Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents
Metallic antimony production from antimony-bearing materials is a research hotspot. The conventional electrowinning technology of antimony is a challenging problem due to the sulfur compounds that come from both the ore itself and the leaching solution in the electrolysis system. The electro-product...
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University of Belgrade, Technical Faculty, Bor
2022-01-01
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Series: | Journal of Mining and Metallurgy. Section B: Metallurgy |
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Online Access: | http://www.doiserbia.nb.rs/img/doi/1450-5339/2022/1450-53392200027M.pdf |
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author | Morcali M.H. Küçükoğlu Ö. Çetiner B.N. Aktaş S. |
author_facet | Morcali M.H. Küçükoğlu Ö. Çetiner B.N. Aktaş S. |
author_sort | Morcali M.H. |
collection | DOAJ |
description | Metallic antimony production from antimony-bearing materials is a research hotspot. The conventional electrowinning technology of antimony is a challenging problem due to the sulfur compounds that come from both the ore itself and the leaching solution in the electrolysis system. The electro-production of antimony in modified non-diaphragm cells is of interest because of the high price and maintenance issues associated with diaphragm cells. A sulfur-based problem in non-diaphragm cells was the focus of this study, which investigated the effects of various salts on this problem and also optimized antimony production conditions. Various salts (i.e., BaCl2, CaCl2, Ba(OH)2, Ca(OH)2) were used as a precipitating agent for the formation of insoluble salts (BaSO4/CaSO4 and BaSO3/CaSO3). Sb concentration, amount of NaOH and Na2S in the bath, electrowinning time, and temperature were investigated to optimize reaction parameters. The Taguchi experimental design was used to determine the effect of each factor on the Sb deposition. The phases and structures formed during electroproduction were identified with the help of various measurement techniques. This study found that in the presence of 96 mM BaCl2, 45 g/L of Sb concentration, 100 g/L of NaOH, and 60 g/L of Na2S were the most suitable factors. It was found that 40 oC was the optimal electrowinning temperature. This result also demonstrated that increasing concentrations of BaCl2 reduced specific energy consumption. |
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issn | 1450-5339 2217-7175 |
language | English |
last_indexed | 2025-02-16T05:58:30Z |
publishDate | 2022-01-01 |
publisher | University of Belgrade, Technical Faculty, Bor |
record_format | Article |
series | Journal of Mining and Metallurgy. Section B: Metallurgy |
spelling | doaj.art-3c871ae39f17410882f40e746677bb192025-02-03T07:49:32ZengUniversity of Belgrade, Technical Faculty, BorJournal of Mining and Metallurgy. Section B: Metallurgy1450-53392217-71752022-01-0158346147310.2298/JMMB220129027M1450-53392200027MNon-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agentsMorcali M.H.0Küçükoğlu Ö.1Çetiner B.N.2Aktaş S.3Naci Topcuoglu Vocational High School, Gaziantep University, Gaziantep, TurkeyDepartment of Metallurgy and Materials Engineering, Marmara University, Istanbul, Turkey + Beykent University, Vocational School, Mechanics Department, Esenyurt/İstanbul, TurkeyDepartment of Metallurgy and Materials Engineering, Marmara University, Istanbul, TurkeyDepartment of Metallurgy and Materials Engineering, Marmara University, Istanbul, TurkeyMetallic antimony production from antimony-bearing materials is a research hotspot. The conventional electrowinning technology of antimony is a challenging problem due to the sulfur compounds that come from both the ore itself and the leaching solution in the electrolysis system. The electro-production of antimony in modified non-diaphragm cells is of interest because of the high price and maintenance issues associated with diaphragm cells. A sulfur-based problem in non-diaphragm cells was the focus of this study, which investigated the effects of various salts on this problem and also optimized antimony production conditions. Various salts (i.e., BaCl2, CaCl2, Ba(OH)2, Ca(OH)2) were used as a precipitating agent for the formation of insoluble salts (BaSO4/CaSO4 and BaSO3/CaSO3). Sb concentration, amount of NaOH and Na2S in the bath, electrowinning time, and temperature were investigated to optimize reaction parameters. The Taguchi experimental design was used to determine the effect of each factor on the Sb deposition. The phases and structures formed during electroproduction were identified with the help of various measurement techniques. This study found that in the presence of 96 mM BaCl2, 45 g/L of Sb concentration, 100 g/L of NaOH, and 60 g/L of Na2S were the most suitable factors. It was found that 40 oC was the optimal electrowinning temperature. This result also demonstrated that increasing concentrations of BaCl2 reduced specific energy consumption.http://www.doiserbia.nb.rs/img/doi/1450-5339/2022/1450-53392200027M.pdfantimonyelectrochemical processmetallic saltsprecipitation |
spellingShingle | Morcali M.H. Küçükoğlu Ö. Çetiner B.N. Aktaş S. Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents Journal of Mining and Metallurgy. Section B: Metallurgy antimony electrochemical process metallic salts precipitation |
title | Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents |
title_full | Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents |
title_fullStr | Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents |
title_full_unstemmed | Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents |
title_short | Non-diaphragm electrodeposition of antimony: Effect of process parameters and precipitating agents |
title_sort | non diaphragm electrodeposition of antimony effect of process parameters and precipitating agents |
topic | antimony electrochemical process metallic salts precipitation |
url | http://www.doiserbia.nb.rs/img/doi/1450-5339/2022/1450-53392200027M.pdf |
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