Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment

The content of zinc in copper smelter slags obtained from pyrometallurgical copper production is comparable to the content of this metal in zinc ores. Therefore, these slags are considered a valuable secondary resource for zinc recovery. At the same time, the features of the mineralogical compositi...

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Autores principales: Mehmet Deniz Turan, Galymzhan A. Karamyrzayev, Rashid K. Nadirov
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Lenguaje:EN
KK
RU
Publicado: al-Farabi Kazakh National University 2021
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Acceso en línea:https://doaj.org/article/5a09d733f26e419f9b44e1d18a2c859f
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spelling oai:doaj.org-article:5a09d733f26e419f9b44e1d18a2c859f2021-11-30T10:30:24ZRecovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment10.15328/cb12441563-03312312-7554https://doaj.org/article/5a09d733f26e419f9b44e1d18a2c859f2021-10-01T00:00:00Zhttps://bulletin.chemistry.kz/index.php/kaznu/article/view/1244https://doaj.org/toc/1563-0331https://doaj.org/toc/2312-7554 The content of zinc in copper smelter slags obtained from pyrometallurgical copper production is comparable to the content of this metal in zinc ores. Therefore, these slags are considered a valuable secondary resource for zinc recovery. At the same time, the features of the mineralogical composition of the slag make the extraction of zinc from it very problematic. Most of the zinc is concentrated in the refractory zinc ferrite (ZnFe2O4). To avoid the formation of a viscous pulp when leaching copper smelter slag with an aqueous solution of sulfuric acid, in this work, the slag was leached with sulfuric acid also in isopropanol and n-pentanol, under the following conditions: 0.5 M H2SO4, pulp density 50 g/L, magnetic stirrer rotation speed 600 rpm. The influence of the duration and temperature of leaching milled (≤100 μm) copper smelter slag of the Balkhash copper smelter on the extraction of zinc into solution was investigated. It was found that the maximum zinc recovery into an aqueous solution was 75 ± 2% at 363 K and 210 min. Replacing water with isopropanol or n-pentanol led to an increase in zinc recovery to 82 ± 2% at 210 min and a lower temperature (353 K) than in an aqueous environment. An increase in temperature to 383 K during leaching in n-pentanol made it possible to extract 92 ± 2% of zinc. A shrinking core model was used to describe the kinetics of the zinc leaching process. It was found that the limiting stage of the process under all investigated conditions is the chemical leaching reaction. Some kinetic characteristics of the leaching process were calculated, in particular, the apparent reaction rate constants, as well as the activation energy. Mehmet Deniz TuranGalymzhan A. KaramyrzayevRashid K. Nadiroval-Farabi Kazakh National Universityarticlecopper smelter slagleachingzinc recoveryisopropanoln-pentanolChemistryQD1-999ENKKRUChemical Bulletin of Kazakh National University, Vol 103, Iss 4 (2021)
institution DOAJ
collection DOAJ
language EN
KK
RU
topic copper smelter slag
leaching
zinc recovery
isopropanol
n-pentanol
Chemistry
QD1-999
spellingShingle copper smelter slag
leaching
zinc recovery
isopropanol
n-pentanol
Chemistry
QD1-999
Mehmet Deniz Turan
Galymzhan A. Karamyrzayev
Rashid K. Nadirov
Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
description The content of zinc in copper smelter slags obtained from pyrometallurgical copper production is comparable to the content of this metal in zinc ores. Therefore, these slags are considered a valuable secondary resource for zinc recovery. At the same time, the features of the mineralogical composition of the slag make the extraction of zinc from it very problematic. Most of the zinc is concentrated in the refractory zinc ferrite (ZnFe2O4). To avoid the formation of a viscous pulp when leaching copper smelter slag with an aqueous solution of sulfuric acid, in this work, the slag was leached with sulfuric acid also in isopropanol and n-pentanol, under the following conditions: 0.5 M H2SO4, pulp density 50 g/L, magnetic stirrer rotation speed 600 rpm. The influence of the duration and temperature of leaching milled (≤100 μm) copper smelter slag of the Balkhash copper smelter on the extraction of zinc into solution was investigated. It was found that the maximum zinc recovery into an aqueous solution was 75 ± 2% at 363 K and 210 min. Replacing water with isopropanol or n-pentanol led to an increase in zinc recovery to 82 ± 2% at 210 min and a lower temperature (353 K) than in an aqueous environment. An increase in temperature to 383 K during leaching in n-pentanol made it possible to extract 92 ± 2% of zinc. A shrinking core model was used to describe the kinetics of the zinc leaching process. It was found that the limiting stage of the process under all investigated conditions is the chemical leaching reaction. Some kinetic characteristics of the leaching process were calculated, in particular, the apparent reaction rate constants, as well as the activation energy.
format article
author Mehmet Deniz Turan
Galymzhan A. Karamyrzayev
Rashid K. Nadirov
author_facet Mehmet Deniz Turan
Galymzhan A. Karamyrzayev
Rashid K. Nadirov
author_sort Mehmet Deniz Turan
title Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
title_short Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
title_full Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
title_fullStr Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
title_full_unstemmed Recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
title_sort recovery of zinc from copper smelter slag by sulfuric acid leaching in an aqueous and alcoholic environment
publisher al-Farabi Kazakh National University
publishDate 2021
url https://doaj.org/article/5a09d733f26e419f9b44e1d18a2c859f
work_keys_str_mv AT mehmetdenizturan recoveryofzincfromcoppersmelterslagbysulfuricacidleachinginanaqueousandalcoholicenvironment
AT galymzhanakaramyrzayev recoveryofzincfromcoppersmelterslagbysulfuricacidleachinginanaqueousandalcoholicenvironment
AT rashidknadirov recoveryofzincfromcoppersmelterslagbysulfuricacidleachinginanaqueousandalcoholicenvironment
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