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Multi-objective Optimization and Control of Self-Heat Recuperative Azeoropic Distillation for Separating an Ethanol/Water Mixture
[Image: see text] Azeotropic distillation is an important method for the separation of an ethanol/water mixture, while the main disadvantage of azeotropic distillation is its high energy consumption. Since the self-heat recuperation technology can effectively recover and utilize the heat of effluent...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical Society
2022
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8992292/ https://www.ncbi.nlm.nih.gov/pubmed/35415331 http://dx.doi.org/10.1021/acsomega.2c00478 |
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author | Li, Lumin Yu, Na Zhu, Yi |
author_facet | Li, Lumin Yu, Na Zhu, Yi |
author_sort | Li, Lumin |
collection | PubMed |
description | [Image: see text] Azeotropic distillation is an important method for the separation of an ethanol/water mixture, while the main disadvantage of azeotropic distillation is its high energy consumption. Since the self-heat recuperation technology can effectively recover and utilize the heat of effluent stream in thermal processes, it is introduced into the ethanol dehydration process. The conventional azeotropic distillation and self-heat recuperative azeotropic distillation (SHRAD) are simulated and optimized with multiple objectives. There exists a design point in the Pareto solution set for which the total annual cost is the lowest, the thermodynamic efficiency is the highest, and the CO(2) emission is the least. Based on the specified design, the dynamic characteristics of the SHRAD configuration are studied, and two control structures are proposed. The improved control structure of the SHRAD process works well under the feed flowrate and composition disturbance, and the SHRAD system can obtain a high-purity ethanol product. The results show that the SHRAD process has significant advantages over conventional azeotropic distillation in terms of economic and environmental benefits. In addition, an effective control structure can ensure the stable operation of the SHRAD process. |
format | Online Article Text |
id | pubmed-8992292 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | American Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-89922922022-04-11 Multi-objective Optimization and Control of Self-Heat Recuperative Azeoropic Distillation for Separating an Ethanol/Water Mixture Li, Lumin Yu, Na Zhu, Yi ACS Omega [Image: see text] Azeotropic distillation is an important method for the separation of an ethanol/water mixture, while the main disadvantage of azeotropic distillation is its high energy consumption. Since the self-heat recuperation technology can effectively recover and utilize the heat of effluent stream in thermal processes, it is introduced into the ethanol dehydration process. The conventional azeotropic distillation and self-heat recuperative azeotropic distillation (SHRAD) are simulated and optimized with multiple objectives. There exists a design point in the Pareto solution set for which the total annual cost is the lowest, the thermodynamic efficiency is the highest, and the CO(2) emission is the least. Based on the specified design, the dynamic characteristics of the SHRAD configuration are studied, and two control structures are proposed. The improved control structure of the SHRAD process works well under the feed flowrate and composition disturbance, and the SHRAD system can obtain a high-purity ethanol product. The results show that the SHRAD process has significant advantages over conventional azeotropic distillation in terms of economic and environmental benefits. In addition, an effective control structure can ensure the stable operation of the SHRAD process. American Chemical Society 2022-03-22 /pmc/articles/PMC8992292/ /pubmed/35415331 http://dx.doi.org/10.1021/acsomega.2c00478 Text en © 2022 The Authors. Published by American Chemical Society https://creativecommons.org/licenses/by-nc-nd/4.0/Permits non-commercial access and re-use, provided that author attribution and integrity are maintained; but does not permit creation of adaptations or other derivative works (https://creativecommons.org/licenses/by-nc-nd/4.0/). |
spellingShingle | Li, Lumin Yu, Na Zhu, Yi Multi-objective Optimization and Control of Self-Heat Recuperative Azeoropic Distillation for Separating an Ethanol/Water Mixture |
title | Multi-objective Optimization and Control of Self-Heat
Recuperative Azeoropic Distillation for Separating an Ethanol/Water
Mixture |
title_full | Multi-objective Optimization and Control of Self-Heat
Recuperative Azeoropic Distillation for Separating an Ethanol/Water
Mixture |
title_fullStr | Multi-objective Optimization and Control of Self-Heat
Recuperative Azeoropic Distillation for Separating an Ethanol/Water
Mixture |
title_full_unstemmed | Multi-objective Optimization and Control of Self-Heat
Recuperative Azeoropic Distillation for Separating an Ethanol/Water
Mixture |
title_short | Multi-objective Optimization and Control of Self-Heat
Recuperative Azeoropic Distillation for Separating an Ethanol/Water
Mixture |
title_sort | multi-objective optimization and control of self-heat
recuperative azeoropic distillation for separating an ethanol/water
mixture |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8992292/ https://www.ncbi.nlm.nih.gov/pubmed/35415331 http://dx.doi.org/10.1021/acsomega.2c00478 |
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