Room-temperature ionic liquids / Alexia Finotello in Industrial & engineering chemistry research, Vol. 47 N°10 (Mai 2008)  

Public ISBD [article]  inIndustrial & engineering chemistry research > Vol. 47 N°10 (Mai 2008) . - p. 3453–3459 Titre : Room-temperature ionic liquids : temperature dependence of gas solubility selectivity Type de document : texte imprimé Auteurs : Alexia Finotello, Auteur ; Jason E. Bara, Auteur ; Dean Camper, Auteur ; Richard D. Noble, Auteur Année de publication : 2008 Article en page(s) : p. 3453–3459 Note générale : Bibliogr. p. 3459 Langues : Anglais (eng) Mots-clés : CO2  CH4  H2  N2  Bulk fluid solubility Résumé : This study focuses on bulk fluid solubility of carbon dioxide (CO2), methane (CH4), hydrogen (H2), and nitrogen (N2) gases in the imidazolium-based RTILs:  1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([emim][Tf2N]), 1-ethyl-3-methylimidazolium tetrafluoroborate ([emim][BF4]), 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([hmim][Tf2N]), and 1,3-dimethylimidazolium methyl sulfate ([mmim][MeSO4]) as a function of temperature (25, 40, 55, and 70 °C) at near-atmospheric pressures. The experimental behaviors are explained in terms of thermodynamic relationships that account for the negligible vapor pressure of the RTIL as well as the low solubilities of the gases. Results show that, as temperature increases, the solubility of CO2 decreases in all RTILs, the solubility of CH4 remains constant in [emim][Tf2N] and [hmim][Tf2N] but increases in [mmim][MeSO4] and [emim][BF4], and the solubility of N2 and H2 increases. Also, the ideal solubility selectivity (ratio of pure-component solubilities) increases as temperature decreases for CO2/N2, CO2/CH4, and CO2/H2 systems. Experimental values for the enthalpy and entropy of solvation are reported. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie0704142 [article] Room-temperature ionic liquids : temperature dependence of gas solubility selectivity [texte imprimé] / Alexia Finotello, Auteur ; Jason E. Bara, Auteur ; Dean Camper, Auteur ; Richard D. Noble, Auteur . - 2008 . - p. 3453–3459. Bibliogr. p. 3459 Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 47 N°10 (Mai 2008) . - p. 3453–3459 Mots-clés : CO2  CH4  H2  N2  Bulk fluid solubility Résumé : This study focuses on bulk fluid solubility of carbon dioxide (CO2), methane (CH4), hydrogen (H2), and nitrogen (N2) gases in the imidazolium-based RTILs:  1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([emim][Tf2N]), 1-ethyl-3-methylimidazolium tetrafluoroborate ([emim][BF4]), 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([hmim][Tf2N]), and 1,3-dimethylimidazolium methyl sulfate ([mmim][MeSO4]) as a function of temperature (25, 40, 55, and 70 °C) at near-atmospheric pressures. The experimental behaviors are explained in terms of thermodynamic relationships that account for the negligible vapor pressure of the RTIL as well as the low solubilities of the gases. Results show that, as temperature increases, the solubility of CO2 decreases in all RTILs, the solubility of CH4 remains constant in [emim][Tf2N] and [hmim][Tf2N] but increases in [mmim][MeSO4] and [emim][BF4], and the solubility of N2 and H2 increases. Also, the ideal solubility selectivity (ratio of pure-component solubilities) increases as temperature decreases for CO2/N2, CO2/CH4, and CO2/H2 systems. Experimental values for the enthalpy and entropy of solvation are reported. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie0704142

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