A novel closed-loop biotechnology for recovery of cobalt from a lithium-ion battery active cathode material

Author:

Pakostova Eva1234ORCID,Graves John2,Latvyte Egle2,Maddalena Giovanni56,Horsfall Louise65ORCID

Affiliation:

1. Centre for Health and Life Sciences, Institute of Health and Wellbeing, Coventry University, Coventry, CV1 5FB, UK

2. Centre for Manufacturing and Materials, Institute for Clean Growth and Future Mobility, Coventry University, Coventry, CV1 5FB, UK

3. MIRARCO Mining Innovation, Sudbury, ON P3E 2C6, Canada

4. Goodman School of Mines, Laurentian University, Sudbury, ON P3E 2C6, Canada

5. Faraday Institution (ReLiB project), Quad One, Harwell Science and Innovation Campus, Didcot, UK

6. School of Biological Sciences, University of Edinburgh, Edinburgh, EH9 3FF, UK

Abstract

In recent years, the demand for lithium-ion batteries (LIBs) has been increasing rapidly. Conventional recycling strategies (based on pyro- and hydrometallurgy) are damaging for the environment and more sustainable methods need to be developed. Bioleaching is a promising environmentally friendly approach that uses microorganisms to solubilize metals. However, a bioleaching-based technology has not yet been applied to recover valuable metals from waste LIBs on an industrial scale. A series of experiments was performed to improve metal recovery rates from an active cathode material (LiCoO2; LCO). (i) Direct bioleaching of ≤0.5 % LCO with two prokaryotic acidophilic consortia achieved >80 % Co and 90 % Li extraction. Significantly lower metal recovery rates were obtained at 30 °C than at 45 °C. (ii) In contrast, during direct bioleaching of 3 % LCO with consortia adapted to elevated LCO levels, the 30 °C consortium performed significantly better than the 45 °C consortium, solubilizing 73 and 93 % of the Co and Li, respectively, during one-step bioleaching, and 83 and 99 % of the Co and Li, respectively, during a two-step process. (iii) The adapted 30°C consortium was used for indirect leaching in a low-waste closed-loop system (with 10 % LCO). The process involved generation of sulfuric acid in an acid-generating bioreactor (AGB), 2–3 week leaching of LCO with the biogenic acid (pH 0.9), selective precipitation of Co as hydroxide, and recirculation of the metal-free liquor back into the AGB. In total, 58.2 % Co and 100 % Li were solubilized in seven phases, and >99.9 % of the dissolved Co was recovered after each phase as a high-purity Co hydroxide. Additionally, Co nanoparticles were generated from the obtained Co-rich leachates, using Desulfovibrio alaskensis, and Co electrowinning was optimized as an alternative recovery technique, yielding high recovery rates (91.1 and 73.6% on carbon felt and roughened steel, respectively) from bioleachates that contained significantly lower Co concentrations than industrial hydrometallurgical liquors. The closed-loop system was highly dominated by the mixotrophic archaeon Ferroplasma and sulfur-oxidizing bacteria Acidithiobacillus caldus and Acidithiobacillus thiooxidans. The developed system achieved high metal recovery rates and provided high-purity solid products suitable for a battery supply chain, while minimizing waste production and the inhibitory effects of elevated concentrations of dissolved metals on the leaching prokaryotes. The system is suitable for scale-up applications and has the potential to be adapted to different battery chemistries.

Funder

Faraday Institution

Engineering and Physical Sciences Research Council

Publisher

Microbiology Society

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