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Turbulent convection in emulsions: the Rayleigh–Bénard configuration
Department of Mechanical and Industrial Engineering, University of Illinois at Chicago, 842 W. Taylor Street, Chicago, IL 60607, USA.
KTH, School of Engineering Sciences (SCI), Engineering Mechanics, Fluid Mechanics. Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544, USA.ORCID iD: 0000-0002-1330-3348
KTH, School of Engineering Sciences (SCI), Engineering Mechanics, Fluid Mechanics. Department of Energy and Process Engineering, Norwegian University of Science and Technology (NTNU), 7491 Trondheim, Norway; Department of Environment, Land and Infrastructure Engineering (DIATI), Politecnico di Torino, 10129 Turin, Italy.ORCID iD: 0000-0002-4346-4732
Department of Mechanical and Industrial Engineering, University of Illinois at Chicago, 842 W. Taylor Street, Chicago, IL 60607, USA.
2024 (English)In: Journal of Fluid Mechanics, ISSN 0022-1120, E-ISSN 1469-7645, Vol. 999, article id A4Article in journal (Refereed) Published
Abstract [en]

This study explores heat and turbulent modulation in three-dimensional multiphase Rayleigh–Bénard convection using direct numerical simulations. Two immiscible fluids with identical reference density undergo systematic variations in dispersed-phase volume fractions, 0.0≤𝛷≤0.5, and ratios of dynamic viscosity, 𝜆𝜇, and thermal diffusivity, 𝜆𝛼, within the range [0.1–10]. The Rayleigh, Prandtl, Weber and Froude numbers are held constant at 108, 4, 6000 and 1, respectively. Initially, when both fluids share the same properties, a 10 % Nusselt number increase is observed at the highest volume fractions. In this case, despite a reduction in turbulent kinetic energy, droplets enhance energy transfer to smaller scales, smaller than those of single-phase flow, promoting local mixing. By varying viscosity ratios, while maintaining a constant Rayleigh number based on the average mixture properties, the global heat transfer rises by approximately 25 % at 𝛷=0.2 and 𝜆𝜇=10. This is attributed to increased small-scale mixing and turbulence in the less viscous carrier phase. In addition, a dispersed phase with higher thermal diffusivity results in a 50 % reduction in the Nusselt number compared with the single-phase counterpart, owing to faster heat conduction and reduced droplet presence near walls. The study also addresses droplet-size distributions, confirming two distinct ranges dominated by coalescence and breakup with different scaling laws.

Place, publisher, year, edition, pages
Cambridge University Press (CUP) , 2024. Vol. 999, article id A4
Keywords [en]
breakup/coalescence, Bénard convection, emulsions
National Category
Energy Engineering Fluid Mechanics Astronomy, Astrophysics and Cosmology
Identifiers
URN: urn:nbn:se:kth:diva-366503DOI: 10.1017/jfm.2024.765ISI: 001350929100001Scopus ID: 2-s2.0-85209768842OAI: oai:DiVA.org:kth-366503DiVA, id: diva2:1982653
Note

QC 20250708

Available from: 2025-07-08 Created: 2025-07-08 Last updated: 2025-07-08Bibliographically approved

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Scapin, NicoloBrandt, Luca

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