2010
DOI: 10.1016/j.micromeso.2010.08.011
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Simplified local density model for adsorption of pure gases on activated carbon using Sutherland and Kihara potentials

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Cited by 22 publications
(17 citation statements)
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“…According to the previous analysis, clay and organic materials are mainly responsible for the gas adsorption on shale. It has also been known that the total amount of adsorbed methane is directly proportional to the organic matter content and the kerogen type of the shale (Jenkins and Boyer 2008;Prasad et al 2009;Elgmati et al 2011;Zhang et al 2012). In this study, kerogen types I, II and III were modelled with the SLD-PR model.…”
Section: Sld-pr Model Represents the Gas Adsorption On Clay Minerals mentioning
confidence: 99%
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“…According to the previous analysis, clay and organic materials are mainly responsible for the gas adsorption on shale. It has also been known that the total amount of adsorbed methane is directly proportional to the organic matter content and the kerogen type of the shale (Jenkins and Boyer 2008;Prasad et al 2009;Elgmati et al 2011;Zhang et al 2012). In this study, kerogen types I, II and III were modelled with the SLD-PR model.…”
Section: Sld-pr Model Represents the Gas Adsorption On Clay Minerals mentioning
confidence: 99%
“…The value of acentric factor w is 0.0113 (Gasem et al 2001). The density r and energy parameter a of the adsorbed gas are position dependent, meaning that these parameters vary with coordinate Z; the fugacity of the adsorbed gas phase can be calculated using the following equation (Hasanzadeh et al 2010;Chareonsuppanimit et al 2012):…”
Section: Sld Modelmentioning
confidence: 99%
“…Simulation of methane adsorption in diverse organic pores in shale reservoirs with multi-period… During adsorption, methane density is always higher at the position where the potential energy is the lowest (Liu et al 2018;Charoensuppanimit et al 2015;Hasanzadeh et al 2010). There are peak densities at symmetrical positions at both ends and inside the slit-shaped pore methane density distribution curve because the potential energy of the pore wall is strongest near the pore wall region.…”
Section: Methane Adsorption Characteristics Of Different Pore Typesmentioning
confidence: 99%
“…The value of the acentric factor ω is 0.0113 for methane (Peng et al 1976). The fugacity of adsorbed gas phase can be calculated by the equation (Fitzgerald et al 2003;Hasanzadeh et al 2010): (17) The covolume b needs to be adjusted for describing the repulsive interaction of adsorbed fluid under high pressure. Then the equation (17) becomes: We used the expression introduced by Chen et al to obtain a ads (z) (Chen et al 1997).…”
Section: Sld Modelmentioning
confidence: 99%