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A homogenised model for the motion of evaporating fronts in porous media

Published online by Cambridge University Press:  23 January 2023

Ellen K. Luckins*
Affiliation:
Mathematical Institute, University of Oxford, Woodstock Road, Oxford OX2 6GG, UK
Christopher J. W. Breward
Affiliation:
Mathematical Institute, University of Oxford, Woodstock Road, Oxford OX2 6GG, UK
Ian M. Griffiths
Affiliation:
Mathematical Institute, University of Oxford, Woodstock Road, Oxford OX2 6GG, UK
Colin P. Please
Affiliation:
Mathematical Institute, University of Oxford, Woodstock Road, Oxford OX2 6GG, UK
*
*Correspondence author. Email: luckins@maths.ox.ac.uk
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Abstract

Evaporation within porous media is both a multiscale and interface-driven process, since the phase change at the evaporating interfaces within the pores generates a vapour flow and depends on the transport of vapour through the porous medium. While homogenised models of flow and chemical transport in porous media allow multiscale processes to be modelled efficiently, it is not clear how the multiscale effects impact the interface conditions required for these homogenised models. In this paper, we derive a homogenised model, including effective interface conditions, for the motion of an evaporation front through a porous medium, using a combined homogenisation and boundary layer analysis. This analysis extends previous work for a purely diffusive problem to include both gas flow and the advective–diffusive transport of material. We investigate the effect that different microscale models describing the chemistry of the evaporation have on the homogenised interface conditions. In particular, we identify a new effective parameter, $\mathcal{L}$, the average microscale interface length, which modifies the effective evaporation rate in the homogenised model. Like the effective diffusivity and permeability of a porous medium, $\mathcal{L}$ may be found by solving a periodic cell problem on the microscale. We also show that the different microscale models of the interface chemistry result in fundamentally different fine-scale behaviour at, and near, the interface.

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Type
Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© The Author(s), 2023. Published by Cambridge University Press
Figure 0

Figure 1. Schematic showing the regions of pore space saturated with liquid (blue) and gas mixture (yellow). The solid microstructure is illustrated by the grey circles. The pore lengthscale, d, and macro-lengthscale, l, are shown; in reality, $\epsilon=d/l$ would be much smaller than in the schematic.

Figure 1

Figure 2. Schematic showing the macroscale evaporating interface, at $Z=0$ in the moving coordinate system, with the outer, intermediate and inner regions for the boundary layer analysis.

Figure 2

Figure 3. Schematics of the microscale cells regions. Left: the cell $\omega_f(t)=[-1/2,1/2]^2\setminus \omega_s(t)$ for the outer and intermediate regions. Right: the inner cell $\omega_{{\mathcal{H}}}$ formed of the region between $z={{\mathcal{H}}}(x,t)$ and $\Gamma$, $x\in[-1/2,1/2]$, excluding the solid structure $\omega_s(t)$. In the analysis we consider the limit as the height of $\Gamma$ increases, so that $\omega_{{\mathcal{H}}}$ becomes semi-infinite in z. The solid inclusions $\omega_s(t)$ (shown as grey circles) move up through both cells at speed $H_T$, so that the cells are periodic in time t with period $1/H_T$.

Figure 3

Figure 4. Schematic showing the liquid region $\omega_l$, consisting of the pore space between $z=-1$ and $z={{\mathcal{H}}}^{(0)}$.

Figure 4

Figure 5. Summary of the results of the analysis of the advection–diffusion problem, at each order and in each region of the domain. The red arrows show the matchings leading to the effective interface conditions: the horizontal arrows at O(1) illustrate the leading-order vapour density matchings (for the chemistry interface condition that we will consider later in Section 4), and the diagonal arrows show the leading-order vapour flux matchings.

Figure 5

Table 1. Summary and comparison of the main results of the chemistry interface condition, for each range of $\alpha$

Figure 6

Figure 6. Microscale interface motion for different pore-scale geometries. The interface shape $t=f(x,y)$, or level sets of the f, are shown in blue at a number of times. The characteristics or rays are straight lines, shown in green. Left: for a diamond-shaped solid obstacle, the solution is given explicitly by (4.19). Centre and right: sketch of two different geometries with the same porosity, but different time period and average interface length $\mathcal{L}$.