Liquid–Liquid Equilibria of Ternary Systems Containing Butyl Acetate, Pentyl Acetate, or Hexyl Acetate + 2-Hydroxyethylammonium Butanoate + Ethanol at 298.15 K

IF 2 3区 工程技术 Q3 CHEMISTRY, MULTIDISCIPLINARY
Renata C. O. Souza, Rafaela R. Pinto, Carlos E. S. Dantas, Ericsem Pereira, Roberta Ceriani*, Silvana Mattedi and Geormenny R. Santos, 
{"title":"Liquid–Liquid Equilibria of Ternary Systems Containing Butyl Acetate, Pentyl Acetate, or Hexyl Acetate + 2-Hydroxyethylammonium Butanoate + Ethanol at 298.15 K","authors":"Renata C. O. Souza,&nbsp;Rafaela R. Pinto,&nbsp;Carlos E. S. Dantas,&nbsp;Ericsem Pereira,&nbsp;Roberta Ceriani*,&nbsp;Silvana Mattedi and Geormenny R. Santos,&nbsp;","doi":"10.1021/acs.jced.4c0045210.1021/acs.jced.4c00452","DOIUrl":null,"url":null,"abstract":"<p >This work studied the liquid–liquid equilibria (LLE) of three ternary systems containing acetates (butyl, pentyl, or hexyl acetate) plus ethanol plus the ionic liquid (IL) 2-hydroxyethylammonium butanoate (2-HEAB) at <i>T</i> = 298.15 K and <i>p</i> = 94.5 kPa. The IL was synthesized using a neutralization reaction. The Fourier-transform infrared spectroscopy (FT-IR) and the nuclear magnetic resonance (NMR) analyses were used to characterize the IL structure. For each ternary system, the equilibrium compositions were determined by a gravimetric method with empirical correlations based on the solubility curve, which was obtained by the cloud point method. The experimental results revealed that the acetate alkyl chain length decreases the system’s partial miscibility area. They also showed that ethanol is distributed preferably in the extract phase (IL-rich) with a partition coefficient (mole basis) of at least 2.5, which is an indicative that 2-HEAB can be used as a solvent for extracting ethanol from acetates, with reasonable values of selectivity (much higher than 1). The binary interaction parameters of the Non-Random Two-Liquid (NRTL) model were adjusted within the LLE experimental data and resulted in root-mean-square deviations up to 1.02%.</p>","PeriodicalId":42,"journal":{"name":"Journal of Chemical & Engineering Data","volume":"70 1","pages":"477–487 477–487"},"PeriodicalIF":2.0000,"publicationDate":"2024-12-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acs.jced.4c00452","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Chemical & Engineering Data","FirstCategoryId":"1","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acs.jced.4c00452","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0

Abstract

This work studied the liquid–liquid equilibria (LLE) of three ternary systems containing acetates (butyl, pentyl, or hexyl acetate) plus ethanol plus the ionic liquid (IL) 2-hydroxyethylammonium butanoate (2-HEAB) at T = 298.15 K and p = 94.5 kPa. The IL was synthesized using a neutralization reaction. The Fourier-transform infrared spectroscopy (FT-IR) and the nuclear magnetic resonance (NMR) analyses were used to characterize the IL structure. For each ternary system, the equilibrium compositions were determined by a gravimetric method with empirical correlations based on the solubility curve, which was obtained by the cloud point method. The experimental results revealed that the acetate alkyl chain length decreases the system’s partial miscibility area. They also showed that ethanol is distributed preferably in the extract phase (IL-rich) with a partition coefficient (mole basis) of at least 2.5, which is an indicative that 2-HEAB can be used as a solvent for extracting ethanol from acetates, with reasonable values of selectivity (much higher than 1). The binary interaction parameters of the Non-Random Two-Liquid (NRTL) model were adjusted within the LLE experimental data and resulted in root-mean-square deviations up to 1.02%.

求助全文
约1分钟内获得全文 求助全文
来源期刊
Journal of Chemical & Engineering Data
Journal of Chemical & Engineering Data 工程技术-工程:化工
CiteScore
5.20
自引率
19.20%
发文量
324
审稿时长
2.2 months
期刊介绍: The Journal of Chemical & Engineering Data is a monthly journal devoted to the publication of data obtained from both experiment and computation, which are viewed as complementary. It is the only American Chemical Society journal primarily concerned with articles containing data on the phase behavior and the physical, thermodynamic, and transport properties of well-defined materials, including complex mixtures of known compositions. While environmental and biological samples are of interest, their compositions must be known and reproducible. As a result, adsorption on natural product materials does not generally fit within the scope of Journal of Chemical & Engineering Data.
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信