FAQ

Dispersion Kinetics Modelling

Data publikacji: 26.08.2016

Czasopismo Techniczne, 2016, Mechanika Zeszyt 1-M (1) 2016, s. 83 - 94

https://doi.org/10.4467/2353737XCT.16.009.4973

Autorzy

,
Pavel Ditl
Department of Process Engineering, Faculty of Mechanical Engineering, Czech Technical University in Prague, Czech Republic.
Wszystkie publikacje autora →
Radek Šulc
Department of Process Engineering, Faculty of Mechanical Engineering, Czech Technical University in Prague, Czech Republic.
Wszystkie publikacje autora →

Tytuły

Dispersion Kinetics Modelling

Abstrakt

Stirred tanks for dispersion, the pre-dispersion of two immiscible liquids or particulate solidliquid suspension are extensively used in the chemical, food, pharmaceutical and metallurgical industries, for purposes such as suspension/emulsion polymerisation, heterogeneous/phase-transfer catalytic chemical reactions, paint production and hydrometallurgical solvent extraction. The aim of this paper is to propose the simple dispersion model enabling the prediction of particle size changes over time and taking into account the type of breakup mechanisms, the non-homogeneity of local turbulent energy dissipation rate in an agitated vessel and the effect of the number of times the liquid passes through the impeller and the impeller zone. The model was successfully tested on data published by Ditl et al. (1981).

Bibliografia

[1] Paul E.L., Atiemo-Obeng V.A., Kresta S.M. (Eds.), Handbook of industrial mixing. Science and Practice, Wiley, Hoboken, NJ, 2004.

[2] Parfitt G.D., Dispersion of powders in liquids (2nd ed)., Applied Science Publishers, London 1973.

[3] Lu S., Pugh R.J., Forssberg E., Interfacial Separation of Particles, Studies in Interface Science, vol. 20, Elsevier 2005.

[4] Yeoh S.L., Papadakis G., Yianneskis M., Determination of mixing time and degree of homogeneity in stirred vessels with large eddy simulation, Chem. Eng. Sci., vol. 60, 2005, 2293-2302.

[5] Cheng D., Feng X., Cheng J., Yang, Ch., Numerical simulation of macro-mixing in liquid-liquid stirred tanks, Chem. Eng. Sci., vol. 101, 2013, 272-282.

[6] Sprow F.B., Distribution of drop sizes in turbulent liquid-liquid dispersions, Chem. Eng. Sci., vol. 22, 1967, 435-442.

[7] Taylor G.I., The formation of emulsions in definable fields of flow, Proc. R. Soc. Lond., A146, 1934, 501-523.

[8] Hinze J.O., Fundamentals of the hydrodynamic mechanism of splitting in dispersion  processes, AIChE J., vol. 1, 1955, 289-295.

[9] Hu B., Angeli P., Matar O.K., Hewitt G.F., Prediction of phase inversion in agitated vessels using a two-region model, Chem. Eng. Sci., vol. 60, 2005, 3487-3495.

[10] Shinnar R., On the behaviour of liquid dispersions in mixing vessels, J. of Fluid Mechanics, vol. 10, 1961, 259-275.

[11] Desnoyer C., Masbernat, O., Gourdon, C., Experimental study of drop size distributions at high phase ratio in liquid-liquid dispersions, Chem. Eng. Sci., vol. 58, 2003, 1353-1363.

[12] Bałdyga J., Podgórska W., Drop break-up in intermittent turbulence: maximum stable and transient sizes of drops, Can. J. of Chem. Eng., vol. 76, 1998, 456-470.

[13] Šulc R., Ditl P., The effect of process conditions on the flocculation process occurring in an agitated vessel, Polish J. of Chem. Technology, vol. 14, 2012, 88-96.

[14] Podgórska W., Bałdyga J., Scale up effects on the drop size distribution of liquidliquid dispersions in agitated vessels, Chem.Eng.Sci., vol. 56, 2001, 741-746.

[15] Raikar N.B., Bhatia S.R., Malone M.F., McClements D.J., Almeida-Rivera C., Bongers P., Henson M., Prediction of emulsion drop size distributions with population balance equation models of multiple drop breakage, Colloids and Surfaces A: Physicochem. Eng. Aspects, vol. 361, 2010, 96-108.

[16] Ditl P., Novák V., Rieger F., Dispergace v kapalinách rychloběžnými míchadly (Dispergation in liquids by high-speed impellers), Chem.průmysl, vol. 31(56), 1981, 3-10.

[17] Schlichting H., Boundary layer theory, McGraw-Hill, New York 1979.

Informacje

Informacje: Czasopismo Techniczne, 2016, Mechanika Zeszyt 1-M (1) 2016, s. 83 - 94

Typ artykułu: Oryginalny artykuł naukowy

Tytuły:

Polski:

Dispersion Kinetics Modelling

Angielski:

Dispersion Kinetics Modelling

Autorzy

Department of Process Engineering, Faculty of Mechanical Engineering, Czech Technical University in Prague, Czech Republic.

Department of Process Engineering, Faculty of Mechanical Engineering, Czech Technical University in Prague, Czech Republic.

Publikacja: 26.08.2016

Status artykułu: Otwarte __T_UNLOCK

Licencja: Żadna

Udział procentowy autorów:

Pavel Ditl (Autor) - 50%
Radek Šulc (Autor) - 50%

Korekty artykułu:

-

Języki publikacji:

Angielski

Liczba wyświetleń: 1622

Liczba pobrań: 750

<p> Dispersion Kinetics Modelling</p>