Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values

Copper anode furnace dust is waste by-product of secondary copper production containing zinc, lead, copper, tin, iron and many other elements. Hydrometallurgical Copper Anode Furnace dust recycling method was studied theoretically by thermodynamic calculations and the proposed method was verified ex...

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Main Authors: Dušan Oráč, Jakub Klimko, Dušan Klein, Jana Pirošková, Pavol Liptai, Tomáš Vindt, Andrea Miškufová
Format: Article
Language:English
Published: MDPI AG 2021-12-01
Series:Metals
Subjects:
Online Access:https://www.mdpi.com/2075-4701/12/1/36
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author Dušan Oráč
Jakub Klimko
Dušan Klein
Jana Pirošková
Pavol Liptai
Tomáš Vindt
Andrea Miškufová
author_facet Dušan Oráč
Jakub Klimko
Dušan Klein
Jana Pirošková
Pavol Liptai
Tomáš Vindt
Andrea Miškufová
author_sort Dušan Oráč
collection DOAJ
description Copper anode furnace dust is waste by-product of secondary copper production containing zinc, lead, copper, tin, iron and many other elements. Hydrometallurgical Copper Anode Furnace dust recycling method was studied theoretically by thermodynamic calculations and the proposed method was verified experimentally on a laboratory scale. The optimum condition for leaching of zinc from dust was identified to be an ambient leaching temperature, a liquid/solid ratio of 10 and H<sub>2</sub>SO<sub>4</sub> concentration of 1 mol/L. A maximum of 98.85% of zinc was leached under the optimum experimental conditions. In the leaching step, 99.7% of lead in the form of insoluble PbSO<sub>4</sub> was separated from the other leached metals. Solution refining was done by combination of pH adjustment and zinc powder cementation. Tin was precipitated from solution by pH adjustment to 3. Iron was precipitated out of solution after pH adjustment to 4 with efficiency 98.54%. Copper was selectively cemented out of solution (99.96%) by zinc powder. Zinc was precipitated out of solution by addition of Na<sub>2</sub>CO<sub>3</sub> with efficiency of 97.31%. ZnO as final product was obtained by calcination of zinc carbonates.
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spelling doaj.art-50b60f34f4f04242af83d47bff3d79232023-11-23T14:41:24ZengMDPI AGMetals2075-47012021-12-011213610.3390/met12010036Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal ValuesDušan Oráč0Jakub Klimko1Dušan Klein2Jana Pirošková3Pavol Liptai4Tomáš Vindt5Andrea Miškufová6Faculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaFaculty of Materials, Institute of Recycling Technologies, Metallurgy and Recycling, Technical University of Košice, Letná 9, 042 00 Kosice, SlovakiaCopper anode furnace dust is waste by-product of secondary copper production containing zinc, lead, copper, tin, iron and many other elements. Hydrometallurgical Copper Anode Furnace dust recycling method was studied theoretically by thermodynamic calculations and the proposed method was verified experimentally on a laboratory scale. The optimum condition for leaching of zinc from dust was identified to be an ambient leaching temperature, a liquid/solid ratio of 10 and H<sub>2</sub>SO<sub>4</sub> concentration of 1 mol/L. A maximum of 98.85% of zinc was leached under the optimum experimental conditions. In the leaching step, 99.7% of lead in the form of insoluble PbSO<sub>4</sub> was separated from the other leached metals. Solution refining was done by combination of pH adjustment and zinc powder cementation. Tin was precipitated from solution by pH adjustment to 3. Iron was precipitated out of solution after pH adjustment to 4 with efficiency 98.54%. Copper was selectively cemented out of solution (99.96%) by zinc powder. Zinc was precipitated out of solution by addition of Na<sub>2</sub>CO<sub>3</sub> with efficiency of 97.31%. ZnO as final product was obtained by calcination of zinc carbonates.https://www.mdpi.com/2075-4701/12/1/36zinc recyclingcopper anode furnace dustrecyclingindustrial wastecircular economyleaching
spellingShingle Dušan Oráč
Jakub Klimko
Dušan Klein
Jana Pirošková
Pavol Liptai
Tomáš Vindt
Andrea Miškufová
Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
Metals
zinc recycling
copper anode furnace dust
recycling
industrial waste
circular economy
leaching
title Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
title_full Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
title_fullStr Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
title_full_unstemmed Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
title_short Hydrometallurgical Recycling of Copper Anode Furnace Dust for a Complete Recovery of Metal Values
title_sort hydrometallurgical recycling of copper anode furnace dust for a complete recovery of metal values
topic zinc recycling
copper anode furnace dust
recycling
industrial waste
circular economy
leaching
url https://www.mdpi.com/2075-4701/12/1/36
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