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Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate
After the atmospheric hydrochloric acid leaching method is used to treat laterite ore and initially purify it, the extract that results often contains a significant amount of Fe(2+) impurities. A novel metallurgical process has been proposed that utilizes microbubble aeration to oxidize Fe(2+) ions...
Autores principales: | , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2023
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10650111/ https://www.ncbi.nlm.nih.gov/pubmed/37959548 http://dx.doi.org/10.3390/ma16216951 |
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author | Xu, Ziyang Wang, Yu Zhu, Boyuan Wei, Guangye Ma, Fei Yu, Zhihui Qu, Jingkui |
author_facet | Xu, Ziyang Wang, Yu Zhu, Boyuan Wei, Guangye Ma, Fei Yu, Zhihui Qu, Jingkui |
author_sort | Xu, Ziyang |
collection | PubMed |
description | After the atmospheric hydrochloric acid leaching method is used to treat laterite ore and initially purify it, the extract that results often contains a significant amount of Fe(2+) impurities. A novel metallurgical process has been proposed that utilizes microbubble aeration to oxidize Fe(2+) ions in laterite hydrochloric acid lixivium, facilitating subsequent separation and capitalizing on the benefits of microbubble technology, including its expansive specific surface area, negatively charged surface attributes, prolonged stagnation duration, and its capacity to produce active oxygen. The study examined the impacts of aeration aperture, stirring speed, oxygen flow rate, pH value, and reaction temperature. Under optimized experimental conditions, which included an aeration aperture of 0.45 µm, stirring at 500 rpm, a bubbling flow rate of 0.4 L/min, pH level maintained at 3.5, and a temperature range of 75–85 °C, the oxidation efficiency of Fe(2+) surpassed 99%. An analysis of the mass transfer process revealed that microbubble aeration markedly enhances the oxygen mass transfer coefficient, measured at 0.051 s(−1). The study also confirmed the self-catalytic properties of Fe(2+) oxidation and conducted kinetic studies to determine an apparent activation energy of 399 kJ/mol. At pH values below 3.5, the reaction is solely governed by chemical reactions; however, at higher pH values (>3.5), both chemical reactions and oxygen dissolution jointly control the reaction. |
format | Online Article Text |
id | pubmed-10650111 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2023 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-106501112023-10-30 Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate Xu, Ziyang Wang, Yu Zhu, Boyuan Wei, Guangye Ma, Fei Yu, Zhihui Qu, Jingkui Materials (Basel) Article After the atmospheric hydrochloric acid leaching method is used to treat laterite ore and initially purify it, the extract that results often contains a significant amount of Fe(2+) impurities. A novel metallurgical process has been proposed that utilizes microbubble aeration to oxidize Fe(2+) ions in laterite hydrochloric acid lixivium, facilitating subsequent separation and capitalizing on the benefits of microbubble technology, including its expansive specific surface area, negatively charged surface attributes, prolonged stagnation duration, and its capacity to produce active oxygen. The study examined the impacts of aeration aperture, stirring speed, oxygen flow rate, pH value, and reaction temperature. Under optimized experimental conditions, which included an aeration aperture of 0.45 µm, stirring at 500 rpm, a bubbling flow rate of 0.4 L/min, pH level maintained at 3.5, and a temperature range of 75–85 °C, the oxidation efficiency of Fe(2+) surpassed 99%. An analysis of the mass transfer process revealed that microbubble aeration markedly enhances the oxygen mass transfer coefficient, measured at 0.051 s(−1). The study also confirmed the self-catalytic properties of Fe(2+) oxidation and conducted kinetic studies to determine an apparent activation energy of 399 kJ/mol. At pH values below 3.5, the reaction is solely governed by chemical reactions; however, at higher pH values (>3.5), both chemical reactions and oxygen dissolution jointly control the reaction. MDPI 2023-10-30 /pmc/articles/PMC10650111/ /pubmed/37959548 http://dx.doi.org/10.3390/ma16216951 Text en © 2023 by the authors. https://creativecommons.org/licenses/by/4.0/Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Article Xu, Ziyang Wang, Yu Zhu, Boyuan Wei, Guangye Ma, Fei Yu, Zhihui Qu, Jingkui Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title | Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title_full | Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title_fullStr | Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title_full_unstemmed | Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title_short | Microbubble Oxidation for Fe(2+) Removal from Hydrochloric Acid Laterite Ore Leachate |
title_sort | microbubble oxidation for fe(2+) removal from hydrochloric acid laterite ore leachate |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10650111/ https://www.ncbi.nlm.nih.gov/pubmed/37959548 http://dx.doi.org/10.3390/ma16216951 |
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