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Heat and mass transfer in unsaturated porous media at a hot boundary: I. One-dimensional analytical model

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Abstract

We present a model of heat and mass transfer in an unsaturated zone of sand and silty clay soils, taking into account the effects of temperature gradients on the advective flux, and of the enhancement of thermal conduction by the process of latent heat transfer through vapor flow. The motivation for this study is to supply information for the planned storage of thermal energy in unsaturated soils and for hot waste storage. Information is required on the possibility of significant drying at a hot boundary, as this would reduce the thermal conductivity of a layer adjacent to the boundary and, thus, prevent effective heat transfer to the soil. This study indicates the possibility that the considered system may be unstable, with respect to the drying conditions, with the occurrence of drying depending on the initial and the boundary conditions. An analysis performed for certain boundary conditions of heat transfer and for given soil properties, disregarding the advective flux of energy, indicated that there are initial conditions of water content for which heating will not cause significant drying. Under these conditions, fine soils may be better suited for heat transfer at the hot boundary, due to their higher field capacity, although their heat conduction coefficients at saturation are lower than those of sandy soils. At present, these conclusions are limited to the range of 50–80°C. Potential effects of solute concentration at the hot boundary are indicated.

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Abbreviations

a :

dry air

gw :

gas-water

g :

gas

s :

solid

w :

water

v :

vapor

vs :

saturated vapor

pm :

porous medium

c :

concentration of solutes

D v g :

coefficient of molecular diffusion of the vapor in the gas

E :

rate of evaporation

E gs :

rate of heat exchange from the gas to the solid phase

E ws :

rate of heat exchange from the water to the solid phase

f 1,f 0 :

shape factors

F T , F θ w :

enhancement coefficients of vapor flow

g :

gravity acceleration

J v gi :

ith component of the diffusive mass flux of the vapor in the gas (per unit area of the porous medium)

J H αi :

ith component of the conductive heat flux in the α-phase (per unit area of the porous medium)

k αij :

ijth component of the effective permeability tensor in the α-phase

k β αij :

ijth component of the tensor representing the effect of pressure and gravity in the α-phase on the advection in the β-phase

K ψ,T :

effective hydraulic conductivity of the soil

L :

latent heat of vaporization

n :

porosity

p α :

pressure in the α-phase

q αi :

ith component of the volumetric advective flux of the α-phase

q T αi :

ith component of the temperature driven part of the volumetric advective flux of the α-phase

q P αi :

ith component of the pressure driven part of the volumetric advective flux of the α-phase

T * αij :

ijth component of the tortuosity tensor in the α-phase

t :

time

T :

temperature

u α :

internal energy in the α-phase (per unit mass of the phase)

x, y, z :

Cartesian coordinates

ɛ ij :

ijth component of the enhancement coefficient of vapor flow

μ α :

dynamic viscosity of the α-phase

v α :

kinematic viscosity of the α-phase

ρ α :

mass density of the α-phase

θ α :

volumetric fraction of the α-phase

θ αs :

volumetric fraction of the α-phase at saturation

Ψ:

matric potential (suction)

Ψ s :

value of the matric potential at saturation

λ α :

thermal conductivity of the α-phase

Λ pm :

overall thermal conductivity of the porous medium

σgw :

gas-water surface tension

X αβ ij :

ijth component of the transformation tensor between an (volume) average performed over the REV and a (surface) average performed over the α-β interface

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Bear, J., Bensabat, J. & Nir, A. Heat and mass transfer in unsaturated porous media at a hot boundary: I. One-dimensional analytical model. Transp Porous Med 6, 281–298 (1991). https://doi.org/10.1007/BF00208954

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  • DOI: https://doi.org/10.1007/BF00208954

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