Solubility of CO2in [1-n-butylthiolanium] [Tf2N] + toluene mixtures: liquid–liquid phase split separation and modelling
Carbon dioxide has been shown to be an effective antisolvent gas for separating organic compounds from ionic liquids (ILs) by inducing a liquid–vapour to liquid–liquid–vapour transition. Using carbon dioxide, toluene can be separated from imidazolium, phosphonium and pyridinum cation-based ILs with...
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Veröffentlicht in: | Philosophical transactions of the Royal Society of London. Series A: Mathematical, physical, and engineering sciences physical, and engineering sciences, 2015-12, Vol.373 (2057), p.1-15 |
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creator | Canales, Roberto I. Lubben, Michael J. Gonzalez-Miquel, Maria Brennecke, Joan F. |
description | Carbon dioxide has been shown to be an effective antisolvent gas for separating organic compounds from ionic liquids (ILs) by inducing a liquid–vapour to liquid–liquid–vapour transition. Using carbon dioxide, toluene can be separated from imidazolium, phosphonium and pyridinum cation-based ILs with the bis(trifluoromethylsulfonyl)imide anion, which is relatively hydrophobic and has a high toluene solubility. A new IL with relatively low viscosity is tested here for the same toluene separation process: 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide. Carbon dioxide solubility in binary and ternary systems containing toluene and 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide is measured at 298.15 and 313.15 K up to 7.4 MPa. Solubility behaviour in this IL is similar to imidazolium-based ILs with the same anion. However, phase split pressures are lower when 1-n-butylthiolanium bis (trifluoromethylsulfonyl)imide is used instead of 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at the same conditions of temperature and initial composition of toluene in the IL. Solubility data are modelled with the conductor-like screening model for real solvents combined with the Soave–Redlich–Kwong equation of state, which provides good qualitative results. |
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Using carbon dioxide, toluene can be separated from imidazolium, phosphonium and pyridinum cation-based ILs with the bis(trifluoromethylsulfonyl)imide anion, which is relatively hydrophobic and has a high toluene solubility. A new IL with relatively low viscosity is tested here for the same toluene separation process: 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide. Carbon dioxide solubility in binary and ternary systems containing toluene and 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide is measured at 298.15 and 313.15 K up to 7.4 MPa. Solubility behaviour in this IL is similar to imidazolium-based ILs with the same anion. However, phase split pressures are lower when 1-n-butylthiolanium bis (trifluoromethylsulfonyl)imide is used instead of 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at the same conditions of temperature and initial composition of toluene in the IL. 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Series A: Mathematical, physical, and engineering sciences</title><description>Carbon dioxide has been shown to be an effective antisolvent gas for separating organic compounds from ionic liquids (ILs) by inducing a liquid–vapour to liquid–liquid–vapour transition. Using carbon dioxide, toluene can be separated from imidazolium, phosphonium and pyridinum cation-based ILs with the bis(trifluoromethylsulfonyl)imide anion, which is relatively hydrophobic and has a high toluene solubility. A new IL with relatively low viscosity is tested here for the same toluene separation process: 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide. Carbon dioxide solubility in binary and ternary systems containing toluene and 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide is measured at 298.15 and 313.15 K up to 7.4 MPa. Solubility behaviour in this IL is similar to imidazolium-based ILs with the same anion. However, phase split pressures are lower when 1-n-butylthiolanium bis (trifluoromethylsulfonyl)imide is used instead of 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at the same conditions of temperature and initial composition of toluene in the IL. Solubility data are modelled with the conductor-like screening model for real solvents combined with the Soave–Redlich–Kwong equation of state, which provides good qualitative results.</description><issn>1364-503X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><sourceid/><recordid>eNqFjLkKwkAURadQcP0E4fUSyK7YimKlhRaCSJiQiXkym7OA6fwH_9AvUdDe6h44nNsh_SjJ0yALk2OPDKy9hmEU5VncJ-1ecV8iR9eCqmG5i1HCKQpkUHrXcteg4lSiF2c4Hep4e4YpuE_CJAOBd-cNswvgePNYvR7PL4BuqGVg9ecWLNPUUIdKApUVCFUxzlFeRqRbU27Z-LdDMlmvDstNcLVOmUIbFNS0RZzOsvksnyf__BvSjko0</recordid><startdate>20151228</startdate><enddate>20151228</enddate><creator>Canales, Roberto I.</creator><creator>Lubben, Michael J.</creator><creator>Gonzalez-Miquel, Maria</creator><creator>Brennecke, Joan F.</creator><general>THE ROYAL SOCIETY</general><scope/></search><sort><creationdate>20151228</creationdate><title>Solubility of CO2in [1-n-butylthiolanium] [Tf2N] + toluene mixtures: liquid–liquid phase split separation and modelling</title><author>Canales, Roberto I. ; Lubben, Michael J. ; Gonzalez-Miquel, Maria ; Brennecke, Joan F.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-jstor_primary_247587683</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Canales, Roberto I.</creatorcontrib><creatorcontrib>Lubben, Michael J.</creatorcontrib><creatorcontrib>Gonzalez-Miquel, Maria</creatorcontrib><creatorcontrib>Brennecke, Joan F.</creatorcontrib><jtitle>Philosophical transactions of the Royal Society of London. Series A: Mathematical, physical, and engineering sciences</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Canales, Roberto I.</au><au>Lubben, Michael J.</au><au>Gonzalez-Miquel, Maria</au><au>Brennecke, Joan F.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Solubility of CO2in [1-n-butylthiolanium] [Tf2N] + toluene mixtures: liquid–liquid phase split separation and modelling</atitle><jtitle>Philosophical transactions of the Royal Society of London. Series A: Mathematical, physical, and engineering sciences</jtitle><date>2015-12-28</date><risdate>2015</risdate><volume>373</volume><issue>2057</issue><spage>1</spage><epage>15</epage><pages>1-15</pages><issn>1364-503X</issn><abstract>Carbon dioxide has been shown to be an effective antisolvent gas for separating organic compounds from ionic liquids (ILs) by inducing a liquid–vapour to liquid–liquid–vapour transition. Using carbon dioxide, toluene can be separated from imidazolium, phosphonium and pyridinum cation-based ILs with the bis(trifluoromethylsulfonyl)imide anion, which is relatively hydrophobic and has a high toluene solubility. A new IL with relatively low viscosity is tested here for the same toluene separation process: 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide. Carbon dioxide solubility in binary and ternary systems containing toluene and 1-n-butylthiolanium bis(trifluoromethylsulfonyl)imide is measured at 298.15 and 313.15 K up to 7.4 MPa. Solubility behaviour in this IL is similar to imidazolium-based ILs with the same anion. However, phase split pressures are lower when 1-n-butylthiolanium bis (trifluoromethylsulfonyl)imide is used instead of 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at the same conditions of temperature and initial composition of toluene in the IL. Solubility data are modelled with the conductor-like screening model for real solvents combined with the Soave–Redlich–Kwong equation of state, which provides good qualitative results.</abstract><pub>THE ROYAL SOCIETY</pub></addata></record> |
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title | Solubility of CO2in [1-n-butylthiolanium] [Tf2N] + toluene mixtures: liquid–liquid phase split separation and modelling |
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