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