An equilibrium phase study is very important for the design, optimization, and control of transformation and separation operations. The investigation of liquid-liquid or liquid-vapor equilibrium has been the subject of much interest in the chemical and petrochemical industry in recent years. Optimizing separation processes is one of the most important areas of process design and numerous types of research both practical and theoretical. The objective of the present work is twofold. First, it involves relying on experimental work to determine data of the liquid-liquid equilibrium (conodals) of ternary systems: {Bisphenol A (1) + Water (2) + Butan-1-ol (3)}, {Bisphenol A (1) + Water (2) + Cyclohexanol (3)} and {Bisphenol A (1) + Water (2) + Cyclohexane (3)}. In the second objective, the experimental results described in the first part were used to calculate interaction parameters of thermodynamic models such as NRTL and UNIQUAC in each phase base on a genetic algorithm technique programmed on MATLAB software. The results of correlations obtained from the experimental equilibrium data for the ternary systems were compared with those obtained from experimental data. The analysis of the results shows a very good agreement between the experimental data and the results obtained after optimization that demonstrates the reliability of the estimated interaction parameters as well as the capacity of NRTL and UNIQUAC models. Therefore, one can retain that the optimization method by genetic algorithms is a reliable method for the design and the simulation of processes.
| Published in | American Journal of Applied Chemistry (Volume 10, Issue 5) |
| DOI | 10.11648/j.ajac.20221005.13 |
| Page(s) | 129-140 |
| Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
| Copyright |
Copyright © The Author(s), 2024. Published by Science Publishing Group |
Liquid-Liquid Equilibrium, Genetic Algorithms (GA), Interaction Parameters
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APA Style
Adama Ouattara, Bamba Lamine, Yao Kouassi Benjamin, Assidjo Nogbou Emmanuel. (2022). Determination of Ternary Systems Bisphenol A-Water-Organic Solvent Interaction Parameters by Genetic Algorithm Approach. American Journal of Applied Chemistry, 10(5), 129-140. https://doi.org/10.11648/j.ajac.20221005.13
ACS Style
Adama Ouattara; Bamba Lamine; Yao Kouassi Benjamin; Assidjo Nogbou Emmanuel. Determination of Ternary Systems Bisphenol A-Water-Organic Solvent Interaction Parameters by Genetic Algorithm Approach. Am. J. Appl. Chem. 2022, 10(5), 129-140. doi: 10.11648/j.ajac.20221005.13
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Download@article{10.11648/j.ajac.20221005.13,
author = {Adama Ouattara and Bamba Lamine and Yao Kouassi Benjamin and Assidjo Nogbou Emmanuel},
title = {Determination of Ternary Systems Bisphenol A-Water-Organic Solvent Interaction Parameters by Genetic Algorithm Approach},
journal = {American Journal of Applied Chemistry},
volume = {10},
number = {5},
pages = {129-140},
doi = {10.11648/j.ajac.20221005.13},
url = {https://doi.org/10.11648/j.ajac.20221005.13},
eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajac.20221005.13},
abstract = {An equilibrium phase study is very important for the design, optimization, and control of transformation and separation operations. The investigation of liquid-liquid or liquid-vapor equilibrium has been the subject of much interest in the chemical and petrochemical industry in recent years. Optimizing separation processes is one of the most important areas of process design and numerous types of research both practical and theoretical. The objective of the present work is twofold. First, it involves relying on experimental work to determine data of the liquid-liquid equilibrium (conodals) of ternary systems: {Bisphenol A (1) + Water (2) + Butan-1-ol (3)}, {Bisphenol A (1) + Water (2) + Cyclohexanol (3)} and {Bisphenol A (1) + Water (2) + Cyclohexane (3)}. In the second objective, the experimental results described in the first part were used to calculate interaction parameters of thermodynamic models such as NRTL and UNIQUAC in each phase base on a genetic algorithm technique programmed on MATLAB software. The results of correlations obtained from the experimental equilibrium data for the ternary systems were compared with those obtained from experimental data. The analysis of the results shows a very good agreement between the experimental data and the results obtained after optimization that demonstrates the reliability of the estimated interaction parameters as well as the capacity of NRTL and UNIQUAC models. Therefore, one can retain that the optimization method by genetic algorithms is a reliable method for the design and the simulation of processes.},
year = {2022}
}
TY - JOUR
T1 - Determination of Ternary Systems Bisphenol A-Water-Organic Solvent Interaction Parameters by Genetic Algorithm Approach
AU - Adama Ouattara
AU - Bamba Lamine
AU - Yao Kouassi Benjamin
AU - Assidjo Nogbou Emmanuel
Y1 - 2022/09/26
PY - 2022
N1 - https://doi.org/10.11648/j.ajac.20221005.13
DO - 10.11648/j.ajac.20221005.13
T2 - American Journal of Applied Chemistry
JF - American Journal of Applied Chemistry
JO - American Journal of Applied Chemistry
SP - 129
EP - 140
PB - Science Publishing Group
SN - 2330-8745
UR - https://doi.org/10.11648/j.ajac.20221005.13
AB - An equilibrium phase study is very important for the design, optimization, and control of transformation and separation operations. The investigation of liquid-liquid or liquid-vapor equilibrium has been the subject of much interest in the chemical and petrochemical industry in recent years. Optimizing separation processes is one of the most important areas of process design and numerous types of research both practical and theoretical. The objective of the present work is twofold. First, it involves relying on experimental work to determine data of the liquid-liquid equilibrium (conodals) of ternary systems: {Bisphenol A (1) + Water (2) + Butan-1-ol (3)}, {Bisphenol A (1) + Water (2) + Cyclohexanol (3)} and {Bisphenol A (1) + Water (2) + Cyclohexane (3)}. In the second objective, the experimental results described in the first part were used to calculate interaction parameters of thermodynamic models such as NRTL and UNIQUAC in each phase base on a genetic algorithm technique programmed on MATLAB software. The results of correlations obtained from the experimental equilibrium data for the ternary systems were compared with those obtained from experimental data. The analysis of the results shows a very good agreement between the experimental data and the results obtained after optimization that demonstrates the reliability of the estimated interaction parameters as well as the capacity of NRTL and UNIQUAC models. Therefore, one can retain that the optimization method by genetic algorithms is a reliable method for the design and the simulation of processes.
VL - 10
IS - 5
ER -
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