Journal ArticleDOI
(Vapour+liquid) equilibria in the ternary system (acetonitrile+n-propanol+ethylene glycol) and corresponding binary systems at 101.3kPa
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TLDR
Experimental isobaric (Vapour+ liquid) equilibrium (VLE) data at 101.3 kPa were determined for three binary systems, viz. {acetonitrile (1)+n-propanol (2)}, {acetitrile(1)−+ ethylene glycol (3)} and {n-polypanol(2)+ Ã Ã − Ã ¼ Ã À Ã ) for one ternary system as discussed by the authors.About:
This article is published in The Journal of Chemical Thermodynamics.The article was published on 2013-12-01. It has received 8 citations till now. The article focuses on the topics: Non-random two-liquid model & Ternary numeral system.read more
Citations
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Journal ArticleDOI
Approach to the 1-propanol dehydration using an extractive distillation process with ethylene glycol
TL;DR: In this paper, the potential use of ethylene glycol as entrainer in a 1-propanol dehydration process by extractive distillation was discussed, and the experimental data were correlated by the Wilson, NRTL and UNIQUAC local composition models in order to obtain a set of thermodynamic parameters.
Journal ArticleDOI
Experimental Measurement and Modeling of Vapor–Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
TL;DR: In this paper, a reliable activity coefficient model for the ternary systems water + ethanol + ethylene glycol, water + 2-propanol + polypropanol + polyethylene glycol was presented.
Journal ArticleDOI
Effect of thermodynamic parameters on prediction of phase behavior and process design of extractive distillation
TL;DR: In this paper, the authors investigated the effect of thermodynamic parameters on the prediction of phase behavior, and process design of extractive distillation using the Aspen Plus simulation platform.
Journal ArticleDOI
Measurement and correlation of the (p, ρ, T) behaviour of liquid ethylene glycol at temperatures from (283.3 to 393.1) K and pressures up to 100.1 MPa
TL;DR: In this article, the (p, ρ, T) behavior of propylene glycol was investigated in the homogeneous liquid phase over the temperature range from (272.7 to 393.0)
Journal ArticleDOI
Isobaric Vapor–Liquid Equilibrium of the Acetonitrile + 1‑Propanol + Ionic Liquids at an Atmospheric Pressure
TL;DR: The mixture of acetonitrile + n-propanol (2) forms a binary azeotropic mixture at atmospheric pressure, which cannot be separated by common distillation as mentioned in this paper.
References
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Journal ArticleDOI
Local compositions in thermodynamic excess functions for liquid mixtures
Henri Renon,John M. Prausnitz +1 more
TL;DR: In this paper, a new equation based on Scott's two-liquid model and on an assumption of nonrandomness similar to that used by Wilson is derived, which gives an excellent representation of many types of liquid mixtures.
Journal ArticleDOI
Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing
Journal ArticleDOI
Vapor-Liquid equilibrium: Part I. An appraisal of data reduction methods
TL;DR: In this paper, it was shown that use of a full P-x-y data set is for all practical purposes based on just the P-y values, and that effective use of such data set can be made only if redundent experimental values of Px,y or P are compared for consistency with calculated values.
Related Papers (5)
Isothermal vapor-liquid equilibrium of ternary mixtures formed by 1-propanol, acetonitrile and benzene
Isobaric vapor–liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at P = 101.3 kPa: Effect of the 1,3-propanediol addition
Yi-Feng Lin,Chein-Hsiun Tu +1 more