2015
DOI: 10.1039/c5ra05745k
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Pure methane, carbon dioxide, and nitrogen adsorption on anthracite from China over a wide range of pressures and temperatures: experiments and modeling

Abstract: The adsorption isotherms and kinetics characteristics were investigated at 294 K, 311 K, 333 K, and 353 K with pressures up to 18 MPa for CH4 and N2 and 5.5 MPa for CO2 on anthracite from China using a volumetric method.

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Cited by 38 publications
(51 citation statements)
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References 54 publications
(93 reference statements)
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“…The absorbed phase densities ρ a for CO 2 and CH 4 were 1.027 and 0.421 g/cm 3 respectively [25][26][27][28][29]. Furthermore, the adsorption capacity of the surface was expressed by n L , and the gas density (when adsorption was half the maximum) was expressed by ρ L .…”
Section: Langmuir + K Modelmentioning
confidence: 99%
See 2 more Smart Citations
“…The absorbed phase densities ρ a for CO 2 and CH 4 were 1.027 and 0.421 g/cm 3 respectively [25][26][27][28][29]. Furthermore, the adsorption capacity of the surface was expressed by n L , and the gas density (when adsorption was half the maximum) was expressed by ρ L .…”
Section: Langmuir + K Modelmentioning
confidence: 99%
“…where ρ t represents the adsorbed phase density in layer t and ρ g represents the bulk phase density. The absorbed phase densities ρ a for CO 2 and CH 4 were assumed to be 1.027 and 0.421 g/cm 3 , respectively [25][26][27][28][29]. In this work, only monolayer adsorption was assumed, for the sake of simplification, and the equation was expressed as ln…”
Section: Ono-kondo Lattice Modelmentioning
confidence: 99%
See 1 more Smart Citation
“…Different hysteresis behavior have been reported, at conditions beyond which capillary condensation can occur, mostly through experimental studies, in methane-coal, carbon dioxide-coal and nitrogen-coal systems [7,[15][16][17]. However, very few literatures exist on shale gas desorption isotherms and by implication, limited resources exist on shale gas sorption hysteresis in spite of the large volume of published work on shale gas adsorption isotherms [7,16,[18][19][20]. While it is not exactly clear why shale gas desorption is not so widely studied like adsorption, despite that it is clearly understood that desorption is akin to shale gas production, it can be speculated that the assumption that the Langmuir isotherm is valid for modeling shale gas sorption processes invariably makes researchers assume that the desorption isotherm should be exactly the same as the adsorption isotherm.…”
Section: Introductionmentioning
confidence: 99%
“…Present study intends to investigate adsorption behavior of methane and carbon dioxide on few Indian shales and also examine applicability of different AI models to adsorption on some Indian shales to find the most accurate AI model. Background of different AI models (Langmuir model, BET model, Dubinin-Astakhov (D-A) model, Dubinin-Radushkevich (D-R) model, and Ono-Kondo model) have been discussed extensively by previous researchers and hence is not included in the manuscript [17,[27][28][29][30][31][32][33][34][35][37][38][39][40][41][42][43][44].…”
Section: Introductionmentioning
confidence: 99%