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利用 Kirkwood-Buff 理论对正己烷-乙醇二元混合物进行热力学分析。

Thermodynamic Analysis of n-Hexane-Ethanol Binary Mixtures Using the Kirkwood-Buff Theory.

机构信息

School of Chemical Engineering , National Technical University of Athens , GR 15780 Athens , Greece.

出版信息

J Phys Chem B. 2019 Jan 10;123(1):247-257. doi: 10.1021/acs.jpcb.8b10425. Epub 2018 Dec 19.

DOI:10.1021/acs.jpcb.8b10425
PMID:30516991
Abstract

A complete thermodynamic analysis of mixtures consisting of molecules with complex chemical constitution can be rather demanding. The Kirkwood-Buff theory of solutions allows the estimation of thermodynamic properties, which cannot be directly extracted from atomistic simulations, such as the Gibbs energy of mixing (Δ G). In this work, we perform molecular dynamics simulations of n-hexane-ethanol binary mixtures in the liquid state under two temperature-pressure conditions and at various mole fractions. On the basis of the recently published methodology of Galata [ Fluid Phase Equilib. 2018 , 470 , 25 - 37 ] , we first calculate the Kirkwood-Buff integrals in the isothermal-isobaric ( NpT) ensemble, identifying how system size affects their estimation. We then extract the activity coefficients, excess Gibbs energy, excess enthalpy, and excess entropy for the n-hexane-ethanol binary mixtures we simulate. We employ two approaches for quantifying composition fluctuations: one based on counting molecular centers of mass and a second one based on counting molecular segments. Results from the two approaches are practically indistinguishable. We compare our results against predictions of vapor-liquid equilibria obtained in a previous simulation work using the same force field, as well as with experimental data, and find very good agreement. In addition, we develop a simple methodology to identify the hydrogen bonds between ethanol molecules and analyze their effects on mixing properties.

摘要

对于由具有复杂化学结构的分子组成的混合物,进行完整的热力学分析可能要求很高。溶液的 Kirkwood-Buff 理论允许估计不能直接从原子模拟中提取的热力学性质,例如混合吉布斯自由能(ΔG)。在这项工作中,我们在两种温度-压力条件下和各种摩尔分数下对正己烷-乙醇二元混合物进行了分子动力学模拟。基于最近发表的 Galata [Fluid Phase Equilib. 2018, 470, 25-37]的方法,我们首先在等温等压(NpT)系综中计算 Kirkwood-Buff 积分,确定系统大小如何影响它们的估计。然后,我们提取我们模拟的正己烷-乙醇二元混合物的活度系数、超额吉布斯自由能、超额焓和超额熵。我们采用两种方法来量化组成波动:一种基于计数分子质心,另一种基于计数分子片段。这两种方法的结果几乎没有区别。我们将我们的结果与使用相同力场的先前模拟工作中获得的汽液平衡预测进行了比较,并与实验数据进行了比较,发现非常吻合。此外,我们开发了一种简单的方法来识别乙醇分子之间的氢键,并分析它们对混合性质的影响。

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