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Processing of a Zinc Leach Residue by a Non-Fossil Reductant

[Image: see text] The suitability of a non-fossil reductant in high-temperature treatment of a zinc leach residue was studied in laboratory-scale experiments. The pyrometallurgical experiments carried out at temperatures of 1200–1350 °C consisted of melting the residue under an oxidizing atmosphere...

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Autores principales: Rämä, Minna, Klemettinen, Lassi, Rinne, Marja, Taskinen, Pekka, Michallik, Radosław Markus, Salminen, Justin, Jokilaakso, Ari
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2023
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10286245/
https://www.ncbi.nlm.nih.gov/pubmed/37360496
http://dx.doi.org/10.1021/acsomega.3c00250
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author Rämä, Minna
Klemettinen, Lassi
Rinne, Marja
Taskinen, Pekka
Michallik, Radosław Markus
Salminen, Justin
Jokilaakso, Ari
author_facet Rämä, Minna
Klemettinen, Lassi
Rinne, Marja
Taskinen, Pekka
Michallik, Radosław Markus
Salminen, Justin
Jokilaakso, Ari
author_sort Rämä, Minna
collection PubMed
description [Image: see text] The suitability of a non-fossil reductant in high-temperature treatment of a zinc leach residue was studied in laboratory-scale experiments. The pyrometallurgical experiments carried out at temperatures of 1200–1350 °C consisted of melting the residue under an oxidizing atmosphere to produce an intermediate, desulfurized slag, which was further cleaned of metals such as Zn, Pb, Cu, and Ag, using renewable biochar as a reductant. The aim was to recover valuable metals and produce a clean, stable slag for use as construction material, for example. The first experiments indicated that biochar is a viable alternative to fossil-based metallurgical coke. The capabilities of biochar as a reductant were studied in more detail after optimizing the processing temperature at 1300 °C and modifying the experimental arrangement by adding rapid quenching of the sample (to a solid state in less than 5 s) to the procedure. Modifying the slag viscosity by adding 5–10 wt % MgO was found to enhance the slag cleaning significantly. With an addition of 10 wt % MgO, the target Zn concentration in slag (Zn < 1 wt %) was reached after as little as 10 min of reduction, and the Pb concentration was also decreased relatively close to the target value (Pb < 0.03 wt %). With an addition of 0–5 wt % MgO, the target Zn and Pb levels were not reached within 10 min, but with longer treatment times of 30–60 min, 5 wt % of MgO was enough to decrease the Zn content in slag sufficiently. The lowest Pb concentration achieved with an addition of 5 wt % MgO was 0.09 wt % after a 60 min reduction time.
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spelling pubmed-102862452023-06-23 Processing of a Zinc Leach Residue by a Non-Fossil Reductant Rämä, Minna Klemettinen, Lassi Rinne, Marja Taskinen, Pekka Michallik, Radosław Markus Salminen, Justin Jokilaakso, Ari ACS Omega [Image: see text] The suitability of a non-fossil reductant in high-temperature treatment of a zinc leach residue was studied in laboratory-scale experiments. The pyrometallurgical experiments carried out at temperatures of 1200–1350 °C consisted of melting the residue under an oxidizing atmosphere to produce an intermediate, desulfurized slag, which was further cleaned of metals such as Zn, Pb, Cu, and Ag, using renewable biochar as a reductant. The aim was to recover valuable metals and produce a clean, stable slag for use as construction material, for example. The first experiments indicated that biochar is a viable alternative to fossil-based metallurgical coke. The capabilities of biochar as a reductant were studied in more detail after optimizing the processing temperature at 1300 °C and modifying the experimental arrangement by adding rapid quenching of the sample (to a solid state in less than 5 s) to the procedure. Modifying the slag viscosity by adding 5–10 wt % MgO was found to enhance the slag cleaning significantly. With an addition of 10 wt % MgO, the target Zn concentration in slag (Zn < 1 wt %) was reached after as little as 10 min of reduction, and the Pb concentration was also decreased relatively close to the target value (Pb < 0.03 wt %). With an addition of 0–5 wt % MgO, the target Zn and Pb levels were not reached within 10 min, but with longer treatment times of 30–60 min, 5 wt % of MgO was enough to decrease the Zn content in slag sufficiently. The lowest Pb concentration achieved with an addition of 5 wt % MgO was 0.09 wt % after a 60 min reduction time. American Chemical Society 2023-06-05 /pmc/articles/PMC10286245/ /pubmed/37360496 http://dx.doi.org/10.1021/acsomega.3c00250 Text en © 2023 The Authors. Published by American Chemical Society https://creativecommons.org/licenses/by/4.0/Permits the broadest form of re-use including for commercial purposes, provided that author attribution and integrity are maintained (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Rämä, Minna
Klemettinen, Lassi
Rinne, Marja
Taskinen, Pekka
Michallik, Radosław Markus
Salminen, Justin
Jokilaakso, Ari
Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title_full Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title_fullStr Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title_full_unstemmed Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title_short Processing of a Zinc Leach Residue by a Non-Fossil Reductant
title_sort processing of a zinc leach residue by a non-fossil reductant
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10286245/
https://www.ncbi.nlm.nih.gov/pubmed/37360496
http://dx.doi.org/10.1021/acsomega.3c00250
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