This study explores heat and turbulent modulation in three-dimensional multiphase Rayleigh–Benard convection using direct numerical simulations. Two immiscible fluids with identical reference density undergo systematic variations in dispersed-phase volume fractions, between 0.0 and 0.5, and ratios of dynamic viscosity and thermal diffusivity 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 volume fraction 0.2 and viscosity ratio 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.
Turbulent convection in emulsions: the Rayleigh–Bénard configuration / Moradi Bilondi, Abbas; Scapin, Nicolò; Brandt, Luca; Mirbod, Parisa. - In: JOURNAL OF FLUID MECHANICS. - ISSN 0022-1120. - 999:(2024). [10.1017/jfm.2024.765]
Turbulent convection in emulsions: the Rayleigh–Bénard configuration
Brandt, Luca;
2024
Abstract
This study explores heat and turbulent modulation in three-dimensional multiphase Rayleigh–Benard convection using direct numerical simulations. Two immiscible fluids with identical reference density undergo systematic variations in dispersed-phase volume fractions, between 0.0 and 0.5, and ratios of dynamic viscosity and thermal diffusivity 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 volume fraction 0.2 and viscosity ratio 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.File | Dimensione | Formato | |
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https://hdl.handle.net/11583/2996263