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Application of stability theory and finite element simulation to characterize miscible displacements.

机译:稳定性理论和有限元模拟在表征混相位移中的应用。

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摘要

Hydrodynamic instability, which results in viscous fingering, is a major factor that limits the success of miscible displacement projects in the field. The ability to predict its occurrence would contribute significantly towards the design of stable and efficient miscible projects for enhanced oil recovery.;In this study, a new stability theory was developed to predict the onset of instability during miscible displacement in petroleum reservoirs. Specifically, a universal dimensionless number and its critical value for the onset of instability, were derived. Knowing the pertinent parameters of a proposed miscible project such as viscosity ratio, the density difference, the effective dispersion coefficients, the macroscopic dimensions of the porous medium, and the injection rate, the stability number can be used to predict whether the displacement will be stable or unstable.;With a two-dimensional Galerkin-based Finite Element simulator, systematic numerical studies were conducted to investigate the subsequent behavior of the displacements in homogeneous and heterogeneous porous media for favorable and unfavorable mobility ratios over a wide range of the new dimension less stability number. The results indicate that a favorable mobility ratio displacement is unconditionally stable whereas an unfavorable mobility ratio displacement is conditionally stable. The effect of heterogeneity is to induce some form of macroscopic dispersion which dampens but does not entirely eliminate instabilities, suggesting that displacement in-situ will be unstable if the necessary and sufficient conditions for instability are met.;Further, the results of numerical simulations and reported laboratory experiments using liquid-liquid fluids show good agreement with theory. These results have shed considerable light on the factors that control the phenomenon of instability. Such information can be useful in the optimal design of miscible projects aimed at the minimization of the adverse impact of instability and the achievement of good oil recovery. A consequence of this theory is a model proposed to calculate the optimum size requirements for a solvent slug displacement process.
机译:导致粘性指弹的流体动力学不稳定性是限制该领域中混相驱油项目成功的主要因素。预测其发生的能力将大大有助于设计稳定有效的可混溶项目以提高采油率。在这项研究中,开发了一种新的稳定性理论来预测在石油储层中混相驱替过程中不稳定的发生。具体来说,得出了一个通用的无量纲数及其对于不稳定现象发作的临界值。了解拟议的可混溶项目的相关参数(例如粘度比,密度差,有效分散系数,多孔介质的宏观尺寸和注入速率)后,可以使用稳定性数来预测位移是否稳定用二维基于Galerkin的有限元仿真器进行了系统的数值研究,研究了在较大范围的新尺寸范围内,均质和非均质多孔介质中位移的后续行为对有利和不利迁移率的影响。稳定性数。结果表明,有利的迁移率比位移是无条件稳定的,而不利的迁移率比位移是有条件的稳定。异质性的影响是引起某种形式的宏观分散,这种分散会抑制但不能完全消除不稳定性,这表明,如果满足必要和充分的不稳定性条件,则原位位移将变得不稳定。报道的使用液-液流体的实验室实验与理论相吻合。这些结果为控制不稳定现象的因素提供了可观的启示。此类信息可用于优化混溶项目的设计,以最大程度地减少不稳定的不利影响并实现良好的采油率。该理论的结果是提出了一个模型,用于计算溶剂块置换工艺的最佳尺寸要求。

著录项

  • 作者

    Idigbe, Koso Ignatius.;

  • 作者单位

    The University of Texas at Austin.;

  • 授予单位 The University of Texas at Austin.;
  • 学科 Engineering Petroleum.
  • 学位 Ph.D.
  • 年度 1989
  • 页码 189 p.
  • 总页数 189
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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