The DOI matches its Crossref record; 41 of the 41 references it cites were found in a registry or an index.
Breakage and coalescence models for drops in turbulent dispersions
Abstract
Abstract A substantial effort has been made by numerous investigators to describe droplet breakage and coalescence in turbulent dispersions. An attempt is made here to improve these models based on existing frameworks and recent advances described in the literature. Two‐step mechanisms are considered for both the breakage and coalescence models. The drop breakage function is structured as the product of the drop‐eddy collision frequency and breakage efficiency which reflect the energetics of turbulent liquid‐liquid dispersions. The coalescence function retains the former structure of the product of drop‐drop collision frequency and coalescence efficiency. The coalescence efficiency model has been modified to account for the effects of film drainage for drops with partially mobile interfaces. These models overcome several inconsistencies observed in previous efforts and are applicable for dense dispersions (about ϕ[0.10–0.30]). For the daughter drops produced by breakage, a probability density is proposed based on the energy requirements for the formation of daughter drops.
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“The daughter drop size distribution should be bimodal with a higher probability density at the ends rather than in the center since the energy requirement for the breakage of a drop into two drops of equal size is larger than the one needed for the breakage into a small and a large drop.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [275]
In the citing paper
“The model of Tsouris and Tavlarides [275] assumes the same form as the one of Prince and Blanch [273]. The eddy-drop collision frequency is based on the assumptions that the isotropic turbulence holds, the drop size is in the inertial sub-range, and only eddies whose size is equal to or smaller than the drop size can cause the breakage of the drops.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [275]
In the citing paper
“The main idea underlying the eddy-drop collision frequency is that eddies and drops behave like ideal gas molecules and collision phenomena can be modeled utilizing the kinetic theory of gases. Besides, it is assumed that the energy required for the breakage of a drop is proportional to the energy needed to create a new surface.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [275]
In the citing paper
“Coalescence occurs if the contact time is large enough so that the liquid film between two drops drains until a critical thickness is reached.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [275]
In the citing paper
“Tsouris and Tavlarides [275] proposed a modification of the Coulaloglou and Tavlarides model [244].”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [275]
Citations
Cites
Fundamentals of the hydrodynamic mechanism of splitting in dispersion processes
Hinze, J. O. (1955) · AIChE Journal · doi:10.1002/aic.690010303 · Cited by 2,694
The formation of emulsions in definable fields of flow
Taylor, G. I. (1934) · Proceedings of the Royal Society of London Series A Containing Papers of a Mathematical and Physical Character · doi:10.1098/rspa.1934.0169 · Cited by 2,572
The viscosity of a fluid containing small drops of another fluid
Taylor, G. I. (1932) · Proceedings of the Royal Society of London Series A Containing Papers of a Mathematical and Physical Character · doi:10.1098/rspa.1932.0169 · Cited by 2,025
Description of interaction processes in agitated liquid-liquid dispersions
Coulaloglou, C. A., & Tavlarides, L. L. (1977) · Chemical Engineering Science · doi:10.1016/0009-2509(77)85023-9 · Cited by 1,245
Self-citationBubble coalescence and break-up in air-sparged bubble columns
Prince, M. J., & Blanch, H. W. (1990) · AIChE Journal · doi:10.1002/aic.690361004 · Cited by 1,238
Theory of Homogeneous Turbulence
Tatsumi, T. (1980) · Advances in applied mechanics · doi:10.1016/s0065-2156(08)70232-1 · Cited by 849
On the behaviour of liquid dispersions in mixing vessels
Shinnar, R. (1961) · Journal of Fluid Mechanics · doi:10.1017/s0022112061000214 · Cited by 456
Drop breakup in turbulent stirred‐tank contactors. Part I: Effect of dispersed‐phase viscosity
Calabrese, R. V., Chang, T., & Dang, P. T. (1986) · AIChE Journal · doi:10.1002/aic.690320416 · Cited by 425
The Status of Population Balances
Ramkrishna, D. (1985) · Reviews in Chemical Engineering · doi:10.1515/revce.1985.3.1.49 · Cited by 393
The lubrication force between two viscous drops
Davis, R. H., Schonberg, J. A., & Rallison, J. M. (1989) · Physics of Fluids A Fluid Dynamics · doi:10.1063/1.857525 · Cited by 302
Research works printed but not linked: 4
- Byrne G. D., 1976, EPISODE: An Experimental Package for the Integration of Systems of Ordinary Differential Equations
- Cutter L. A. “Flow and Turbulence in a Stirred Tank ” PhD Thesis Columbia University New York (1960).
- Hinze J. O., 1959, Turbulence
- Kennard E. H., 1938, Kinetic Theory of Gases
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Estimation of Coalescence and Breakage Rate Constants within a Kühni Column
Kentish, S. E., Stevens, G. W., & Pratt, H. R. C. (1998) · Industrial & Engineering Chemistry Research · doi:10.1021/ie970336q · Cited by 27
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Azizi, F., & Taweel, A. M. A. (2010) · Chemical Engineering Science · doi:10.1016/j.ces.2010.08.034 · Cited by 25
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Falzone, S., Buffo, A., Vanni, M., & Marchisio, D. L. (2018) · Advances in chemical engineering · doi:10.1016/bs.ache.2018.01.002 · Cited by 26
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Raikar, N. B., Bhatia, S. R., Malone, M. F., & Henson, M. A. (2006) · Chemical Engineering Science · doi:10.1016/j.ces.2006.08.022 · Cited by 23
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Chen, Y., Ding, J., Weng, P., Yang, X., & Wu, W. (2019) · Chemical Engineering Journal · doi:10.1016/j.cej.2019.05.187 · Cited by 22
Krýsa, P., & Šoóš, M. (2022) · International Journal of Heat and Mass Transfer · doi:10.1016/j.ijheatmasstransfer.2022.123466 · Cited by 24
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Efficacy of a spinning disc as a bubble break-up device
Deglon, D. A., O’Connor, C. T., & Pandit, A. B. (1998) · Chemical Engineering Science · doi:10.1016/s0009-2509(97)00309-6 · Cited by 22
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Dalmau, E., Sánchez, A., Montesinos, J. L. G., Valero, F., Lafuente, J., & Casas, C. (1998) · Journal of Biotechnology · doi:10.1016/s0168-1656(97)00153-3 · Cited by 19
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Self-citationCOMPARISON OF LIQUID-LIQUID DISPERSIONS FORMED BY A STIRRED TANK AND ELECTROSTATIC SPRAYING*
Tsouris, C., NEAL, S. H., Shah, V. M., Spurrier, M. A., & Lee, M. K. (1997) · Chemical Engineering Communications · doi:10.1080/00986449708936612 · Cited by 16
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Eskin, D., Taylor, S., Ma, S. M., & Abdallah, W. (2017) · Chemical Engineering Science · doi:10.1016/j.ces.2017.07.023 · Cited by 13
Metadata
- Authors
- Tsouris, C., & Tavlarides, L. L.
- Affiliations
- Syracuse University (US)
- Corresponding author
- Tavlarides, L. L.
- Venue
- AIChE Journal
- Publisher
- Wiley
- Published
- 1994-03
- Volume
- 40
- Issue
- 3
- Pages
- 395-406
- ISSN
- 0001-1541 (ISSN-L)
- 1547-5905
- OpenAlex
- W2150301534
- Cited by
- 544
- References
- 41
- Citations by year
- 2026: 11 · 2025: 16 · 2024: 21 · 2023: 16 · 2022: 17 · 2021: 20 · 2020: 22 · 2019: 27 · 2018: 11 · 2017: 26 · 2016: 22 · 2015: 22 · 2014: 18 · 2013: 28 · 2012: 13
- FWCI
- 6.33
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- AIChE Journal (publishedVersion)
- Topics
- Physical Sciences › Chemical Engineering › Fluid Flow and Transfer Processes › Fluid Dynamics and Mixing
- Physical Sciences › Engineering › Computational Mechanics › Fluid Dynamics and Heat Transfer
- Physical Sciences › Chemical Engineering › Fluid Flow and Transfer Processes › Innovative Microfluidic and Catalytic Techniques Innovation
- Keywords
- droplet breakup, droplet coalescence, turbulent dispersion, liquid-liquid dispersions, coalescence efficiency, film drainage
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