Direct Energy Minimization Algorithm for Numerical Simulation of Carbon Dioxide Injection

L. Khakimova, A. Isaeva, V. Dobrozhanskiy, Y. Podladchikov
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Abstract

We discuss numerical simulation of carbon dioxide injection considered by oil and gas companies. Complex behavior of multicomponent reservoir fluids mixed with carbon dioxide may cause the occurrence of vapor-liquid-liquid equilibria (VLLE), salt precipitation in aquifers, pore-clogging, etc. We propose a simple algorithm for phase equilibria calculations based on the minimization of the multicomponent system free energy. This algorithm can be used to calculate phase separations and component partitioning between the phases under various conditions (critical region, two- and three-phase equilibria, etc.). We demonstrate the applicability of the proposed algorithm in a series of calculations. We consider binary and ternary mixtures that include carbon dioxide and hydrocarbons. We examine the algorithm in two- and three-phase equilibrium calculations and compare its performance with the popular iterative fugacity equilibration technique. We show that both calculation techniques give near-identical results for the considered mixtures. Thus, we show that the free energy minimization algorithm can be used interchangeably with the fugacity equilibration technique for calculating phase equilibria. This algorithm is applicable for VLLE calculations, which is important when considering multicomponent reservoir fluids that include carbon dioxide.
二氧化碳喷射数值模拟的直接能量最小化算法
讨论了油气公司考虑的二氧化碳注入数值模拟问题。多组分储层流体与二氧化碳混合的复杂行为可能导致气液液平衡(VLLE)、含水层盐沉淀、孔隙堵塞等现象的发生。我们提出了一种基于多组分系统自由能最小化的相平衡计算的简单算法。该算法可用于计算各种条件下(临界区、两相平衡和三相平衡等)的相分离和相之间的组分分配。我们在一系列的计算中证明了所提出算法的适用性。我们考虑二元和三元混合物,包括二氧化碳和碳氢化合物。我们在两相和三相平衡计算中考察了该算法,并将其性能与流行的迭代逸度平衡技术进行了比较。我们表明,这两种计算技术给出了几乎相同的结果为考虑的混合物。因此,我们证明了自由能最小化算法可以与逸度平衡技术交替使用来计算相平衡。该算法适用于VLLE计算,这在考虑包含二氧化碳的多组分油藏流体时非常重要。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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