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Effects of Pore Parameters and Functional Groups in Coal on CO(2)/CH(4) Adsorption

[Image: see text] The mechanisms of CO(2)/CH(4) adsorption in coal are the theoretical foundation for CO(2) sequestration in coal seams targeted for enhanced coalbed methane recovery. Herein, by changing the model (low rank coal: WMC, middle rank coal: XM and high rank coal: CZ) with plenty of side...

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Detalles Bibliográficos
Autores principales: Dong, Kui, Zhai, Zhiwei, Guo, Aijun
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8655761/
https://www.ncbi.nlm.nih.gov/pubmed/34901591
http://dx.doi.org/10.1021/acsomega.1c02573
Descripción
Sumario:[Image: see text] The mechanisms of CO(2)/CH(4) adsorption in coal are the theoretical foundation for CO(2) sequestration in coal seams targeted for enhanced coalbed methane recovery. Herein, by changing the model (low rank coal: WMC, middle rank coal: XM and high rank coal: CZ) with plenty of side aliphatic chains and functional groups established in the literature, the influence and mechanism of pore parameters and functional groups(–CH(3), –OH, –C(2)O, –C=O) on the adsorption of CO(2) and CH(4) in different rank coals are systematically studied. Using the Connolly surface algorithm to calculate the pore volume (V(F)) and the specific surface area (S(SA)) of coal with different functional groups, it can be seen that the influence of the functional group change on the pore structure is related to the coal rank. Changing the various functional groups in the original coal structure to a unified functional group (−CH(3), −OH, −C(2)O, or −C=O) will increase the accessible pore volume (V(F)) and the specific surface area (S(SA)), except in low-rank and middle-rank coal, where the ordered arrangement of −C=O will decrease V(F) and S(SA). The adsorption capacities of different pore parameters and functional groups were calculated by Grand Canonical Monte Carlo simulation and density functional theory. On pure adsorption, the pore parameters exert greater influence than the functional groups. By comparing the adsorption energy of the original pore structure containing functional groups and that of modified pores without functional groups, the contributions of the pore structure and original functional groups on CO(2)/CH(4) adsorption are 71 and 29% and 83 and 17%, respectively. Small-diameter pores and −C(2)O have a strong adsorption capacity. In terms of competitive adsorption, the −C=O functional groups and pore diameters ranging from 1.0 to 2.0 nm can significantly enhance the selectivity of CO(2) over CH(4). The CH(4) and CO(2) adsorption does not occur via rigorous monolayer adsorption; multilayer adsorption can occur for CH(4) and CO(2) with pore diameters of 1.0–2.0 and 1.0–2.2 nm, respectively, thus causing micropore filling. These quantitative results establish a foundation for the development of adsorption theory for CO(2)/CH(4) in coal.