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Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor
In recent years, the emission of detrimental acidic pollutants to the atmosphere has raised the concerns of scientists. Sulphur dioxide (SO(2)) is a harmful greenhouse gas, which its abnormal release to the atmosphere may cause far-ranging environmental and health effects like acid rain and respirat...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Nature Publishing Group UK
2023
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9873644/ https://www.ncbi.nlm.nih.gov/pubmed/36693929 http://dx.doi.org/10.1038/s41598-023-28580-6 |
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author | Cao, Yan Taghvaie Nakhjiri, Ali Ghadiri, Mahdi |
author_facet | Cao, Yan Taghvaie Nakhjiri, Ali Ghadiri, Mahdi |
author_sort | Cao, Yan |
collection | PubMed |
description | In recent years, the emission of detrimental acidic pollutants to the atmosphere has raised the concerns of scientists. Sulphur dioxide (SO(2)) is a harmful greenhouse gas, which its abnormal release to the atmosphere may cause far-ranging environmental and health effects like acid rain and respiratory problems. Therefore, finding promising techniques to alleviate the emission of this greenhouse gas may be of great urgency towards environmental protection. This paper aims to evaluate the potential of three novel absorbents (seawater (H(2)O), dimethyl aniline (DMA) and sodium hydroxide (NaOH) to separate SO(2) acidic pollutant from SO(2)/air gaseous stream inside the hollow fiber membrane contactor (HFMC). To reach this goal, a CFD-based simulation was developed to predict the results. Also, a mathematical model was applied to theoretically evaluate the transport equations in different compartments of contactor. Comparison of the results has implied seawater is the most efficient liquid absorbent for separating SO(2). After seawater, NaOH and DMA are placed at the second and third rank (99.36% separation using seawater > 62% separation using NaOH > 55% separation using DMA). Additionally, the influence of operational parameters (i.e., gas and liquid flow rates) and also membrane/module parameters (i.e., length of membrane module, hollow fibers’ number and porosity) on the SO(2) separation percentage is investigated as another highlight of this paper. |
format | Online Article Text |
id | pubmed-9873644 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2023 |
publisher | Nature Publishing Group UK |
record_format | MEDLINE/PubMed |
spelling | pubmed-98736442023-01-26 Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor Cao, Yan Taghvaie Nakhjiri, Ali Ghadiri, Mahdi Sci Rep Article In recent years, the emission of detrimental acidic pollutants to the atmosphere has raised the concerns of scientists. Sulphur dioxide (SO(2)) is a harmful greenhouse gas, which its abnormal release to the atmosphere may cause far-ranging environmental and health effects like acid rain and respiratory problems. Therefore, finding promising techniques to alleviate the emission of this greenhouse gas may be of great urgency towards environmental protection. This paper aims to evaluate the potential of three novel absorbents (seawater (H(2)O), dimethyl aniline (DMA) and sodium hydroxide (NaOH) to separate SO(2) acidic pollutant from SO(2)/air gaseous stream inside the hollow fiber membrane contactor (HFMC). To reach this goal, a CFD-based simulation was developed to predict the results. Also, a mathematical model was applied to theoretically evaluate the transport equations in different compartments of contactor. Comparison of the results has implied seawater is the most efficient liquid absorbent for separating SO(2). After seawater, NaOH and DMA are placed at the second and third rank (99.36% separation using seawater > 62% separation using NaOH > 55% separation using DMA). Additionally, the influence of operational parameters (i.e., gas and liquid flow rates) and also membrane/module parameters (i.e., length of membrane module, hollow fibers’ number and porosity) on the SO(2) separation percentage is investigated as another highlight of this paper. Nature Publishing Group UK 2023-01-24 /pmc/articles/PMC9873644/ /pubmed/36693929 http://dx.doi.org/10.1038/s41598-023-28580-6 Text en © The Author(s) 2023 https://creativecommons.org/licenses/by/4.0/Open Access This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article's Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article's Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) . |
spellingShingle | Article Cao, Yan Taghvaie Nakhjiri, Ali Ghadiri, Mahdi Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title | Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title_full | Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title_fullStr | Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title_full_unstemmed | Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title_short | Computational fluid dynamics comparison of prevalent liquid absorbents for the separation of SO(2) acidic pollutant inside a membrane contactor |
title_sort | computational fluid dynamics comparison of prevalent liquid absorbents for the separation of so(2) acidic pollutant inside a membrane contactor |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9873644/ https://www.ncbi.nlm.nih.gov/pubmed/36693929 http://dx.doi.org/10.1038/s41598-023-28580-6 |
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