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SO(2) Adsorption and Kinetics Analysis during Supported Triethanolamine Acetate Ionic Liquid Desulfurization
[Image: see text] Ionic liquid desulfurization is an effective method for achieving green and circulating desulfurization. To overcome the negative impact of the high viscosity of ionic liquids on the desulfurization process, an economical and efficient supported ionic liquid—triethanolamine acetate...
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/PMC9670701/ https://www.ncbi.nlm.nih.gov/pubmed/36406586 http://dx.doi.org/10.1021/acsomega.2c04664 |
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author | Wang, Chenglong Tang, Lishu Cui, Lin Chen, Shouyan Liu, Jinglong Dong, Yong |
author_facet | Wang, Chenglong Tang, Lishu Cui, Lin Chen, Shouyan Liu, Jinglong Dong, Yong |
author_sort | Wang, Chenglong |
collection | PubMed |
description | [Image: see text] Ionic liquid desulfurization is an effective method for achieving green and circulating desulfurization. To overcome the negative impact of the high viscosity of ionic liquids on the desulfurization process, an economical and efficient supported ionic liquid—triethanolamine acetate ionic liquid/silica (TAIL/SiO(2)) was prepared in this study. TAIL is synthesized using triethanolamine and acetic acid and subsequently loaded onto silica gel particles. The effects of the reaction temperature, humidity, silica particle size, and loading ratio on SO(2) adsorption are investigated using a fixed-bed reactor. The results indicate that the surface of the silica gel loaded with ionic liquid formed uneven spherical clusters, and the aggregate volume increased with an increase in the loading ratio. The TAIL/SiO(2) sulfur capacity could be effectively increased by increasing the loading ratio (exceeding 0.74 is unfavorable), decreasing the silica particle size, and reducing the reaction temperature and moisture content. The maximum sulfur capacity can reach 124.98 mg SO(2)/(g TAIL/SiO(2)) under experimental conditions, which is higher than that of activated carbon. The Bangham rate model effectively predicts the kinetics of the adsorption process of SO(2). |
format | Online Article Text |
id | pubmed-9670701 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | American Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-96707012022-11-18 SO(2) Adsorption and Kinetics Analysis during Supported Triethanolamine Acetate Ionic Liquid Desulfurization Wang, Chenglong Tang, Lishu Cui, Lin Chen, Shouyan Liu, Jinglong Dong, Yong ACS Omega [Image: see text] Ionic liquid desulfurization is an effective method for achieving green and circulating desulfurization. To overcome the negative impact of the high viscosity of ionic liquids on the desulfurization process, an economical and efficient supported ionic liquid—triethanolamine acetate ionic liquid/silica (TAIL/SiO(2)) was prepared in this study. TAIL is synthesized using triethanolamine and acetic acid and subsequently loaded onto silica gel particles. The effects of the reaction temperature, humidity, silica particle size, and loading ratio on SO(2) adsorption are investigated using a fixed-bed reactor. The results indicate that the surface of the silica gel loaded with ionic liquid formed uneven spherical clusters, and the aggregate volume increased with an increase in the loading ratio. The TAIL/SiO(2) sulfur capacity could be effectively increased by increasing the loading ratio (exceeding 0.74 is unfavorable), decreasing the silica particle size, and reducing the reaction temperature and moisture content. The maximum sulfur capacity can reach 124.98 mg SO(2)/(g TAIL/SiO(2)) under experimental conditions, which is higher than that of activated carbon. The Bangham rate model effectively predicts the kinetics of the adsorption process of SO(2). American Chemical Society 2022-11-04 /pmc/articles/PMC9670701/ /pubmed/36406586 http://dx.doi.org/10.1021/acsomega.2c04664 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 | Wang, Chenglong Tang, Lishu Cui, Lin Chen, Shouyan Liu, Jinglong Dong, Yong SO(2) Adsorption and Kinetics Analysis during Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title | SO(2) Adsorption
and Kinetics Analysis during
Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title_full | SO(2) Adsorption
and Kinetics Analysis during
Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title_fullStr | SO(2) Adsorption
and Kinetics Analysis during
Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title_full_unstemmed | SO(2) Adsorption
and Kinetics Analysis during
Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title_short | SO(2) Adsorption
and Kinetics Analysis during
Supported Triethanolamine Acetate Ionic Liquid Desulfurization |
title_sort | so(2) adsorption
and kinetics analysis during
supported triethanolamine acetate ionic liquid desulfurization |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9670701/ https://www.ncbi.nlm.nih.gov/pubmed/36406586 http://dx.doi.org/10.1021/acsomega.2c04664 |
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