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Kinematics in a slowly drying porous medium: Reconciliation of pore network simulations and continuum modeling

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Academic year: 2021

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FIG. 1. Sketch of considered drying situation. The top region of size δ represents the external mass transfer boundary layer.
FIG. 2. Sketch of a 3D cubic pore network with the gas-diffusion boundary layer on top.
FIG. 4. Illustration of the various types of throats present in the network during drying.
FIG. 5. Drying curves obtained from PN simulations: (a) the average evapo-rated liquid mass as a function of time, (b) the average normalized evaporation rate (red curve), the normalized evap-oration rate for each realization (solid black curves), the av
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