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Two- and three-hydrocarbon phase streamline-based compositional simulation of gas injections

机译:基于二烃和三烃相流线的注气组成模拟

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摘要

Up to three three-hydrocarbon phases can develop during gas flooding of oil reservoirs at relatively low temperatures. Very few reservoir simulators and none of the published streamline simulators can handle three-hydrocarbon phases. In this work, we have developed a four-phase (including water) compositional streamline module that works with an existing finite-difference simulator to study gas injections. Gravity effects are added using an operator splitting technique. TVD schemes are implemented to construct the numerical solution along streamlines for reducing the impact of numerical dispersion. Two- and three-hydrocarbon phase simulations of gas injections in quarter five-spot models have been demonstrated using this simulator. Breakthrough recovery efficiency increases with the viscous-to-gravity ratio in the range of 1 -100. Gas injection simulation of the reservoir oil indicates that three-hydrocarbon phases exist only near the gas-oil displacement front The gas phase is present in a few grid blocks while the second liquid phase is present in many grid blocks, under the conditions studied.
机译:在温度相对较低的储油层进行气驱过程中,最多可形成三个三烃相。很少有油藏模拟器,没有一个已发布的流线型模拟器能够处理三烃相。在这项工作中,我们开发了一个四相(包括水)成分流线模块,该模块可与现有的有限差分模拟器一起研究气体注入。使用运算符拆分技术添加重力效果。实施TVD方案可沿流线构造数值解,以减少数值离散的影响。使用此模拟器演示了四分之五点模型中注气的两个和三个烃相模拟。突破性回收效率随着粘稠比在1 -100的范围内增加。储层油的注气模拟表明,在烃油驱替锋附近仅存在三个烃相。在研究的条件下,气相存在于几个网格块中,而第二液相存在于许多网格块中。

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