首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Measurements and Correlation of Isobaric Vapor-Liquid Equilibria for the Binary Systems of Cyclohexanol plus Cyclohexyl Formate and Cyclopentanol plus Cyclopentyl Formate under Various Pressures
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Measurements and Correlation of Isobaric Vapor-Liquid Equilibria for the Binary Systems of Cyclohexanol plus Cyclohexyl Formate and Cyclopentanol plus Cyclopentyl Formate under Various Pressures

机译:环己醇加环己基甲酸环己基甲酸甲酸二甲酸甲酸二甲酸甲酸二甲酸甲酸酯和环戊醇加环戊基甲酸甲酯在各种压力下的测量和相关性

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摘要

Data of vapor-liquid equilibria are essential in the design of a separation unit in the technology of cyclic alkene indirect hydration in the presence of formic acid. This work aims at measuring the vapor-liquid equilibria (VLE) data of the binary systems cyclohexanol + cyclohexyl formate and cyclopentanol + cyclopentyl formate under various pressures and to correlate these data by nonrandom-two liquid and universal quasichemical models to obtain binary interaction parameters that will be used for the design of a distillation unit. According to the best of our knowledge, the VLE of cyclopentanol + cyclopentyl formate binary system has not been published in the literature. Furthermore, the accuracy of the experimental data fitting for the system of cyclohexanol + cyclohexyl formate was compared to a previously published model. Moreover, the model obtained in this work was tested for data prediction under higher pressures, and good accuracy was achieved. Also, the thermodynamic consistency of the experimental data was evaluated by Fredenslund test, and the data fitting accuracy was calculated based on average absolute deviation and root-mean-square-error values.
机译:蒸汽液体平衡数据在甲酸存在下的环状烯烃间接水合技术中的分离单元的设计中是必不可少的。这项工作旨在测量二元系统的蒸汽均衡(VLE)甲己醇+环己基甲酸酯和环戊醇+环戊基在各种压力下甲酸酯,并通过非正常 - 两个液体和通用的新型模型与这些数据相关,以获得二元相互作用参数将用于设计蒸馏装置。根据我们所知,环戊烷醇+环戊基甲酸酯二元系统的VLE尚未公布在文献中。此外,将环己醇+环己基甲酸酯系统的实验数据配合的准确性与先前公布的模型进行了比较。此外,在该工作中获得的模型在更高的压力下进行数据预测,实现了良好的精度。此外,通过Fredenslund测试评估了实验数据的热力学稠度,并且基于平均绝对偏差和根均方误差值计算数据拟合精度。

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