Ternary adsorption equilibrium of H-2/CH4/C2H4 onto activated carbon

Authors
Jeong, Byung-ManAhn, Eui-SubYun, Jeong-HoLee, Chang-HaChoi, Dae-Ki
Issue Date
2007-07-01
Publisher
ELSEVIER SCIENCE BV
Citation
SEPARATION AND PURIFICATION TECHNOLOGY, v.55, no.3, pp.335 - 342
Abstract
Adsorption equilibrium data for the pure component H-2, CH4, and C2H4, and their binary and ternary mixtures have been measured on activated carbon. The experimental measurements were done by a static method in the pressures up to 2 MPa at temperatures of 293.15, 303.15, and 313.15 K. Langmuir. Langmuir-Freundlich (L-F), and Flory-Huggins vacancy solution model (F-H VSM) were used to correlate the experimental pure component isotherm data. It was found that the L-F isotherm and F-H VSM show better fitting accuracy than the other isotherm models. Mixture adsorption equilibrium data on the activated carbon were predicted by the extended Langmuir, extended L-F, ideal adsorbed solution theory (IAST), and vacancy solution model (VSM). (c) 2006 Elsevier B.V. All rights reserved.
Keywords
VACANCY SOLUTION THEORY; GAS-MIXTURES; HYDROGEN-PRODUCTION; NATURAL-GAS; BINARY; PREDICTION; NITROGEN; ISOTHERM; EQUATION; METHANE; VACANCY SOLUTION THEORY; GAS-MIXTURES; HYDROGEN-PRODUCTION; NATURAL-GAS; BINARY; PREDICTION; NITROGEN; ISOTHERM; EQUATION; METHANE; activated carbon; mixture gas adsorption; Langmuir; Langmuir-Freundlich; ideal adsorbed solution theory (IAST); vacancy solution model (VSM)
ISSN
1383-5866
URI
https://pubs.kist.re.kr/handle/201004/134275
DOI
10.1016/j.seppur.2006.11.004
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KIST Article > 2007
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