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Isobaric Phase Equilibrium of Isopropyl Acetate–Isopropanol–Imidazolium-Based Ionic Liquids at 101.3 kPa
Journal of Chemical & Engineering Data ( IF 2.6 ) Pub Date : 2024-04-10 , DOI: 10.1021/acs.jced.4c00046
Jiaming Zhu 1 , Feihu Li 1 , Xiwei Hu 1 , Qunsheng Li 1 , Hongkang Zhao 1
Affiliation  

This study investigates the phase equilibrium behavior of the isopropyl acetate (IAC)-isopropanol (IPA) azeotrope system at 101.3 kPa in the presence of three different imidazolium-based ionic liquids (ILs) as entrainers, 1-butyl-3-methylimidazolium acetate ([BMIM][Ac]), 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf2]), and 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([HMIM][NTf2]). First, according to the measured vapor–liquid equilibrium (VLE) data of the binary system IAC(1)-IPA(2) and the ternary system IAC(1)-IPA(2)-ILs(3), [BMIM][Ac] in the ternary system produces a strong salting-in effect on IPA, while [BMIM][NTf2] and [HMIM][NTf2] produces a salting-in effect on IAC, and the effect of [BMIM][Ac] is much stronger than [BMIM][NTf2] and [HMIM][NTf2]. This work uses the nonrandom (local) two-liquid equation to correlate the VLE data. The mole fractions of [BMIM][Ac], [BMIM][NTf2], and [HMIM][NTf2] required to exactly eliminate the azeotropic point of the IAC-IPA system are 0.035, 0.144, and 0.206, respectively.

中文翻译:

乙酸异丙酯-异丙醇-咪唑基离子液体在 101.3 kPa 下的等压相平衡

本研究研究了乙酸异丙酯 (IAC)-异丙醇 (IPA) 共沸物体系在 101.3 kPa 下,在三种不同的咪唑基离子液体 (IL) 作为共沸剂(1-丁基-3-甲基咪唑乙酸盐)存在下的相平衡行为。 [BMIM][Ac])、1-丁基-3-甲基咪唑鎓双(三氟甲基磺酰基)亚胺([BMIM][NTf 2 ])和1-己基-3-甲基咪唑鎓双(三氟甲基磺酰基)亚胺([HMIM][NTf 2 ])。首先,根据二元体系IAC(1)-IPA(2)和三元体系IAC(1)-IPA(2)-ILs(3)实测气液平衡(VLE)数据,[BMIM][三元体系中的Ac]对IPA产生较强的盐析作用,而[BMIM][NTf 2 ]和[HMIM][NTf 2 ]对IAC产生盐析作用,[BMIM][Ac的作用]比[BMIM][NTf 2 ]和[HMIM][NTf 2 ]强得多。这项工作使用非随机(局部)二液方程来关联 VLE 数据。精确消除IAC-IPA体系的共沸点所需的[BMIM][Ac]、[BMIM][NTf 2 ]和[HMIM][NTf 2 ]摩尔分数分别为0.035、0.144和0.206。
更新日期:2024-04-10
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