Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching

A research using ferronickel slag, the by-product of ferronickel production, as raw material for magnesium extraction was carried out. It is essential to upgrade the value of ferronickel slag instead of used directly for reclamation materials. Moreover, the accumulation due to increasing ferronickel...

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Main Authors: Prasetyo A.B., Khaerul A., Mayangsari W., Febriana E., Maksum A., Andinie J., Firdiyono F., Soedarsono J.W.
Format: Article
Language:English
Published: University of Belgrade, Technical Faculty, Bor 2021-01-01
Series:Journal of Mining and Metallurgy. Section B: Metallurgy
Subjects:
Online Access:http://www.doiserbia.nb.rs/img/doi/1450-5339/2021/1450-53392100018P.pdf
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author Prasetyo A.B.
Khaerul A.
Mayangsari W.
Febriana E.
Maksum A.
Andinie J.
Firdiyono F.
Soedarsono J.W.
author_facet Prasetyo A.B.
Khaerul A.
Mayangsari W.
Febriana E.
Maksum A.
Andinie J.
Firdiyono F.
Soedarsono J.W.
author_sort Prasetyo A.B.
collection DOAJ
description A research using ferronickel slag, the by-product of ferronickel production, as raw material for magnesium extraction was carried out. It is essential to upgrade the value of ferronickel slag instead of used directly for reclamation materials. Moreover, the accumulation due to increasing ferronickel demand as well as the environmental contamination due to various potentially toxic elements contained in the ferronickel slag could be prevented. The general objective of this study is to utilize the ferronickel slag for magnesium materials. The specific objective is to determine the optimum conditions of magnesium extraction in the process of alkali fusion followed by hydrochloric acid leaching. A novel method for magnesium extraction from ferronickel slag was carried out through reducing silica content followed by acid leaching method. Alkali fusion of the mixture of ferronickel slag and Na2CO3 at 1000°C for 60 minutes, followed by water leaching at 100°C for 60 minutes with solid to liquid percentage of 20 % was carried out to separate the silica. The leaching residue resulted from water leaching was then leached using hydrochloric acid solution to extract magnesium. The leaching temperature and time as well as the hycrochloric acid concentration were varied in the acid leaching process. Alkali fusion process proved the sodium silicate can be generated and that it can be separated in the water leaching to the leached solution. Meanwhile, the leaching residue was leached using hydrochloric acid to extract the magnesium. The highest magnesium extraction percentage is 82.67% that resulted from an optimum acid leaching condition with temperature of 80°C for 30 minutes using 2M HCl solution. Based on the kinetics study, the activation energy (Ea) for the leaching reaction of magnesium at atmospheric pressure between 32°C to 80°C is 9.44 kJ/mol and affected by diffusion and chemical reactions.
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issn 1450-5339
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publishDate 2021-01-01
publisher University of Belgrade, Technical Faculty, Bor
record_format Article
series Journal of Mining and Metallurgy. Section B: Metallurgy
spelling doaj-art-97a184c718fd4f13ae1f3fa27ad4b0332025-02-02T19:57:03ZengUniversity of Belgrade, Technical Faculty, BorJournal of Mining and Metallurgy. Section B: Metallurgy1450-53392217-71752021-01-0157222523310.2298/JMMB200224018P1450-53392100018PMagnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leachingPrasetyo A.B.0Khaerul A.1Mayangsari W.2Febriana E.3Maksum A.4Andinie J.5Firdiyono F.6Soedarsono J.W.7Center of Minerals Processing and Corrosion Research, Department of Metallurgical and Materials Engineering, Universitas Indonesia, Depok, Indonesia + Research Center for Metallurgy and Materials, Indonesian Institute of Sciences, Serpong, Tangsel, IndonesiaDepartment of Metallurgy Engineering, Universitas Sultan Ageng Tirtayasa, Cilegon Banten, IndonesiaCenter of Minerals Processing and Corrosion Research, Department of Metallurgical and Materials Engineering, Universitas Indonesia, Depok, Indonesia + Research Center for Metallurgy and Materials, Indonesian Institute of Sciences, Serpong, Tangsel, IndonesiaResearch Center for Metallurgy and Materials, Indonesian Institute of Sciences, Serpong, Tangsel, IndonesiaDepartment of Mechanical Engineering, Politeknik Negeri Jakarta, Depok, IndonesiaDepartment of Metallurgy Engineering, Universitas Sultan Ageng Tirtayasa, Cilegon Banten, IndonesiaResearch Center for Metallurgy and Materials, Indonesian Institute of Sciences, Serpong, Tangsel, IndonesiaCenter of Minerals Processing and Corrosion Research, Department of Metallurgical and Materials Engineering, Universitas Indonesia, Depok, IndonesiaA research using ferronickel slag, the by-product of ferronickel production, as raw material for magnesium extraction was carried out. It is essential to upgrade the value of ferronickel slag instead of used directly for reclamation materials. Moreover, the accumulation due to increasing ferronickel demand as well as the environmental contamination due to various potentially toxic elements contained in the ferronickel slag could be prevented. The general objective of this study is to utilize the ferronickel slag for magnesium materials. The specific objective is to determine the optimum conditions of magnesium extraction in the process of alkali fusion followed by hydrochloric acid leaching. A novel method for magnesium extraction from ferronickel slag was carried out through reducing silica content followed by acid leaching method. Alkali fusion of the mixture of ferronickel slag and Na2CO3 at 1000°C for 60 minutes, followed by water leaching at 100°C for 60 minutes with solid to liquid percentage of 20 % was carried out to separate the silica. The leaching residue resulted from water leaching was then leached using hydrochloric acid solution to extract magnesium. The leaching temperature and time as well as the hycrochloric acid concentration were varied in the acid leaching process. Alkali fusion process proved the sodium silicate can be generated and that it can be separated in the water leaching to the leached solution. Meanwhile, the leaching residue was leached using hydrochloric acid to extract the magnesium. The highest magnesium extraction percentage is 82.67% that resulted from an optimum acid leaching condition with temperature of 80°C for 30 minutes using 2M HCl solution. Based on the kinetics study, the activation energy (Ea) for the leaching reaction of magnesium at atmospheric pressure between 32°C to 80°C is 9.44 kJ/mol and affected by diffusion and chemical reactions.http://www.doiserbia.nb.rs/img/doi/1450-5339/2021/1450-53392100018P.pdfferronickelslagalkali-fusionleachingmagnesiumsilicaextraction
spellingShingle Prasetyo A.B.
Khaerul A.
Mayangsari W.
Febriana E.
Maksum A.
Andinie J.
Firdiyono F.
Soedarsono J.W.
Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
Journal of Mining and Metallurgy. Section B: Metallurgy
ferronickel
slag
alkali-fusion
leaching
magnesium
silica
extraction
title Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
title_full Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
title_fullStr Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
title_full_unstemmed Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
title_short Magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
title_sort magnesium extraction of ferronickel slag processed by alkali fusion and hydrochloric acid leaching
topic ferronickel
slag
alkali-fusion
leaching
magnesium
silica
extraction
url http://www.doiserbia.nb.rs/img/doi/1450-5339/2021/1450-53392100018P.pdf
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AT khaerula magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT mayangsariw magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT febrianae magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT maksuma magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT andiniej magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT firdiyonof magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching
AT soedarsonojw magnesiumextractionofferronickelslagprocessedbyalkalifusionandhydrochloricacidleaching