller position and liquid height using the alkaline hydrolysis reaction of esters. As a result, following their good correlation was obtained. $$d_{32}=0.270\(\frac{{\sigma}^{0.6}}{{\rho}^{0.2}P^{0.4}_{Vi}}\)k_La=0.49\(\frac{6{\phi}D_A}{d^2_{32}}\)\(\frac{P_Vd^4_{32}}{{\rho}v^3}\)^{0.193}Sc^{1/3}$$.
Keywords
Process of Environmental Pollutants; Mass Transfer Volumetric Coefficient; Sauter Mean Diameter; Liquid - Liquid Agitated Vessel; Impeller Position; Liquid Height;
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Times Cited By KSCI : 2  (Citation Analysis)
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1 Mochizuki, M. and Sato, K., "Drop Diameter Near the Tip of Turbine Impeller," Kag. Kog. Ronbunshu, 10(1), 49-55(1984).   DOI
2 Hinze, J. O., "Fundamentals of the Hydrodynamic Mechanism of Splitting in Dispersion Processes," AIChE J., 1(3), 289-295(1955).   DOI
3 Sprow, F. B., "Distribution of Drop Sizes Produced in Turbulent Liquid-liquid Dispersion," Chem. Eng. Sci., 22(3), 435-442(1967).   DOI   ScienceOn
4 McManamey, W. J., "Sauter Mean and Maximum Drop Diameters of Liquid-liquid Dispersions in Turbulent Agitated Vessels at Low Dispersed Phase Hold-up," Chem. Eng. Sci., 34(3), 432- 434(1979).   DOI   ScienceOn
5 Hiraoka, S., Tada, Y., Suzuki, H., Mori, H., Aragaki, T. and Yamada I., "Correlation of Mass Transfer Volumetric Coefficient with Power Input in Stirred Liquid-Liquid Dispersions," J. Chem. Eng. Japan, 23(4), 468-474(1990).   DOI   ScienceOn
6 Levins, B. E. and Glastonbury, J. R., "Particle-Liquid Hydrodynamic and Mass Transfer in a Stirred Vessel Part II-Mass Transfer," Trans. IChemE, 50, 132-146(1972).
7 Kikuchi, K., Tadakuma, Y., Sugawara, T. and Ohashi, H., "Effect of Inert Particle Concentration on Mass Transfer between Particles and Liquid in Solid-Liquid Two-Phase Upflow through Vertical Tubes and in Stirred Tanks," J. Chem. Eng. Japan, 20(2), 134-140(1987).   DOI
8 Asai, S., Konishi, Y. and Sasaki, Y., "Mass Transfer between Fine Particles and Liquids in Agitated Vessels," J. Chem. Eng. Japan, 21(2), 107-112(1988).   DOI
9 Kim, C. H., Chun, S. H., Shin, D. W., Kim, L. H., Lee, H. C. and Baek, Y. S., "CDF Simulation for Mixture Characteristic of DME-propane Liquified Fuels," Korean Chem. Eng. Res.(HWAHAK KONGHAK), 50(2), 328-333(2012).   DOI   ScienceOn
10 Keey, R. B. and Glen, J. B., "Area-free Mass Transfer Coefficients for Liquid Extraction in a Continuously Worked Mixer," AIChE J. 15(6), 942-947(1969).   DOI
11 Schindler, H. D. and Treybal, R. E., "Continuous-phase Masstransfer Coefficients for Liquid Extraction in Agitated Vessels," AIChE J. 14(5), 790-798(1968).   DOI
12 Skelland, A. H. P. and Lee, J. M., "Drop Size and Continuousphase Mass Transfer in Agitated Vessels," AIChE J. 27(1), 99-111(1981).   DOI   ScienceOn
13 Skelland, A. H. P. and Moeti, L. T., "Mechanism of Continuousphase Mass Transfer in Agitated Liquid-liquid Systems," Ind. Eng. Chem. Res., 29(11), 2258-2267(1990).   DOI
14 Calderbank, P. H. and Moo-Young, M. B., "The Continuous Phase Heat and Mass-transfer Properties of Dispersions," Chem. Eng. Sci., 16(1, 2), 39-54(1961).   DOI   ScienceOn
15 Hiraoka, S., Kamei, N., Kato, Y., Tada, Y., Asai, K., Hibino, S. and Yamaguchi, T., "Mass Transfer Volumetric Coefficient and Droplet Diameter in Liquid- Liquid Dispersions Stirred with a Paddle Impeller with Wire Gauze," J. Chem. Eng. Japan, 26(2), 227-229(1993).   DOI   ScienceOn
16 Chen, H. T. and Middleman, S., "Drop Size Distribution in Agitated Liquid-liquid Systems," AIChE J., 13(5), 989-995(1967).   DOI
17 Calderbank, P. H., "Physical Rate Processes in Industrial Fermentation, Part 1: The Interfacial Area in Gas-Liquid Contacting with Mechanical Agitation," Trans. IChemE, 36, 443-458(1958).
18 Kato, Y., Hiraoka, S., Fukumoto, S., Tada, Y., Nagatsu, Y., Ohmasa, R., Koh, S. T. and Lee, Y. S., "Flow Visualization and Numerical Analysis of a New Mixing Equipment with Vibratory Fins," Korean J. Chem. Eng., 27(1), 1-5(2010).   DOI   ScienceOn