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
|