4.7 Article

Competitive adsorption characteristics based on partial pressure and adsorption mechanism of CO2/CH4 mixture in shale pores

Journal

CHEMICAL ENGINEERING JOURNAL
Volume 430, Issue -, Pages -

Publisher

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2021.133172

Keywords

Competitive adsorption; Partial pressure; Heterogeneous surfaces; Adsorption mechanism; Shale gas

Funding

  1. National Natural Science Foundation of China [52076032]
  2. National Key Research and Development Project [2019YFC0312304]
  3. Fundamental Research Funds for the Central Universities [DUT21LAB121]

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Gas partial pressure is found to be the decisive factor in competitive adsorption behavior, and Langmuir equation is applicable for fitting adsorption isotherms in different layers. By controlling the timing and amount of CO2 injection, it is possible to enhance CH4 recovery and CO2 storage effectively.
In the context that CS-EGR technology has received more and more attention, molecular dynamics simulation method was used to analyze the competitive adsorption characteristics and mechanism of CO2/CH4 mixture in graphene-MMT heterogeneous surface pores. In the case of certain temperature and pore size, the gas partial pressure of mixture is found to be the decisive factor of the competitive adsorption behavior. It's better to describe the competitive adsorption behavior by gas partial pressure. Langmuir equation was applied to fitting adsorption isotherm in the first adsorption layer and the second adsorption layer. The good fitting results indicate that although the competitive adsorption mechanism of CO2/CH4 mixture can't be considered as monolayer adsorption due to the existence of multiple adsorption layers, each adsorption layer can be explained by Langmuir adsorption theory. To enhance the CH4 recovery and CO2 storage, the appropriate timing and amount of CO2 injection were proposed. The pressure should be reduced to as low as possible in the first pressure drawdown process, because the first pressure drawdown is obviously beneficial to CH4 production. The Ratio should be controlled not to exceed 1.11 similar to 1.21 when injecting CO2. The operation recommendations can effectively enhance the shale gas recovery and CO2 storage and may help to optimize the design of CS-EGR technology.

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