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Isobaric Vapor−Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane

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Department of Material Science, Tallinn University of Technology, Ehitajate tee 5, 19086 Tallinn, Estonia
Cite this: J. Chem. Eng. Data 2011, 56, 3, 601–605
Publication Date (Web):February 22, 2011
https://doi.org/10.1021/je101301s
Copyright © 2011 American Chemical Society

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    Abstract

    Isobaric vapor−liquid equilibria (VLE) were measured for the ternary system pentan-1-ol + pentyl acetate + nonane and for one constituent binary system, pentan-1-ol + pentyl acetate, at the pressures (26.66, 53.33, 79.99, and 101.32) kPa. Boiling temperature (T)−liquid composition (x) relations were obtained by using a semimicroebulliometer. The Wilson equation was used to correlate the binary Tx data and to predict VLE in the ternary system.

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    Cited By

    This article is cited by 2 publications.

    1. A. Ghanadzadeh Gilani, E. Nasiri-Touli, H. Ghanadzadeh Gilani, S. Shekarsaraee. Comparative Study of Liquid–Liquid Phase Equilibria of the Type II Systems Water + Carboxylic Acids (C5 and C6) + Acetate Esters: Measurement and Correlation. Industrial & Engineering Chemistry Research 2020, 59 (7) , 3129-3140. https://doi.org/10.1021/acs.iecr.9b05389
    2. A. Ghanadzadeh Gilani, M. Nasouri Gazani, B. Mohammadi Khanghah, A. Najafgholizadeh. Experimental and correlated liquid-liquid equilibrium data for water-phosphoric acid-ester. The Journal of Chemical Thermodynamics 2018, 123 , 51-61. https://doi.org/10.1016/j.jct.2018.03.025

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