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Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore
An integrated hydrometallurgical process was used for the zinc leaching and purification from a zinc ore containing 9.75 wt% zinc. The zinc minerals in the ore were hemimorphite, willemite, and calcophanite. Main gangue minerals were quartz, goethite, hematite, and calcite. Central composite design...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Nature Publishing Group UK
2021
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7810752/ https://www.ncbi.nlm.nih.gov/pubmed/33452391 http://dx.doi.org/10.1038/s41598-021-81141-7 |
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author | Soltani, Faraz Darabi, Hossna Aram, Reza Ghadiri, Mahdi |
author_facet | Soltani, Faraz Darabi, Hossna Aram, Reza Ghadiri, Mahdi |
author_sort | Soltani, Faraz |
collection | PubMed |
description | An integrated hydrometallurgical process was used for the zinc leaching and purification from a zinc ore containing 9.75 wt% zinc. The zinc minerals in the ore were hemimorphite, willemite, and calcophanite. Main gangue minerals were quartz, goethite, hematite, and calcite. Central composite design (CCD) method was used to design leaching experiments and the optimum conditions were found as follows: 30% of solid fraction, 22.05% sulphuric acid concentration, and the leaching temperature of 45 °C. The PLS containing 35.07 g/L zinc, 3.16 g/L iron, and 4.58 g/L manganese impurities was produced. A special purification process including Fe precipitation and Zn solvent extraction was implemented. The results showed that after precipitation of iron, Zn extraction of 88.5% was obtained with the 2 stages extraction system composed of 30 vol% D2EHPA as extractant. The overall Zn recovery from the ore was 71.44%. Therefore, an appropriate solution containing 16.6 g/L Zn, 0.05 g/L Fe, and 0.11 g/L Mn was prepared for the electro-winning unit without using the roasting and calcination steps (conventional method), which result in environmental pollution. |
format | Online Article Text |
id | pubmed-7810752 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | Nature Publishing Group UK |
record_format | MEDLINE/PubMed |
spelling | pubmed-78107522021-01-21 Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore Soltani, Faraz Darabi, Hossna Aram, Reza Ghadiri, Mahdi Sci Rep Article An integrated hydrometallurgical process was used for the zinc leaching and purification from a zinc ore containing 9.75 wt% zinc. The zinc minerals in the ore were hemimorphite, willemite, and calcophanite. Main gangue minerals were quartz, goethite, hematite, and calcite. Central composite design (CCD) method was used to design leaching experiments and the optimum conditions were found as follows: 30% of solid fraction, 22.05% sulphuric acid concentration, and the leaching temperature of 45 °C. The PLS containing 35.07 g/L zinc, 3.16 g/L iron, and 4.58 g/L manganese impurities was produced. A special purification process including Fe precipitation and Zn solvent extraction was implemented. The results showed that after precipitation of iron, Zn extraction of 88.5% was obtained with the 2 stages extraction system composed of 30 vol% D2EHPA as extractant. The overall Zn recovery from the ore was 71.44%. Therefore, an appropriate solution containing 16.6 g/L Zn, 0.05 g/L Fe, and 0.11 g/L Mn was prepared for the electro-winning unit without using the roasting and calcination steps (conventional method), which result in environmental pollution. Nature Publishing Group UK 2021-01-15 /pmc/articles/PMC7810752/ /pubmed/33452391 http://dx.doi.org/10.1038/s41598-021-81141-7 Text en © The Author(s) 2021 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/. |
spellingShingle | Article Soltani, Faraz Darabi, Hossna Aram, Reza Ghadiri, Mahdi Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title | Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title_full | Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title_fullStr | Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title_full_unstemmed | Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title_short | Leaching and solvent extraction purification of zinc from Mehdiabad complex oxide ore |
title_sort | leaching and solvent extraction purification of zinc from mehdiabad complex oxide ore |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7810752/ https://www.ncbi.nlm.nih.gov/pubmed/33452391 http://dx.doi.org/10.1038/s41598-021-81141-7 |
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