Liquid-liquid equilibria of the system 1-(2-hydroxyethyl)-3-methylimidozolium tetrafluoroborate or 1-(2-hydroxyethyl)-2,3-dimethylimidozolium tetrafluoroborate plus water plus 1-butanol at 293.15 K
文献类型：期刊论文
| 作者 | Hu, XS; Yu, J; Liu, HZ |
| 刊名 | JOURNAL OF CHEMICAL AND ENGINEERING DATA
 |
| 出版日期 | 2006-03-01 |
| 卷号 | 51期号:2页码:691-695 |
| 关键词 | temperature ionic liquids phase-behavior chloride plus ethanol plus benzene plus t=298.2 k mixtures hexafluorophosphate imidazolium alkane |
| ISSN号 | 0021-9568 |
| 其他题名 | J. Chem. Eng. Data |
| 中文摘要 | Liquid-liquid equilibrium data are presented for mixtures of 1-(2-hydroxyethyl)-3-methylimidazolium tetrafluoroborate ([C(2)OHmim]BF4) or 1-(2-hydroxyethyl)-2,3-dimethylimidazolium tetrafluoroborate ([C(2)OHdmim]BF4) + water + 1-butanol at 293.15 K. The data presented provide valuable insight into how the environmentally friendly ionic liquid solvent can be used to separate 1-butanol and water. Selectivity values, derived from the tie line data, show that [C(2)OHdmim]BF4 has better extraction capacity than [C(2)OHmim]BF4. The experimental results show that the two ionic liquids are potentially candidates to separate 1-butanol and water by liquid-liquid extraction. The experimental tie lines were correlated with the NTRL equation. |
| 英文摘要 | Liquid-liquid equilibrium data are presented for mixtures of 1-(2-hydroxyethyl)-3-methylimidazolium tetrafluoroborate ([C(2)OHmim]BF4) or 1-(2-hydroxyethyl)-2,3-dimethylimidazolium tetrafluoroborate ([C(2)OHdmim]BF4) + water + 1-butanol at 293.15 K. The data presented provide valuable insight into how the environmentally friendly ionic liquid solvent can be used to separate 1-butanol and water. Selectivity values, derived from the tie line data, show that [C(2)OHdmim]BF4 has better extraction capacity than [C(2)OHmim]BF4. The experimental results show that the two ionic liquids are potentially candidates to separate 1-butanol and water by liquid-liquid extraction. The experimental tie lines were correlated with the NTRL equation. |
| WOS标题词 | Science & Technology ; Physical Sciences ; Technology |
| 类目[WOS] | Chemistry, Multidisciplinary ; Engineering, Chemical |
| 研究领域[WOS] | Chemistry ; Engineering |
| 关键词[WOS] | TEMPERATURE IONIC LIQUIDS ; PHASE-BEHAVIOR ; CHLORIDE PLUS ; ETHANOL PLUS ; BENZENE PLUS ; T=298.2 K ; MIXTURES ; HEXAFLUOROPHOSPHATE ; IMIDAZOLIUM ; ALKANE |
| 收录类别 | SCI |
| 原文出处 | |
| 语种 | 英语 |
| WOS记录号 | WOS:000236005000071 |
| 公开日期 | 2013-10-24 |
| 版本 | 出版稿 |
| 源URL | [http://ir.ipe.ac.cn/handle/122111/4006]  |
| 专题 | 过程工程研究所_研究所（批量导入） |
| 作者单位 | 1.Chinese Acad Sci, Inst Proc Engn, Lab Separat Sci & Engn, Beijing 100080, Peoples R China 2.Chinese Acad Sci, Grad Sch, Beijing 100039, Peoples R China |
| 推荐引用方式 GB/T 7714 | Hu, XS,Yu, J,Liu, HZ. Liquid-liquid equilibria of the system 1-(2-hydroxyethyl)-3-methylimidozolium tetrafluoroborate or 1-(2-hydroxyethyl)-2,3-dimethylimidozolium tetrafluoroborate plus water plus 1-butanol at 293.15 K[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA,2006,51(2):691-695. |
| APA | Hu, XS,Yu, J,&Liu, HZ.(2006).Liquid-liquid equilibria of the system 1-(2-hydroxyethyl)-3-methylimidozolium tetrafluoroborate or 1-(2-hydroxyethyl)-2,3-dimethylimidozolium tetrafluoroborate plus water plus 1-butanol at 293.15 K.JOURNAL OF CHEMICAL AND ENGINEERING DATA,51(2),691-695. |
| MLA | Hu, XS,et al."Liquid-liquid equilibria of the system 1-(2-hydroxyethyl)-3-methylimidozolium tetrafluoroborate or 1-(2-hydroxyethyl)-2,3-dimethylimidozolium tetrafluoroborate plus water plus 1-butanol at 293.15 K".JOURNAL OF CHEMICAL AND ENGINEERING DATA 51.2(2006):691-695. |
入库方式： OAI收割
来源：过程工程研究所
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