Local models for representing phase equilibria in multicomponent, non-ideal vapor-liquid and liquid-liquid systems. 2. Application to process design

1984 ◽  
Vol 23 (3) ◽  
pp. 609-618 ◽  
Author(s):  
Eldred H. Chimowitz ◽  
Sandro Macchietto ◽  
Thomas F. Anderson ◽  
Leroy F. Stutzman
Keyword(s):  
Phase Equilibria ◽  
Process Design ◽  
Local Models ◽  
Liquid Systems ◽  
Vapor Liquid

Local models for representing phase equilibriums in multicomponent, nonideal vapor-liquid and liquid-liquid systems. 1. Thermodynamic approximation functions

1983 ◽  
Vol 22 (2) ◽  
pp. 217-225 ◽  
Author(s):  
Eldred H. Chimowitz ◽  
Thomas F. Anderson ◽  
Sandro M. Macchietto ◽  
Leroy F. Stutzman
Keyword(s):  
Local Models ◽  
Liquid Systems ◽  
Vapor Liquid

Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor–Liquid–Liquid Equilibria

2016 ◽  
Vol 61 (8) ◽  
pp. 2700-2711 ◽  
Author(s):  
Petri Uusi-Kyyny ◽  
Simona Ionita ◽  
Muhammad Saad Qureshi ◽  
Ville Alopaeus ◽  
Dominique Richon
Keyword(s):  
Phase Equilibria ◽  
Pvt Measurements ◽  
Vapor Liquid

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.

Determination of methanol/CO2 and acetonitrile/CO2 vapor-liquid phase equilibria using a variable-volume view cell

1996 ◽  
Vol 123 (1-2) ◽  
pp. 215-230 ◽  
Author(s):  
Tricia S. Reighard ◽  
Stephen T. Lee ◽  
Susan V. Olesik
Keyword(s):  
Liquid Phase ◽  
Phase Equilibria ◽  
Variable Volume ◽  
Vapor Liquid

Isobaric vapor-liquid equilibria and distillation process design for separating ketones in biomass pyrolysis oil

2021 ◽  
pp. 106622
Author(s):  
Qiaoyan Shang ◽  
Jifa Xiao ◽  
Xiaojuan Liu ◽  
Yujie Ling ◽  
Wenge Liu ◽  
...  
Keyword(s):  
Process Design ◽  
Pyrolysis Oil ◽  
Distillation Process ◽  
Biomass Pyrolysis ◽  
Vapor Liquid Equilibria ◽  
Vapor Liquid
Sign in / Sign up

Export Citation Format

Share Document