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Modeling Three-Phase Flow during Steam Chamber Rise-Impact of Water Drainage on Oil Production Rate

机译:蒸汽室升水造型水资源引流率的三相流动

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The existing models for steam chamber rise rate ignore the effect of water drainage that can result in three-phase flow near the finger/chamber edge. We hypothesize that a steam finger can be divided into three different regions with different pore scale displacement mechanisms. We develop the flux equations for the three regions by assuming 1) negligible oil flow inside the finger, 2) three-phase flow in the transition zone, and 3) single-phase oil flow beyond the transition zone. We further assume that oil flow is coupled to water flow in the transition zone where the dominanat pore-scale mechanisms are double displacement, coalescence, and film drainage. The model results suggest that fast drainage of water in the transition region enhances the oil displacement rate due to the flow coupling. However, increase of the transition zone thickness, due to slow water drainage, decreases the chamber rise rate because of the decrease in the rate of heat conduction to the cold bitumen.
机译:现有的蒸汽室上升速率模型忽略了可以导致手指/腔室边缘附近的三相流的排水的效果。我们假设蒸汽手指可以分为三个不同的区域,具有不同的孔隙率位移机构。我们通过假设1)在手指内的可忽略不计的油流动,2)在过渡区中的三相流动,3)超出过渡区的单相油流动的助焊剂方程。我们进一步假设油流量与过渡区中的水流相连,其中多米诺孔孔隙机制是双位移,聚结和薄膜排水。模型结果表明,由于流量耦合,过渡区域中的水的快速排水增强了油位移率。然而,由于排水慢,过渡区厚度的增加降低了腔室上升率,因为冷热沥青的热传导速率降低。

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