Thermodynamic analysis and separation kinetics of liquid-liquid extraction process in water-organic solvent-Quercetin system

IF 5.5 3区 工程技术 Q1 ENGINEERING, CHEMICAL
Mohd Aurif Shergujri, Gaurav Ashok Bhaduri
{"title":"Thermodynamic analysis and separation kinetics of liquid-liquid extraction process in water-organic solvent-Quercetin system","authors":"Mohd Aurif Shergujri,&nbsp;Gaurav Ashok Bhaduri","doi":"10.1016/j.jtice.2025.106190","DOIUrl":null,"url":null,"abstract":"<div><h3>Background</h3><div>Thermodynamic evaluation of Quercetin distribution in water and organic solvent system is important for the design of Quercetin separation process. Additionally, kinetic analysis of Quercetin distribution has an effect on its separation efficiency. These are useful in designing process for green separation of Quercetin involving aqueous extracts.</div></div><div><h3>Methods</h3><div>The liquid-liquid extraction process has been demonstrated with equilibrium data for water-organic solvent-Quercetin system. This is studied at three different temperatures i.e. 293, 303, and 313 K. The organic solvent mixture used was ethyl acetate-hexane (1:1 v/v). Kinetic studies of the purification process along with its optimisation was done using a stirred tank.</div></div><div><h3>Significant Findings</h3><div>The distribution coefficient of Quercetin was in the range of 9.5–0.78 and the separation factor was in the range of 281.7–22.7. The distribution coefficient and extraction efficiency was not affected with change in temperature. The degree of consistency of the equilibrium was evaluated using Othmer-Tobias equation. Additionally, the kinetic study showed that the mass transfer coefficient was a function of stirrer speed and volumetric ratio of aqueous to organic phase. The maximum mass transfer coefficient of 9.41 min<sup>-1</sup> was obtained for a stirrer speed of 600 rpm and ratio of V<sub>aq</sub>/V<sub>org</sub> of 2.</div></div>","PeriodicalId":381,"journal":{"name":"Journal of the Taiwan Institute of Chemical Engineers","volume":"173 ","pages":"Article 106190"},"PeriodicalIF":5.5000,"publicationDate":"2025-05-17","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of the Taiwan Institute of Chemical Engineers","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1876107025002433","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0

Abstract

Background

Thermodynamic evaluation of Quercetin distribution in water and organic solvent system is important for the design of Quercetin separation process. Additionally, kinetic analysis of Quercetin distribution has an effect on its separation efficiency. These are useful in designing process for green separation of Quercetin involving aqueous extracts.

Methods

The liquid-liquid extraction process has been demonstrated with equilibrium data for water-organic solvent-Quercetin system. This is studied at three different temperatures i.e. 293, 303, and 313 K. The organic solvent mixture used was ethyl acetate-hexane (1:1 v/v). Kinetic studies of the purification process along with its optimisation was done using a stirred tank.

Significant Findings

The distribution coefficient of Quercetin was in the range of 9.5–0.78 and the separation factor was in the range of 281.7–22.7. The distribution coefficient and extraction efficiency was not affected with change in temperature. The degree of consistency of the equilibrium was evaluated using Othmer-Tobias equation. Additionally, the kinetic study showed that the mass transfer coefficient was a function of stirrer speed and volumetric ratio of aqueous to organic phase. The maximum mass transfer coefficient of 9.41 min-1 was obtained for a stirrer speed of 600 rpm and ratio of Vaq/Vorg of 2.
水-有机溶剂-槲皮素体系液-液萃取过程热力学分析及分离动力学
槲皮素在水和有机溶剂体系中的分布热力学评价对槲皮素分离工艺的设计具有重要意义。此外,槲皮素分布的动力学分析对其分离效率也有影响。这对槲皮素水提物绿色分离工艺设计具有一定的指导意义。方法用平衡数据验证了水-有机溶剂-槲皮素体系的液-液萃取工艺。这在三种不同的温度下进行了研究,即293、303和313 K。使用的有机溶剂混合物为乙酸乙酯-己烷(1:1 v/v)。利用搅拌槽对纯化过程进行了动力学研究,并对其进行了优化。显著性发现槲皮素的分布系数在9.5 ~ 0.78之间,分离系数在281.7 ~ 22.7之间。分布系数和萃取效率不受温度变化的影响。利用Othmer-Tobias方程对平衡的一致性进行了评价。此外,动力学研究表明,传质系数是搅拌速度和水相与有机相体积比的函数。当搅拌转速为600 rpm, Vaq/Vorg为2时,传质系数最大,为9.41 min-1。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
CiteScore
9.10
自引率
14.00%
发文量
362
审稿时长
35 days
期刊介绍: Journal of the Taiwan Institute of Chemical Engineers (formerly known as Journal of the Chinese Institute of Chemical Engineers) publishes original works, from fundamental principles to practical applications, in the broad field of chemical engineering with special focus on three aspects: Chemical and Biomolecular Science and Technology, Energy and Environmental Science and Technology, and Materials Science and Technology. Authors should choose for their manuscript an appropriate aspect section and a few related classifications when submitting to the journal online.
×
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:604180095
Book学术官方微信