Isobaric Vapor–Liquid Equilibrium of Binary Mixtures of Acetophenone and 1-Phenylethanol at 3.00, 5.00, 10.00, and 15.00 kPa

IF 2 3区工程技术 Q3 CHEMISTRY, MULTIDISCIPLINARY

Journal of Chemical & Engineering Data Pub Date : 2025-01-24 DOI:10.1021/acs.jced.4c0062810.1021/acs.jced.4c00628

Fengzhi Li, Wangfeng Cai, Yang Xiao, Yujie Yao and Yan Wang*,

引用次数: 0

Abstract

Vapor–liquid equilibrium (VLE) data for the acetophenone (AP) and 1-phenylethanol (1-PE) binary system were measured at 3.00, 5.00, 10.00, and 15.00 kPa by using a modified Rose–Williams distiller. The thermodynamic consistency of the experimental data was verified through the Fredenslund test and Van Ness test. The data were correlated using the NRTL, UNIQUAC, and Wilson models, with root-mean-square deviations (RMSDs) for vapor composition (y₁) and equilibrium temperature (T) calculated. The findings suggest that the NRTL, Wilson, and UNIQUAC models are appropriate for use in this system.

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来源期刊

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.