Excess thermodynamic functions for ternary systems. 5. Total-pressure data and GE for 1,4-dioxane-ethanol-water at 50.degree.C-Reference-Cited by-同舟云学术

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Excess thermodynamic functions for ternary systems. 5. Total-pressure data and GE for 1,4-dioxane-ethanol-water at 50.degree.C

Published:1979-04 Issue:2 Volume:24 Page:133-136
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Balcazar-Ortiz A. Mario,Patel Rohit B.,Abbott Michael M.,Van Ness Hendrick C.

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je60081a022

Cited by 29 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Effect of Variation between Different Experimental VLE Data Sets on Thermodynamic Model and Separation Predictions: NRTL Correlation of the Ethanol + Water System;Industrial & Engineering Chemistry Research;2024-06-05

2. Water–ethanol–sodium chloride system: The main sources of uncertainties in thermodynamic properties determined by potentiometry;Fluid Phase Equilibria;2016-03

3. Using the NRTL model with the Vidal equation of state EOS-qE formulation for vapor/liquid equilibrium calculations;Fluid Phase Equilibria;2014-03

4. Supramolecular structure and physicochemical properties of the dioxane–ethanol mixtures;Journal of Molecular Liquids;2010-08

5. Reappraisal of the Vidal equation-of-state formulation for vapor/liquid equilibrium;Fluid Phase Equilibria;2008-03

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