Recovery of aluminum oxide and iron oxide from aluminum electrolysis iron-rich cover material and preparation of aluminum fluoride

In aluminum electrolysis, the iron-rich cover material is formed on the cover material and the steel rod connecting the carbon anode. Due to the high iron content in the iron-rich cover material, it differs from traditional cover material and thus requires harmless recycling and treatment. A process...

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Veröffentlicht in:Environmental science and pollution research international 2024-04, Vol.31 (18), p.27388-27402
Hauptverfasser: Lan, Jinghao, Yan, Hengwei, Liu, Zhanwei, Ma, Wenhui
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Yan, Hengwei
Liu, Zhanwei
Ma, Wenhui
description In aluminum electrolysis, the iron-rich cover material is formed on the cover material and the steel rod connecting the carbon anode. Due to the high iron content in the iron-rich cover material, it differs from traditional cover material and thus requires harmless recycling and treatment. A process was proposed and used in this study to recovery F, Al, and Fe elements from the iron-rich cover material. This process involved aluminum sulfate solution leaching for fluorine recovery and alkali-acid synergistic leaching for α-Al 2 O 3 and Fe 2 O 3 recovery were obtained. The optimal leaching rates for F, Na, Ca, Fe, and Si were 93.92, 96.25, 94.53, 4.48, and 28.87%, respectively. The leaching solution and leaching residue were obtained. The leaching solution was neutralized to obtain the aluminum hydroxide fluoride hydrate (AHFH, AlF 1.5 (OH) 1.5 ·(H 2 O) 0.375 ). AHFH was calcined to form a mixture of AlF 3 and Al 2 O 3 with a purity of 96.14%. The overall recovery rate of F in the entire process was 92.36%. Additionally, the leaching residue was sequentially leached with alkali and acid to obtain the acid leach residue α-Al 2 O 3 . The pH of the acid-leached solution was adjusted to produce a black-brown precipitate, which was converted to Fe 2 O 3 under a high-temperature calcination, and the recovery rate of Fe in the whole process was 94.54%. Therefore, this study provides a new method for recovering F, Al, and Fe in iron-rich cover material, enabling the utilization of aluminum hazardous waste sources.
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Due to the high iron content in the iron-rich cover material, it differs from traditional cover material and thus requires harmless recycling and treatment. A process was proposed and used in this study to recovery F, Al, and Fe elements from the iron-rich cover material. This process involved aluminum sulfate solution leaching for fluorine recovery and alkali-acid synergistic leaching for α-Al 2 O 3 and Fe 2 O 3 recovery were obtained. The optimal leaching rates for F, Na, Ca, Fe, and Si were 93.92, 96.25, 94.53, 4.48, and 28.87%, respectively. The leaching solution and leaching residue were obtained. The leaching solution was neutralized to obtain the aluminum hydroxide fluoride hydrate (AHFH, AlF 1.5 (OH) 1.5 ·(H 2 O) 0.375 ). AHFH was calcined to form a mixture of AlF 3 and Al 2 O 3 with a purity of 96.14%. The overall recovery rate of F in the entire process was 92.36%. Additionally, the leaching residue was sequentially leached with alkali and acid to obtain the acid leach residue α-Al 2 O 3 . The pH of the acid-leached solution was adjusted to produce a black-brown precipitate, which was converted to Fe 2 O 3 under a high-temperature calcination, and the recovery rate of Fe in the whole process was 94.54%. 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Due to the high iron content in the iron-rich cover material, it differs from traditional cover material and thus requires harmless recycling and treatment. A process was proposed and used in this study to recovery F, Al, and Fe elements from the iron-rich cover material. This process involved aluminum sulfate solution leaching for fluorine recovery and alkali-acid synergistic leaching for α-Al 2 O 3 and Fe 2 O 3 recovery were obtained. The optimal leaching rates for F, Na, Ca, Fe, and Si were 93.92, 96.25, 94.53, 4.48, and 28.87%, respectively. The leaching solution and leaching residue were obtained. The leaching solution was neutralized to obtain the aluminum hydroxide fluoride hydrate (AHFH, AlF 1.5 (OH) 1.5 ·(H 2 O) 0.375 ). AHFH was calcined to form a mixture of AlF 3 and Al 2 O 3 with a purity of 96.14%. The overall recovery rate of F in the entire process was 92.36%. Additionally, the leaching residue was sequentially leached with alkali and acid to obtain the acid leach residue α-Al 2 O 3 . The pH of the acid-leached solution was adjusted to produce a black-brown precipitate, which was converted to Fe 2 O 3 under a high-temperature calcination, and the recovery rate of Fe in the whole process was 94.54%. Therefore, this study provides a new method for recovering F, Al, and Fe in iron-rich cover material, enabling the utilization of aluminum hazardous waste sources.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><pmid>38512573</pmid><doi>10.1007/s11356-024-32877-y</doi><tpages>15</tpages></addata></record>
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identifier ISSN: 1614-7499
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source MEDLINE; SpringerLink Journals
subjects Acids
Aluminum
Aluminum - chemistry
Aluminum Compounds - chemistry
aluminum fluoride
Aluminum fluorides
Aluminum hydroxide
Aluminum oxide
Aluminum Oxide - chemistry
Aluminum sulfate
anodes
Aquatic Pollution
Atmospheric Protection/Air Quality Control/Air Pollution
carbon
Connecting rods
Earth and Environmental Science
Ecotoxicology
Electrolysis
Environment
Environmental Chemistry
Environmental Health
Ferric Compounds - chemistry
Ferric oxide
Fluorides
Fluorides - chemistry
Fluorine
hazardous waste
Hazardous wastes
High temperature
Iron
Iron - chemistry
Iron oxides
Leaching
Recycling
Research Article
Residues
Roasting
steel
Waste Water Technology
Water Management
Water Pollution Control
title Recovery of aluminum oxide and iron oxide from aluminum electrolysis iron-rich cover material and preparation of aluminum fluoride
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