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Effect of Gas Dissolution on Heavy Oil Well Performance: Rheology Considerations

机译:气体溶解对重油井性能的影响:流变考虑因素

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Crude oils may exhibit shear rate dependent viscosity under reservoir temperature and pressure conditions due to many factors such as wax content, asphaltenes, solids, and water droplets. In a previous experimental study we investigated the shear rate- shear stress relationship for heavy crude oil using capillary viscometer. The study showed mildly non-Newtonian behavior of heavy oil and the rheological power-law parameters (flow behavior index and flow consistency) depend on the extent of gas dissolution and at higher gas dissolution the fluid flow behavior index approaches unity. Impact of non-Newtonian flow behavior on oil inflow performance can be significant. In this study, a two dimensional unsteady state model is developed to represent the multiphase flow behavior of heavy oil, accounting for the non-Newtonian behavior and the model is solved using a fully implicit finite difference scheme. In essence, the approach is that of a traditional black oil type of reservoir modeling, but with the viscosity of the heavy oil represented by a power law model. Power law parameters for saturated oil at high temperature and different pressures, obtained from experiments in a companion study are used in modeling the rheology of heavy oil. Modified Darcy’s law is used to model non-Newtonian flow of heavy oil through porous media. Results of the numerical solution are validated with analytical solution of single phase non-Newtonian flow through porous media available in the literature. Non-Newtonian behavior under reservoir conditions can increase the pressure drawdown required for production by several times and hence affect the production. The well inflow performance calculated using the simulator shows that, as the exponent of the power law model decreases, the production flow rate decreases. Thus, in comparison to a Newtonian behavior, a power law behavior results in a poorer inflow performance. The results presented here may be used to explain higher recoveries in heavy oils which display non-Newtonian behavior. Additionally, strategies for production optimization could be achieved by controlling the fluid rheology and hence the power law parameters by maintaining solution gas in the oil phase.
机译:由于许多因素,如蜡含量,沥青质,固体和水滴,原油可能在储层温度和压力条件下表现出剪切速率粘度。在先前的实验研究中,我们研究了使用毛细管粘度计的重原油的剪切速率 - 剪切应力关系。该研究表明了重油的温和非牛顿行为和流变能力 - 法律参数(流动行为指数和流动稠度)取决于气体溶解的程度,并且在较高的气体溶解中,流体流动行为指数接近统一。非牛顿流动行为对石油流入性能的影响可能是显着的。在这项研究中,开发了二维不稳定状态模型以表示重油的多相流动行为,占非牛顿行为的核算,并且使用完全隐含的有限差分方案来解决模型。从本质上讲,该方法是传统的黑色油漆储层建模,但随着电力法模型所代表的重油的粘度。饱和油在伴随研究中的实验中获得的高温和不同压力的饱和律参数用于建模重油的流变学。改进的达西法律用于通过多孔介质模拟非牛顿重油流。通过文献中可用的多孔介质,用单相非牛顿流的分析解决方法验证了数值溶液的结果。储层条件下的非牛顿行为可以增加几次生产所需的压力缩减,从而影响生产。使用模拟器计算的井流入性能表明,随着电力法模型的指数降低,生产流量降低。因此,与牛顿行为相比,权力法行为导致较差的流入性能。此处呈现的结果可用于解释显示非牛顿行为的重油中的更高回收率。另外,通过控制流体流变学,可以通过在油相中维持溶液气体来实现生产优化的策略。

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