download pdf version of PhD book - Universiteit Utrecht
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6.3 Unsaturated flow modeling<br />
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pressure. The capillary pressure <strong>of</strong> a meniscus is given by the Laplace equation<br />
[Bear, 1988]<br />
P c = P n − P w = γ wn<br />
( 1<br />
r 1<br />
+ 1 r 2<br />
)<br />
= 2γ wn<br />
r ∗ (6.8)<br />
where r ∗ is the mean radius <strong>of</strong> curvature. For a capillary tube <strong>of</strong> radius r,<br />
we have r ∗ = r/ cos(θ) (Young-Laplace’s equation), in which θ is the contact<br />
angle between fluid interface and the capillary wall. The invading fluid enters<br />
and fills a pore throat only when the injection pressure equals or exceeds to or<br />
larger than the entry capillary pressure <strong>of</strong> the pore.<br />
We assume that the wetting phase is everywhere hydraulically connected. This<br />
means that there will be no trapping <strong>of</strong> the wetting phase, as it can always<br />
escape along the edges. The capillary pressure is increased incrementally so<br />
that fluid-fluid interfaces will move only a short distance before coming to rest<br />
in equilibrium at the opening <strong>of</strong> smaller pore throats.<br />
6.3.2 Fluid flow within drained pores<br />
To calculate the flow across the network, we need to calculate the flow <strong>of</strong> water<br />
in saturated pores as well as along edges <strong>of</strong> drained pores. The conductance<br />
<strong>of</strong> an angular drained pore depends on its degree <strong>of</strong> local saturation, which is<br />
directly related to the radius <strong>of</strong> curvature <strong>of</strong> the meniscus formed along the<br />
pore edges. However, Rao<strong>of</strong> and Hassanizadeh [2011a] have shown that if the<br />
conductance is made dimensionless using the radius <strong>of</strong> curvature, then it becomes<br />
independent <strong>of</strong> saturation. They used a numerical solution to calculate<br />
the dimensionless conductances <strong>of</strong> drained pores with scalene triangular cross<br />
section. This was done by numerically solving the dimensionless form <strong>of</strong> the<br />
Navier-Stokes equations and the equation <strong>of</strong> conservation <strong>of</strong> mass. They performed<br />
calculations for a range <strong>of</strong> corner half-angles, from 5 degree to a wide<br />
corner half-angle <strong>of</strong> 75 degrees. Figure (6.4) shows the computed dimensionless<br />
conductance as a function <strong>of</strong> corner half-angle.<br />
The dimensional form <strong>of</strong> conductance, g, which is a function <strong>of</strong> capillary pressure,<br />
is<br />
g = g ∗ r4 c<br />
µ<br />
(6.9)<br />
where r c is the radius <strong>of</strong> curvature <strong>of</strong> the interface and µ is the wetting fluid<br />
viscosity. The radius <strong>of</strong> curvature r c depends on the capillary pressure prevaling<br />
139