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Dalton Transactions
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ARTICLE
Journal Name
Calculation of isosteric heats of CO2 and CH4 adsorption. The CO2
and CH4 Gas adsorption isotherms at 195, 273, and 298 K were fitted
with a Langmuir-Freundlich equation (Eqn. 3). The isosteric heats of
CO2 and CH4 adsorption were calculated from the Langmuir-
Freundlich fitted isotherms by using the Clausius-Clapeyron
expression (4), in which, P is pressure (atm), N is the amount
adsorbed gas (mmol g-1), Nm is the amount adsorbed gas at
saturation, and b and c are constants.
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Calculation of CO2 separation parameters for the vacuum swing
adsorption (VSA) method. For evaluation of materials for the
separation of CO2 from CH4 and N2 , Bae and Snurr23 suggested the
use of five parameters: (1) CO2 uptake under the adsorption
ads
ads
conditions, N1 (mol kg-1), (2) Working CO2 capacity, ΔN1 = N1
-
N1 (mol kg-1), (3) Regenerability, R = (ΔN1/ N1ads) x 100 (%), (4)
Selectivity under adsorption conditions, α12 = (N1ads/ N2ads)(y2/y1),
des
ads
(5) Sorbent selection parameter, S = (α12ads)2/(α12des)(ΔN1/ ΔN2). Here
N is the adsorbed amount and y is the mole fraction in the gas phase.
Subscripts 1 and 2 indicate the strongly adsorbed component (CO2)
and the weakly adsorbed component (CH4 or N2), respectively. The
selectivity parameters were extracted from the isotherms of CO2,
CH4, and N2 at 298 K, which were fit to the Langmuir-Freundlich
equation (Eqn. 3). The results are presented in Table S2, ESI†.
Conflicts of interest
There are no conflicts to declare.
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Acknowledgments
This work was supported by the National Research Foundation of
Korea (NRF) Grant funded by the Korean Government (MEST; No.
2005-0049412).
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6 | J. Name., 2012, 00, 1-3
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