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Numerical simulation of diverse thermal in situ upgrading processes for the hydrocarbon production from kerogen in oil shale reservoirs

机译:油页岩油藏干酪根生产烃的多种热原位改造过程的数值模拟

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We investigate the productivity and product selectivity of diverse thermal in situ upgrading processes in oil shale reservoirs. In situ upgrading processes applying the ideas of Shell In situ Conversion Process, ExxonMobil Electrofrac, and Texas A&M Steamfrac are simulated by using sector models with the assumption of symmetric patterns. In-house fully functional simulator is used, which has been developed for the kerogen pyrolysis and hydrocarbon production. In the simulation cases, sensitivity analyses to the factors having major influence on the productivity and product selectivity are conducted. The effects of the temperature of vertical heaters, the spacing of hydraulic fractures, and the position of horizontal production wells are analyzed in the applied In situ Conversion Process, Electrofrac, and Steamfrac, respectively. In the applied In situ Conversion Process cases, hydrocarbon production increases with the increasing heater temperature. In the applied Electrofrac cases, hydrocarbon production increases with the increasing spacing of hydraulic fractures, even though longer time period for the process is needed. In the applied Steamfrac cases, the case of production well located at the same depth to the injection well shows the least hydrocarbon production. Among the processes, the applied In situ Conversion Process cases show the highest weight percentage of total hydrocarbon components in the produced fluid, and the applied Electrofrac cases follow it. The applied Steamfrac cases show far lower weight percentage of hydrocarbon production than the other methods. In terms of the mass ratio of produced hydrocarbon to decomposed kerogen, the applied Steamfrac cases show the largest value among the processes by aqueous phase sweeping liquid organic phase, but they also show the huge water oil mass ratio by the continuous injection of hot water. All the applied In situ Conversion Process cases and the Electrofrac case with the short spacing of hydraulic fractures show good heating efficiency by decomposing whole kerogen in the system.
机译:我们调查了油页岩储层中各种热原位改造过程的生产率和产品选择性。采用壳原位转换过程,埃克森美孚Electrofrac和Texas A&M Steamfrac的思想的原位升级过程是通过使用具有对称模式的扇区模型进行模拟的。使用内部全功能模拟器,该模拟器已开发用于干酪根热解和碳氢化合物生产。在模拟情况下,对影响生产率和产品选择性的主要因素进行敏感性分析。在应用的原位转化工艺,Electrofrac和Steamfrac中分别分析了垂直加热器温度,水力压裂间距和水平生产井位置的影响。在应用的原位转化过程中,碳氢化合物的产量随着加热器温度的升高而增加。在应用的Electrofrac情况下,即使需要更长的时间,但随着水力压裂间距的增加,碳氢化合物的产量也会增加。在应用的Steamfrac案例中,与注入井位于同一深度的生产井案例显示出最少的烃产量。在这些过程中,应用的原位转化过程案例显示出产出液中总烃成分的重量百分比最高,而应用的Electrofrac案例紧随其后。应用的Steamfrac案例显示出的碳氢化合物生产的重量百分比远低于其他方法。就产出的烃与分解的干酪根的质量比而言,Steamfrac案例在水相吹扫液态有机相的过程中显示出最大值,但通过连续注入热水也显示出巨大的水油质量比。所有应用的原位转化工艺案例和水力压裂裂缝间距较小的Electrofrac案例均通过分解系统中的整个干酪根显示出良好的加热效率。

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