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download pdf version of PhD book - Universiteit Utrecht

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6.3 Unsaturated flow modeling<br />

. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .<br />

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

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