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Prediction of Adsorption Isotherms of Multicomponent Gas Mixtures in Tight Porous Media by the Oil-Gas-Adsorption Three-Phase Vacancy Solution Model

机译:油气吸附三相空位溶洞模型预测致密多孔介质中多组分气体混合物的吸附等温线

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摘要

For unconventional reservoirs, the effect of adsorption on phase equilibrium cannot be neglected because the process occurs in extremely tight porous media. This work focuses on the adsorption prediction of multicomponent mixture systems in tight porous media with the oil-gas-adsorption three-phase equilibrium model to a gas sample in the literature. The revisited vacancy solution model of adsorption by Bhatia and Ding is introduced to study the adsorption behaviors of the mixture. The gas and adsorbed phases are assumed to be the solutions of adsorbates with a hypothetical solvent called "vacancy", and the vacancy is treated as an additional component engaged in the phase equilibrium in this theory. Instead of using parameters extracted from the multicomponent adsorption data, this method takes advantage because it accurately predicts the gas mixture adsorption equilibrium with consideration of non-ideal behavior in the adsorbed phase from pure gas adsorption isotherms over wide ranges of conditions, which could be efficient in terms of cost and time. It can explain the competitive adsorption phenomenon, which is proven during the adsorption process of the gas mixture. The experimental data in the literature of CH4-C2H6 binary gas mixtures of different compositions with a pressure ranging from 0 to 125 bar under the temperatures of 40, 50, and 60 degrees C are restudied in this work. The prediction results are compared to two other methods, including the extended Langmuir model and the multicomponent potential theory. This method shows an improved precision with less than 5% mean absolute percentage error in all cases. In addition to predications of desorption for the depletion process, the vacancy solution model has the potential in future work to give simulations for other production operations, such as CO2 or N-2 injection for the displacement of hydrocarbons in shales.
机译:对于非常规储层,吸附作用对相平衡的影响不可忽略,因为该过程发生在极其紧密的多孔介质中。这项工作的重点是在文献中利用油气吸附三相平衡模型对致密气孔介质中多组分混合物系统的吸附预测。引入了Bhatia和Ding的吸附空位溶液模型,研究了混合物的吸附行为。假定气相和吸附相是被吸附物与称为“空位”的假设溶剂形成的溶液,并且在该理论中空位被视为参与相平衡的附加组分。代替使用从多组分吸附数据中提取的参数,该方法具有优势,因为它可以在宽范围的条件下根据纯气体吸附等温线准确地预测吸附相中的非理想行为,从而准确预测气体混合物的吸附平衡。在成本和时间方面。它可以解释竞争性吸附现象,这在混合气体的吸附过程中得到了证明。在这项工作中,对文献中不同组成的CH4-C2H6二元气体混合物在40、50和60摄氏度下的压力为0至125 bar的实验数据进行了研究。将预测结果与其他两种方法进行比较,包括扩展的Langmuir模型和多组分势理论。该方法在所有情况下均显示出提高的精度,平均绝对百分比误差小于5%。除了对枯竭过程进行解吸的预测外,空缺解决方案模型还具有在未来的工作中为其他生产操作(例如注入CO2或N-2注入以替代页岩中的碳氢化合物)模拟的潜力。

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  • 来源
    《Energy & fuels》 |2018年第12期|12166-12173|共8页
  • 作者单位

    Yangtze Univ, Hubei Cooperat Innovat Ctr Unconvent Oil & Gas, Wuhan 430100, Hubei, Peoples R China|Univ Regina, Petr Syst Engn, Regina, SK S4S 0A2, Canada;

    Univ Regina, Petr Syst Engn, Regina, SK S4S 0A2, Canada;

    Yangtze Univ, Hubei Cooperat Innovat Ctr Unconvent Oil & Gas, Wuhan 430100, Hubei, Peoples R China;

    Univ Regina, Petr Syst Engn, Regina, SK S4S 0A2, Canada;

    Southwest Petr Univ, Fac Petr Engn, Chengdu 610500, Sichuan, Peoples R China;

    Univ Regina, Petr Syst Engn, Regina, SK S4S 0A2, Canada;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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