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5. Pore-Network Modeling <strong>of</strong> Two-Phase Flow<br />

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

5.4.2.2 Relative permeability for a carbonate rock<br />

In this section, we are applying the new formulation to a network which is based<br />

on the statistical properties <strong>of</strong> a carbonate rock. Al-Kharusi and Blunt [2008]<br />

applied a methodology to extract networks from pore space images <strong>of</strong> carbonate<br />

rock samples, in order to make predictions <strong>of</strong> multiphase transport properties.<br />

They started with a 2D thin-section image; then, converted it statistically<br />

to a 3D representation <strong>of</strong> the pore space. Using concept <strong>of</strong> maximal ball [Al-<br />

Kharusi and Blunt, 2008, 2007], they constructed a 3D pore-network model and<br />

simulated primary drainage, waterflooding, and secondary drainage processes<br />

[Valvatne and Blunt, 2004]. In that model, the resistance to flow was assigned<br />

to pore throats only. The simulated results were compared to the laboratorymeasured<br />

values obtained though centrifuge experiments. The good agreement<br />

for capillary pressure-saturation and intrinsic permeability implied that they<br />

had estimated pore and throat sizes correctly (Figure 5.13). However, the predicted<br />

wetting-phase relative permeability was overestimated compared to the<br />

experimental results, as shown in Figure (5.14). They mentioned the large coordination<br />

number (which was derived using imaging technics) as a potential<br />

reason for discrepancy between relative permeabilities. As another potential<br />

source <strong>of</strong> discrepancy, they mentioned the fact that the pore-network model<br />

did not capture all local heterogeneities <strong>of</strong> the sample due to the size <strong>of</strong> the<br />

network. All <strong>of</strong> these arguments could potentially explain the overestimation<br />

<strong>of</strong> the relative permeability. However, we believe that this discrepancy could<br />

have been minimized by taking into account the resistance to the flow within<br />

(partially-) drained pore bodies. To verify this explanation, we generated a<br />

network with similar properties to those used by Al-Kharusi and Blunt [2008].<br />

The capillary pressure-saturation curves obtained from our network and the<br />

network model <strong>of</strong> Al-Kharusi and Blunt [2008] are shown in Figure (5.13), together<br />

with the P c −S w curve measured in the centrifuge experiments. There is<br />

good agreement between the two pore-network modeling results and measured<br />

values. There is also a good agreement between calculated values <strong>of</strong> absolute<br />

permeability using our network and that <strong>of</strong> Al-Kharusi and Blunt [2008] (Table<br />

5.2). The relative permeability results <strong>of</strong> both pore-network models are shown<br />

in Figure (5.14) together with values obtained from the centrifuge experiments.<br />

It is clear that including the resistance to the flow within pore bodies improves<br />

the agreement between simulated and measured values <strong>of</strong> relative permeability.<br />

An important observation from Figure (5.14) is that the maximum discrepancy<br />

between results from Al-Kharusi and Blunt [2008] and experiments occurs at<br />

116

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