Analysis of Vapor–Liquid Equilibrium in Ternary Systems for an Adequate Planning of Their Experimental Determination and Correlation
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Title: | Analysis of Vapor–Liquid Equilibrium in Ternary Systems for an Adequate Planning of Their Experimental Determination and Correlation |
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Authors: | Marcilla, Antonio | Oliver, Inés | Moncur, Liam | Carbonell Hermida, Paloma | Olaya, Maria del Mar |
Research Group/s: | Procesado y Pirólisis de Polímeros |
Center, Department or Service: | Universidad de Alicante. Departamento de Ingeniería Química | Universidad de Alicante. Instituto Universitario de Ingeniería de los Procesos Químicos |
Keywords: | Vapor–liquid equilibrium | Ternary systems | Experimental data |
Issue Date: | 29-Feb-2024 |
Publisher: | American Chemical Society |
Citation: | Journal of Chemical & Engineering Data. 2024, 69(10): 3462-3471. https://doi.org/10.1021/acs.jced.3c00712 |
Abstract: | Experimental vapor–liquid equilibrium (VLE) data, and the activity coefficient model parameters obtained by their correlation, are frequently used in separation processes design. The inspection of this information for ternary systems has revealed some problems that are not widely known and could lead to serious mistakes. A small sampling of ten ternary systems, with VLE data sets at constant pressure, arbitrarily selected has been considered to illustrate these problems. The experimental VLE data and the NRTL model parameters for these systems have been taken from different sources, one database and two commercial simulation packages. A MATLAB code has been developed to prepare 3D graphs where the T/x and T/y surfaces calculated by the activity coefficient model (NRTL) are represented along with the experimental VLE data. The results of the analysis of this small sample are very worrying. In fact, half of the selected systems present severe inconsistences between the experimental VLE data and the T/x,y surfaces calculated using the correlation results published or implemented in the simulation software. These inconsistences are of different natures, but the most notable is the existence of parameter sets that do not correlate at all the VLE behavior of the system that they supposedly represent. These irregularities may occur only in the ternary region, only in the binary subsystems, or, in some cases, in both. These problems go frequently unnoticed for different reasons. As discussed in this work, the typical 2D graphs and deviations in T or P and vapor composition are not enough in some cases so as to have an adequate idea of both the quality of the data and the suitability of the model to represent them. This is particularly true when considering, as is strongly advisible, the complete set of data, i.e. the ternary and binary VLE data simultaneously. Some recommendations are presented in this work to overcome the problems detected both when planning the experimental design to determine VLE data and to correlate them with a model. |
Sponsor: | The authors would like to thank “Ministerio de Ciencia e Innovación” for financial support through Project PID2020-119320GB-I00. |
URI: | http://hdl.handle.net/10045/141162 |
ISSN: | 0021-9568 (Print) | 1520-5134 (Online) |
DOI: | 10.1021/acs.jced.3c00712 |
Language: | eng |
Type: | info:eu-repo/semantics/article |
Rights: | © 2024 The Authors. Published by American Chemical Society. This publication is licensed under CC-BY 4.0. |
Peer Review: | si |
Publisher version: | https://doi.org/10.1021/acs.jced.3c00712 |
Appears in Collections: | INV - GTP3 - Artículos de Investigación sobre Equilibrio entre Fases |
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