Affiliation:
1. Institute of Environmental Engineering and Management, College of Engineering, National Taipei University of Technology, Taipei 10608, Taiwan
2. School of Metallurgical and Ecological Engineering, University of Science and Technology Beijing, Beijing 100083, China
3. Functional Advanced Materials Engineering Research Center, School of Integrated Science and Innovation, Sirindhorn International Institute of Technology, Thammasat University, Klong Luang 12121, Thailand
Abstract
In this paper, a novel procedure is proposed for comprehensively recovering zinc fluoride (ZnF2), manganese fluorides [MnFx(x = 2, 3)], manganese dioxide (MnO2), and carbon powder from the electrode powder of spent alkaline batteries. Firstly, hydrofluoric acid (HF) leaching is conducted on the electrode powder of spent alkaline batteries. Secondly, potassium permanganate (KMnO4) is introduced into the leachate to selectively precipitate manganese (Mn) ions to recover MnO2. Subsequently, the water content in the leachate is evaporated to recover ZnF2. Finally, the leaching residue is leached again by using HF, after which the water content in the leachate is evaporated to recover MnFx. The results indicated that under optimal conditions of a HF concentration of 4 M, a leaching time of 15 min, and a liquid–solid ratio of 5 mL/g, the optimal leaching selectivity for Zn and Mn was achieved and the leaching efficiencies of Zn and Mn were 97.83% and 39.94%, respectively. When KMnO4 with a dosage (KMnO4/Mn ion molar ratio) of 0.5:1 was added to the leachate, MnO2 with a grade of 91.68% and a Mn recovery of 39.07% was obtained. In addition, ZnF2 with a grade of 97.98% and a Zn recovery of 96.15% was also obtained after removing the water content from the leachate via evaporation. Under the optimal conditions of a HF concentration of 2 M, a leaching time of 15 min, and a liquid–solid ratio of 10 mL/g for the leaching residue, followed by removing the water content in the leachate via evaporation, MnFx with a grade of 94.20% and a Mn recovery of 59.46%, was obtained. The residue of the releaching process was carbon powder. The effectiveness of the proposed recovery procedure was confirmed.
Funder
NTUT-TU Joint Research Program
Thammasat University and the National Taipei University of Technology
USTB-NTUT Joint Research Program
Ministry of Science and Technology
Subject
Management, Monitoring, Policy and Law,Renewable Energy, Sustainability and the Environment,Geography, Planning and Development,Building and Construction