Measurement and Correlation of Liquid–Liquid Equilibrium for the Ternary System 1‑Octyl-3-methylimidazolium Tetrafluoroborate + 1‑Ethyl-3-methylimidazolium Tetrafluoroborate + Water
Mixed ionic liquids have excellent physicochemical properties; therefore, they are increasingly used in academic research. The separation of mixed ionic liquids is a key problem for the recycle of ionic liquids, and liquid–liquid extraction is an effective process to separate mixed ionic liquids. Th...
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Veröffentlicht in: | Journal of chemical and engineering data 2024-03, Vol.69 (3), p.1178-1187 |
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container_title | Journal of chemical and engineering data |
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creator | Ba, Jiawei Cui, Xianbao Shen, Xiantong Feng, Tianyang Fu, Taotao Feng, Huisheng |
description | Mixed ionic liquids have excellent physicochemical properties; therefore, they are increasingly used in academic research. The separation of mixed ionic liquids is a key problem for the recycle of ionic liquids, and liquid–liquid extraction is an effective process to separate mixed ionic liquids. The COSMO-SAC model was used to screen solvents to separate the ionic liquid mixture 1-octyl-3-methylimidazolium tetrafluoroborate ([C8mim][BF4]) + 1-ethyl-3-methylimidazolium tetrafluoroborate ([C2mim][BF4]) by liquid–liquid extraction, and water is selected as solvent. The liquid–liquid equilibrium (LLE) data for the ternary system of [C8mim][BF4] + [C2mim][BF4] + water were measured at temperatures of 298.15, 308.15, and 318.15 K under atmospheric pressure. The experimental LLE data were well correlated by the nonrandom two-liquid model. The experimental results show that water is an effective solvent for the separation of the ionic liquid mixture of [C8mim][BF4] and [C2mim][BF4]. |
doi_str_mv | 10.1021/acs.jced.3c00758 |
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The separation of mixed ionic liquids is a key problem for the recycle of ionic liquids, and liquid–liquid extraction is an effective process to separate mixed ionic liquids. The COSMO-SAC model was used to screen solvents to separate the ionic liquid mixture 1-octyl-3-methylimidazolium tetrafluoroborate ([C8mim][BF4]) + 1-ethyl-3-methylimidazolium tetrafluoroborate ([C2mim][BF4]) by liquid–liquid extraction, and water is selected as solvent. The liquid–liquid equilibrium (LLE) data for the ternary system of [C8mim][BF4] + [C2mim][BF4] + water were measured at temperatures of 298.15, 308.15, and 318.15 K under atmospheric pressure. The experimental LLE data were well correlated by the nonrandom two-liquid model. 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Chem. Eng. Data</addtitle><description>Mixed ionic liquids have excellent physicochemical properties; therefore, they are increasingly used in academic research. The separation of mixed ionic liquids is a key problem for the recycle of ionic liquids, and liquid–liquid extraction is an effective process to separate mixed ionic liquids. The COSMO-SAC model was used to screen solvents to separate the ionic liquid mixture 1-octyl-3-methylimidazolium tetrafluoroborate ([C8mim][BF4]) + 1-ethyl-3-methylimidazolium tetrafluoroborate ([C2mim][BF4]) by liquid–liquid extraction, and water is selected as solvent. The liquid–liquid equilibrium (LLE) data for the ternary system of [C8mim][BF4] + [C2mim][BF4] + water were measured at temperatures of 298.15, 308.15, and 318.15 K under atmospheric pressure. The experimental LLE data were well correlated by the nonrandom two-liquid model. The experimental results show that water is an effective solvent for the separation of the ionic liquid mixture of [C8mim][BF4] and [C2mim][BF4].</description><subject>Liquid-Liquid Equilibria and Vapor-Liquid-Liquid Equilibria</subject><issn>0021-9568</issn><issn>1520-5134</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><recordid>eNqNkL1OwzAQxy0EEqWwM3qHFJ_zPaKqfEhFHShijJz4orpyYrCdoUx9BcTj8DZ9EpKWFYnl7qT7_066HyGXwCbAONyIyk3WFcpJWDGWxtkRGUHMWRBDGB2TEeszQR4n2Sk5c27NGItSDiPy_YTCdRYbbD0VraRTYy1q4ZVpqanpXL13Su62X4eBzvqqVWlV19DaWOpXSJdoW2E39HnjPDYUdtvPReU3OgiDBv1qo1WjpPgweoCW6K2odWesKY0VHunVnpgNwX8Tr32z5-SkFtrhxW8fk5e72XL6EMwX94_T23kgIMp8IBJWRZDEmGQAUZRLlGVUpqyM85qDyEBmKU9YLmWeoOCllIBpxkMOeQUsleGYsMPdyhrnLNbFm1VN_3EBrBjkF738YpBf_MrvkesDst-Yrhek3d_xH3BmkCY</recordid><startdate>20240314</startdate><enddate>20240314</enddate><creator>Ba, Jiawei</creator><creator>Cui, Xianbao</creator><creator>Shen, Xiantong</creator><creator>Feng, Tianyang</creator><creator>Fu, Taotao</creator><creator>Feng, Huisheng</creator><general>American Chemical Society</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0001-6080-2628</orcidid><orcidid>https://orcid.org/0000-0003-1881-1509</orcidid></search><sort><creationdate>20240314</creationdate><title>Measurement and Correlation of Liquid–Liquid Equilibrium for the Ternary System 1‑Octyl-3-methylimidazolium Tetrafluoroborate + 1‑Ethyl-3-methylimidazolium Tetrafluoroborate + Water</title><author>Ba, Jiawei ; Cui, Xianbao ; Shen, Xiantong ; Feng, Tianyang ; Fu, Taotao ; Feng, Huisheng</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a148t-a60c4165e6811449dedb4b70b59f21a81d872609dd96ea2bdd1e7823219c107d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Liquid-Liquid Equilibria and Vapor-Liquid-Liquid Equilibria</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ba, Jiawei</creatorcontrib><creatorcontrib>Cui, Xianbao</creatorcontrib><creatorcontrib>Shen, Xiantong</creatorcontrib><creatorcontrib>Feng, Tianyang</creatorcontrib><creatorcontrib>Fu, Taotao</creatorcontrib><creatorcontrib>Feng, Huisheng</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of chemical and engineering data</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ba, Jiawei</au><au>Cui, Xianbao</au><au>Shen, Xiantong</au><au>Feng, Tianyang</au><au>Fu, Taotao</au><au>Feng, Huisheng</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Measurement and Correlation of Liquid–Liquid Equilibrium for the Ternary System 1‑Octyl-3-methylimidazolium Tetrafluoroborate + 1‑Ethyl-3-methylimidazolium Tetrafluoroborate + Water</atitle><jtitle>Journal of chemical and engineering data</jtitle><addtitle>J. Chem. Eng. Data</addtitle><date>2024-03-14</date><risdate>2024</risdate><volume>69</volume><issue>3</issue><spage>1178</spage><epage>1187</epage><pages>1178-1187</pages><issn>0021-9568</issn><eissn>1520-5134</eissn><abstract>Mixed ionic liquids have excellent physicochemical properties; therefore, they are increasingly used in academic research. The separation of mixed ionic liquids is a key problem for the recycle of ionic liquids, and liquid–liquid extraction is an effective process to separate mixed ionic liquids. The COSMO-SAC model was used to screen solvents to separate the ionic liquid mixture 1-octyl-3-methylimidazolium tetrafluoroborate ([C8mim][BF4]) + 1-ethyl-3-methylimidazolium tetrafluoroborate ([C2mim][BF4]) by liquid–liquid extraction, and water is selected as solvent. The liquid–liquid equilibrium (LLE) data for the ternary system of [C8mim][BF4] + [C2mim][BF4] + water were measured at temperatures of 298.15, 308.15, and 318.15 K under atmospheric pressure. The experimental LLE data were well correlated by the nonrandom two-liquid model. The experimental results show that water is an effective solvent for the separation of the ionic liquid mixture of [C8mim][BF4] and [C2mim][BF4].</abstract><pub>American Chemical Society</pub><doi>10.1021/acs.jced.3c00758</doi><tpages>10</tpages><orcidid>https://orcid.org/0000-0001-6080-2628</orcidid><orcidid>https://orcid.org/0000-0003-1881-1509</orcidid></addata></record> |
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source | ACS Publications |
subjects | Liquid-Liquid Equilibria and Vapor-Liquid-Liquid Equilibria |
title | Measurement and Correlation of Liquid–Liquid Equilibrium for the Ternary System 1‑Octyl-3-methylimidazolium Tetrafluoroborate + 1‑Ethyl-3-methylimidazolium Tetrafluoroborate + Water |
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