气液平衡的量子化学分子动力学模拟和径向分布函数分析

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Byoung Chul Kim, Su Yeong Jeong, Cho Won Jin, Jeom-Soo Kim, Young Han Kim
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引用次数: 0

摘要

本文采用量子化学(QC)分子动力学模拟方法对深共晶溶剂(DES)和离子液体(IL)三种典型体系的气液平衡(VLE)进行了估计,而不是传统的分子模拟方法。此外,从QC模拟中导出了径向分布函数(RDF)来考察液相中的分子行为。与实验数据相比,QC模拟的平均绝对误差为2.72%。RDF分析解释了醋酸丙酯溶剂对醋酸水二元体系相对挥发性的增加。分析表明,由甘油和氯化胆碱组成的DES混合物有利于水和i-丙醇的分离。在1-乙基-3-甲基咪唑的帮助下,水和硫酸乙酯之间的相互作用比乙醇和水之间的相互作用更强,这解释了IL如何改善乙醇和水在气相中的分离。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Vapour–liquid equilibrium using quantum chemical molecular dynamics simulation and radial distribution function analysis

Instead of the classical molecular simulation widely implemented for estimating the vapour–liquid equilibrium (VLE), a quantum chemical (QC) molecular dynamics simulation was applied to the VLE estimation in three typical systems that include a deep eutectic solvent (DES) and an ionic liquid (IL). In addition, a radial distribution function (RDF) was derived from the QC simulation to examine the molecular behaviour in the liquid phase. A mean absolute error of 2.72% was obtained from the QC simulation compared to the experimental data. The RDF analysis explains the relative volatility increase of the acetic acid and water binary system with the propyl acetate solvent. This analysis indicated that the DES mixture comprising glycerol and choline chloride facilitated the separation of water and i-propanol. The interaction between water and ethyl sulphate pair with the help of 1-ethyl-3-methylimidazolium as an IL is stronger than that between ethanol and water, which explains how the IL improves ethanol and water separation in the vapour phase.

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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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