Effect of three-body interactions on the vapor-liquid phase equilibria of binary fluid mixtures

2006 ◽  
Vol 125 (7) ◽  
pp. 074503 ◽  
Author(s):  
Liping Wang ◽  
Richard J. Sadus
Keyword(s):  
Liquid Phase ◽  
Phase Equilibria ◽  
Binary Fluid ◽  
Fluid Mixtures ◽  
Three Body ◽  
Binary Fluid Mixtures ◽  
Vapor Liquid

Fully developed traveling-wave convection in binary fluid mixtures

1989 ◽  
Vol 63 (4) ◽  
pp. 376-379 ◽  
Author(s):  
W. Barten ◽  
M. Lücke ◽  
W. Hort ◽  
M. Kamps
Keyword(s):  
Traveling Wave ◽  
Binary Fluid ◽  
Fluid Mixtures ◽  
Binary Fluid Mixtures

Pattern study of thermal phase separation for binary fluid mixtures

2011 ◽  
Vol 21 (5) ◽  
pp. 572-583 ◽  
Author(s):  
Adriano Tiribocchi ◽  
Antonio Piscitelli ◽  
Giuseppe Gonnella ◽  
Antonio Lamura
Keyword(s):  
Phase Separation ◽  
Binary Fluid ◽  
Fluid Mixtures ◽  
Thermal Phase ◽  
Binary Fluid Mixtures

scholarly journals Thermodynamics and Machine Learning Based Approaches for Vapor–Liquid–Liquid Phase Equilibria in n-Octane/Water, as a Naphtha–Water Surrogate in Water Blends

Processes ◽  
2021 ◽  
Vol 9 (3) ◽  
pp. 413
Author(s):  
Sandra Lopez-Zamora ◽  
Jeonghoon Kong ◽  
Salvador Escobedo ◽  
Hugo de Lasa
Keyword(s):  
Machine Learning ◽  
Liquid Phase ◽  
Phase Equilibria ◽  
Aspen Plus ◽  
Phase Region ◽  
Two Phase ◽  
Technical Literature ◽  
Phase Liquid ◽  
Liquid Vapor ◽  
Vapor Liquid

The prediction of phase equilibria for hydrocarbon/water blends in separators, is a subject of considerable importance for chemical processes. Despite its relevance, there are still pending questions. Among them, is the prediction of the correct number of phases. While a stability analysis using the Gibbs Free Energy of mixing and the NRTL model, provide a good understanding with calculation issues, when using HYSYS V9 and Aspen Plus V9 software, this shows that significant phase equilibrium uncertainties still exist. To clarify these matters, n-octane and water blends, are good surrogates of naphtha/water mixtures. Runs were developed in a CREC vapor–liquid (VL_ Cell operated with octane–water mixtures under dynamic conditions and used to establish the two-phase (liquid–vapor) and three phase (liquid–liquid–vapor) domains. Results obtained demonstrate that the two phase region (full solubility in the liquid phase) of n-octane in water at 100 °C is in the 10-4 mol fraction range, and it is larger than the 10-5 mol fraction predicted by Aspen Plus and the 10-7 mol fraction reported in the technical literature. Furthermore, and to provide an effective and accurate method for predicting the number of phases, a machine learning (ML) technique was implemented and successfully demonstrated, in the present study.

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