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Isobaric Vapor–Liquid Equilibria of the Ternary System 1-Pentanol + Nonane + Anisole

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Department of Material Science, Tallinn University of Technology, Ehitajate tee 5, 19086 Tallinn, Estonia
* Corresponding author. E-mail: [email protected]
Cite this: J. Chem. Eng. Data 2008, 53, 1, 310–314
Publication Date (Web):December 19, 2007
https://doi.org/10.1021/je700594n
Copyright © 2008 American Chemical Society

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    Abstract

    Isobaric vapor–liquid equilibria (VLE) were measured for the ternary system 1-pentanol + nonane + anisole and for two constituent binaries, nonane + anisole and 1-pentanol + anisole, 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. A minimum boiling azeotrope was observed in nonane + anisole and in 1-pentanol + anisole. The azeotrope in the ternary system was observed only at the pressure 26.66 kPa. 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 10 publications.

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    4. Helle Kirss, Mati Kuus, and Enn Siimer . Isobaric Vapor−Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane. Journal of Chemical & Engineering Data 2011, 56 (3) , 601-605. https://doi.org/10.1021/je101301s
    5. Helle Kirss, Mati Kuus and Enn Siimer. Isobaric Vapor−Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole. Journal of Chemical & Engineering Data 2009, 54 (7) , 2128-2131. https://doi.org/10.1021/je900058p
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