Theoretical analysis and simulations reveal scaling laws for heat transfer in porous media, enhancing thermal engineering applications.
This study conducted theoretical analysis and direct numerical simulations (DNS) of vertical natural convection in a two-dimensional cavity filled with porous media, where the imposed temperature gradient is oriented perpendicular to the direction of gravity. Three regimes characterised by distinct flow states and the angle θ of the isothermal layer are identified. In the steady regime I with θ ≈ π /2 , the flow is weak and heat transfer is dominated by conduction. In the transitional regime II with rapidly increasing θ , kinetic and thermal boundary layers gradually develop. In the turbulent regime III with θ ≈ 0 , clear boundary layers arise and turbulent thermal convection prevails. Corresponding to these flow states, theoretical analysis is performed to derive the scaling laws of the Nusselt number Nu-1~ RaDγ ₁Prη ₁ and Reynolds number Re~ RaDγ ₂Prη ₂ with respect to Rayleigh–Darcy number RaD and Prandtl number Pr . We derive (γ ₁,γ ₂,η ₁,η ₂)=(2,1,0,-1) for the steady regime and $(1/3,4/9,0,-2/3)$ for the turbulent regime. All theoretical scaling exponents in these two regimes are validated by DNS results. Furthermore, we find that the influence of the Darcy number $Da$ becomes almost negligible when it is sufficiently small. Unified models for Pr=1 are proposed to integrate the three regimes and are applicable across a broad range of φ and RaD , which are satisfactorily verified by DNS results. The unified models provide a predictive framework for heat transport and flow intensity in porous-medium thermal convection, thereby offering practical values for thermal engineering applications.
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Rao et al. (2026) studied this question.
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