Supercritical methane isothermal adsorption model considering multiple adsorption mechanisms in shale

被引:0
|
作者
Liu X. [1 ]
Zhang L. [1 ]
Li S. [2 ]
Zhang J. [3 ]
Zhao Y. [1 ]
Zhang R. [1 ]
Guo J. [1 ]
Tang H. [1 ]
Zhang F. [1 ]
机构
[1] State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southxvest Petroleum University, Sichuan, Chengdu
[2] PetroChina Coalbed Methane Company Limited, Beijing
[3] PetroChina Zhejiang Oilfield Company, Zhejiang, Hangzhou
来源
Shiyou Xuebao/Acta Petrolei Sinica | 2022年 / 43卷 / 10期
关键词
adsorption contribution; isothermal adsorption; multiple adsorption mechanism; shale; supercritical methane;
D O I
10.7623/syxb202210011a
中图分类号
学科分类号
摘要
The research on supercritical methane isothermal adsorption model in shale is of great significance for shale gas reserve assessment, production dynamics prediction and development program preparation. Based on the supercritical methane isothermal adsorption theory and molecular dynamics simulation results, the DA-BET supercritical methane isothermal adsorption model was established considering the differences of adsorption mechanisms in different scale spaces, characterizing the methane molecule adsorption in micropores and mesopores/macro-pores by use of DA micropore filling model and BET multimolecular layer adsorption model, repectively. On this basis, the model fitting method and fitting effect were analyzed using high temperature and high pressure experimental data, and the contribution of different adsorption mechanisms to supercritical methane isothermal adsorption in shale was also explored. The results show that the DA-BET supercritical methane isothermal adsorption model can highly accurately fit the experimental data, and the adsorption characteristic curves obtained by cal-culationsatisfy the uniqueness, and the model can be used to predict the methane adsorption capacity of shale at high temperature. In the low-pressure stage, methane molecules are predominantly adsorbed by micropore filling, temperature and pressure significantly affect the contribution of different adsorption mechanisms to the total adsorption; the lower the temperature and the higher the pressure, the smaller the contribution of micropore filling adsorption to the total adsorption capacity. © 2022 Science Press. All rights reserved.
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页码:1487 / 1499
页数:12
相关论文
共 47 条
  • [31] ZUO Luo, HU Zhiming, CUI Yaxing, Et al., High temperature and pressure methane adsorption characteristics and adsorption kinetics of shale, Journal of China Coal Society, 41, 8, pp. 2017-2023, (2016)
  • [32] DUAN Xianggang, HU Zhiming, GAO Shusheng, Et al., Shale high pressure isothermal adsorption curve and the production dynamic experiments of gas well [J], Petroleum Exploration and Development, 45, 1, pp. 119-127, (2018)
  • [33] XIONG Jian, LIU Xiangjun, LIANG Lixi, Molecular simulation on the adsorption behaviors of methane in montmorillonite slit pores, Acta Petrolei Sinica, 37, 8, pp. 1021-1029, (2016)
  • [34] ZHAO Tianyi, Study on storage and microscale seepage mechanism of shale gas, (2018)
  • [35] DUBININ M M, ASTAKHOV V A., Development of the concepts of volume filling of micropores in the adsorption of gases and vapors by microporous adsorbents, Russian Chemical Bulletin, 20, 1, pp. 3-7, (1971)
  • [36] XIONG Jian, LIU Xiangjun, LIANG Lixi, Isothermal adsorption model of .supercritical methane in shale, Petroleum Drilling Techniques, 43, 3, pp. 96-102, (2015)
  • [37] FENG Guangjun, High-temperature High-pressure methane adsorption and shale gas occurrence in Lower Cambrian shale, Upper Yangtze area, (2020)
  • [38] DUBININ M M., The potential theory of adsorption of gases and vapors for adsorbents with energetically nonuniform surfaces, Chemical Reviews, 60, 2, pp. 235-241
  • [39] AMANKWAH K A G, SCHWARZ J A., A modified approach for estimating pseudo-vapor pressures in the application of the Dubinin-Astakhov equation, Carbon, 33, 9, pp. 1313-1319, (1995)
  • [40] REICH R, ZIEGLER W T, ROGERS K A., Adsorption of methane, ethane, and ethylene gases and their binary and ternary mixtures and carbon dioxide on activated carbon at 212-301K and pressures to 35 atmospheres, Industrial Engineering Chemistry Process Design and Development, 19, 3, pp. 336-344, (1980)