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Numerical modeling of CO_2 diffusion into water-oil liquid system using moving mesh technique

机译:移动网格技术对CO_2扩散到水油体系中的数值模拟

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摘要

A new diffusion model is developed to study the mass diffusion of CO2 in the water-oil liquid system. The diffusion stages are divided by the position of diffused CO2 front in the liquid system. The 1st and 2nd diffusion stages are performed to characterize the CO2 diffusion in individual oil phase and in water-oil liquid system, respectively. The Peng-Robinson equation of state combined with the diffusion model of two stages are developed to describe the diffusion process of CO2 in the water-oil liquid system. The developed model is validated by matching the pressure changes results of model calculation with an experimental acquisition. Besides, a moving mesh technique is applied to determine the oil swelling effect caused by the CO2 diffusion. The results indicate that both CO2 concentration profiles and oil swelling effect exhibit distinct characteristics at different stages. The CO2 distributes only in the oil phase at the 1st diffusion stage but presents simultaneously in both water and oil phases at the 2nd diffusion stage. The oil swelling factors are 0.90% and 10.84% at the end of the 1st (t = 12.8 h) and 2nd (t = 512.8 h) diffusion stages, respectively.
机译:研究了一种新的扩散模型,以研究CO 2在水-油液系统中的质量扩散。扩散阶段除以液体系统中扩散的CO2前沿的位置。进行第一和第二扩散阶段以表征CO2在各个油相和水-油液系统中的扩散。结合两个阶段的扩散模型,建立了Peng-Robinson状态方程,描述了CO2在水-油液系统中的扩散过程。通过将模型计算的压力变化结果与实验采集结果相匹配来验证开发的模型。此外,应用移动网格技术来确定由CO2扩散引起的油溶胀效果。结果表明,CO2浓度曲线和油溶胀效应在不同阶段均表现出不同的特征。 CO2在第一个扩散阶段仅分布在油相中,而在第二个扩散阶段同时在水相和油相中都存在。在第一个(t = 12.8 h)和第二个(t = 512.8 h)扩散阶段结束时,油溶胀因子分别为0.90%和10.84%。

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