Abstract
This study reports the process scale-up and long-term performance of an energy-efficient and cost-effective membrane solvent extraction (MSX) process for separation and recovery of high purity rare earth oxides (REOs) from scrap permanent magnets (SPMs). The rare earth elements (REEs), including dysprosium, neodymium, and praseodymium, are recovered from SPMs using a neutral extractant, tetraoctyl diglycolamide (TODGA) embedded in a microporous polypropylene hollow fiber membrane module. The MSX process performance is demonstrated with bench scale module with membrane surface area of 1.4 m2 to industrial scale modules with membrane surface area of up to 20 m2 to enable the processing of up to 1 ton month−1 of SPMs. The purity and the yield of the recovered REOs are >99.5 wt% and >95%, respectively. The average extraction rate of REOs is >10 g m−2 hr−1. A skid of MSX system is assembled with a membrane area of 40 m2. The MSX skid successfully recovers REOs with a capacity of 300 kg REOs/month. Finally, it is determined that the organic phase containing the extractant maintains its performance up to 250 h. The results suggest that the MSX process is an economically viable and environmentally friendly process for separation and recovery of REOs from electronic wastes.
Original language | English |
---|---|
Article number | 2200390 |
Journal | Advanced Engineering Materials |
Volume | 24 |
Issue number | 12 |
DOIs | |
State | Published - Dec 2022 |
Funding
S.Z.I. and P.W. contributed equally to this work. This research/work was supported by the cooperative research and development agreement (CRADA) between the Momentum Technologies Inc., and U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, Advanced Manufacturing Office, Office of Technology Commercialization. The authors thank Preston Bryant and Rob Miles of Momentum Technologies for supporting the project and providing the scrap permanent magnet samples. The authors acknowledge the extensive support in experimental activities provided by Lawrence E. Powell and Dale Adcock. This article has been authored by UT Battelle LLC under Contract No. DE-AC05-00OR22725 with the U.S. Department of Energy. The Department of Energy will provide public access to these results of federally sponsored research in accordance with the DOE Public Access Plan (http://energy.gov/downloads/doe-public-access-plan). S.Z.I. and P.W. contributed equally to this work. This research/work was supported by the cooperative research and development agreement (CRADA) between the Momentum Technologies Inc., and U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, Advanced Manufacturing Office, Office of Technology Commercialization. The authors thank Preston Bryant and Rob Miles of Momentum Technologies for supporting the project and providing the scrap permanent magnet samples. The authors acknowledge the extensive support in experimental activities provided by Lawrence E. Powell and Dale Adcock. This article has been authored by UT Battelle LLC under Contract No. DE‐AC05‐00OR22725 with the U.S. Department of Energy. The Department of Energy will provide public access to these results of federally sponsored research in accordance with the DOE Public Access Plan (http://energy.gov/downloads/doe‐public‐access‐plan).
Funders | Funder number |
---|---|
CRADA | |
DOE Public Access Plan | |
Momentum Technologies Inc. | |
Office of Technology Commercialization | |
Rob Miles of Momentum Technologies | |
U.S. Department of Energy | |
Advanced Manufacturing Office | |
Office of Energy Efficiency and Renewable Energy | |
UT-Battelle | DE-AC05-00OR22725 |
Keywords
- circular economy
- membrane solvent extraction
- process scale-up
- rare earth separations