Prediction of vapor-liquid equilibria of non-aqueous systems in the subcritical range by using the NRTL equation-Reference-Cited by-同舟云学术

Prediction of vapor-liquid equilibria of non-aqueous systems in the subcritical range by using the NRTL equation

Published:1993-12 Issue:2 Volume:91 Page:265-280
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Vetere Alessandro

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference17 articles.

1. One-parameter equation for excess Gibbs energy of strongly nonideal liquid mixtures;Bruin;Ind. Eng. Chem., Process Des. Dev.,1971

2. Gmehling, J. Onken, U. 1977a. Vapor-liquid Equilibrium Data Collection: Aqueous-organic Systems, DECHEMA Chemistry Data Series, Vol. 1, Part 1, Frankfurt.

3. Gmehling, J. Onken, U. 1977b. Vapor-liquid Equilibrium Data Collection: Organic Hydroxy Compounds; Alcohols. DECHEMA Chemistry Data Series, Vol. 1, Part 2a, Frankfurt.

4. Vapor-Liquid Equilibrium Data Collection: Aqueous Organic Systems (Suppl. 1);Gmehling,1981

Cited by 10 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. Modeling the Total Ternary Phase Diagram of NaNO3–KNO3–NaNO2 Using the Binary Subsystems Data;International Journal of Thermophysics;2019-11-23

2. One-parameter modified nonrandom two-liquid (NRTL) activity coefficient model;Fluid Phase Equilibria;2014-10

3. The NRTL equation as a predictive tool for vapor–liquid equilibria;Fluid Phase Equilibria;2004-04

4. A simple modification of the NRTL equation;Fluid Phase Equilibria;2000-08

5. An empirical method to evaluate the solubility of several gases in polar and non-polar solvents;Fluid Phase Equilibria;1997-05