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structural geology, propagation mechanics and - Stanford School of ...

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5.2. Reservoir production<br />

A st<strong>and</strong>ard five-spot production-well configuration—square, with central injector <strong>and</strong><br />

producers at the corners—was used to simulate two-phase (oil-water) incompressible<br />

flow within the b<strong>and</strong> pattern. Two case scenarios were modeled using the same 5.5-acre<br />

pattern (150 m on a side)—the only difference being a 45° rotation <strong>of</strong> the production-<br />

wells about a fixed injector location (Figure 7.8). In Case 1, the straight-line path from<br />

injector to two <strong>of</strong> the producers runs generally along the dominant b<strong>and</strong> trend, while the<br />

path to the two other producers runs generally across it. In Case 2, the straight-line paths<br />

from injector to all four producers run oblique to the dominant b<strong>and</strong> trend. For both cases,<br />

we specified complete initial saturation <strong>of</strong> the pore volume with oil, exact balance at all<br />

times between the total volume <strong>of</strong> water injected <strong>and</strong> the total volume <strong>of</strong> fluid produced,<br />

<strong>and</strong> equal pressure at all four production wells. A total injection/pumping rate <strong>of</strong> 15.9<br />

m 3 /day was used <strong>and</strong> both simulations were run for 250 days, yielding a total pore volume<br />

injected (PVI) <strong>of</strong> 0.15 (i.e. 15% <strong>of</strong> the total model pore volume). Relative permeability<br />

was accounted for using representative data for light crude oil (viscosity 2 cp) as the<br />

nonwetting phase <strong>and</strong> formation water (viscosity 1 cp) as the wetting phase in granular<br />

media similar to the Aztec s<strong>and</strong>stone (Table 1). Capillary pressure is neglected in these<br />

simulations, as attempting to include it produced computational problems. The efficient<br />

h<strong>and</strong>ling <strong>of</strong> strong capillary effects may require the modification <strong>of</strong> some <strong>of</strong> our<br />

numerical treatments. The simulation results are presented in Figures 7.9 <strong>and</strong> 7.10.<br />

5.2.1. Results<br />

Figure 7.9 shows equivalent saturation-map snapshots for the two simulations at<br />

approximately 0.03, 0.09 <strong>and</strong> 0.15 PVI. In both cases, the elliptical patterns <strong>of</strong> water<br />

infiltration that develop suggest a strong tendency toward preferred transport along the<br />

dominant b<strong>and</strong> trend. Judging from the aspect ratios <strong>of</strong> the infiltration patterns, the<br />

transport rate along the b<strong>and</strong> trend exceeds that across it by at least a factor <strong>of</strong> two. This<br />

effect results in early breakthrough <strong>of</strong> water to the production wells oriented along the<br />

b<strong>and</strong> trend from the injector in Case 1 at < 0.03 PVI (Figure 7.9a). For Case 2, significant<br />

breakthrough does not occur until 0.09 PVI (Figure 7.9b). These diverging results are<br />

clearly reflected at 0.15 PVI (Figure 7.9c), when the substantially greater area <strong>of</strong> water<br />

infiltration for Case 2 illustrates that 56% more oil has been produced than in Case 1.<br />

187

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