Effect of Dispersed Phase Viscosity on Emulsification in Turbulence Flow

Article Preview

Abstract:

Systematic experimental study has been performed to examine the effects of dispersed phase viscosity on emulsification in turbulence flow. It is found that the volume drop size distributions widen as dispersed phase viscosity increased; at lower dispersed phase viscosity, both Sauter mean diameter and the maximum stable diameter increase with the viscosity, while at higher dispersed phase viscosity, Sauter mean diameter and the maximum stable diameter decreasing and increasing, respectively. It has also been found that linear relation between the Sauter mean diameter and the maximum stable drop diameter is still valid for the emulsions which show a bimodal volume distribution, and the proportional constant decreases as dispersed phase viscosity increases.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

571-575

Citation:

Online since:

November 2013

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2014 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] Y. S. Bo, Z. Z. Chang, Y. C. Yong, The simulation of the drop sizes in turbulent liquid-liquid dispersions, Journal of chemical engineering of Chinese Univ. 22(2008) 574-579.

Google Scholar

[2] M. Zerfa, B. W. Brooks, Prediction of vinyl choloride drop sizes in stablished liquid-liquid agitated dispersion, Chem. Eng. Sci. 51 (1996) 3223-3233.

DOI: 10.1016/0009-2509(95)00389-4

Google Scholar

[3] L. Y. Ling, H. L. Min, C. Hao, et al, Drop size model in oil-water dispersed flows, Journal of Chemical Industry and Engineering. 63(2012) 2059-(2063).

Google Scholar

[4] S. Hall, M. Cooke, A. J. Kowalski, et al, Droplet break-up by in-line Silverson rotor–stator mixer, Chem. Eng. Sci. 66(2011) 2068-(2079).

DOI: 10.1016/j.ces.2011.01.054

Google Scholar

[5] J. T. Davies, A physical interpretation of drop sizes in homogenizers and agitated tanks including the dispersion of viscous oil, Chem. Eng. Sci. 42(1987) 1671-1676.

DOI: 10.1016/0009-2509(87)80172-0

Google Scholar

[6] R. V. Calabrese, T. P. K. Chang, P. T. Dang, Drop breakup in turbulent stirred-tank contactors, AIChE J. 32(1986) 657-666.

DOI: 10.1002/aic.690320416

Google Scholar

[7] G. A. Padron, Effect of surfactants on drop size distribution in a batch rotor–stator mixer. PhD Thesis, University of Maryland, MD, USA. (2005).

Google Scholar

[8] C. A. Coulaloglou, L. L. Tavlarides, Description of interaction processes in agitated liquid-liquid dispersions, Chem. Eng. Sci. 32(1977), 1289-1297.

DOI: 10.1016/0009-2509(77)85023-9

Google Scholar