Cobalt Recovery from Li-Ion Battery Recycling: A Critical Review
Abstract
:1. Introduction
1.1. Cobalt: Critical and Strategic Metal
1.2. Li-Ion Batteries
Cathode Type | LCO | LFP | LMO | NCA | NMC |
---|---|---|---|---|---|
Chemical formula | LiCoO2 | LiFePO4 | LiMn2O4 or LiMnO2 | Li(Ni0.8Co0.15Al0.05)O2 | LiNi0.33Co0.33Mn0.33O2–NMC111 LiNi0.5Co0.3Mn0.2O2–NMC532 LiNi0.6Co0.2Mn0.2O2–NMC622 LiNi0.8Co0.1Mn0.1O2–NMC811 |
Structure | Layered | Olivine | Spinel | Layered | Layered |
Year introduced | 1991 | 1996 | 1996 | 1999 | 2008 |
Safety | Moderate | Excellent | Very good | Good | Good |
Energy density | Very good | Good | Good | Excellent | Excellent |
Power density | Good | Very good | Very good | Very good | Good |
Lifespan | Good | Very good | Very good | Very good | Very good |
Cycle lifespan | Good | Very good | Good | Very good | Very good |
Performance | Very good | Very good | Good | Very good | Very good |
Cost | Poor | Very good | Very good | Good | Good |
Market share | Obsolete | Electric bikes, buses, and large vehicles | Small | Steady | Growing (from NMC 111 > NMC 532 > NMC 622 > NMC 811 to no-cobalt chemistries |
Specific density (Wh/g) | 200 | 120 | 140 | 245 | 200 |
Cycles (charge-discharge) | 1000 | 300 | 820 | 950 | 850 |
1.3. Urban Mining and Challenges for Sustainable Development
2. State-of-Art
2.1. Leaching of Li-Ion Batteries
2.1.1. Inorganic Acid Leaching
References | Li-Ion Battery Type | Leaching Agents | Conditions | Co Leaching Efficiency |
---|---|---|---|---|
Meshram et al. (2015) [43] | NMC | Leaching agent: H2SO4 Reducing agent: NaHSO3 | S/L ratio = 20 g/L; 1 M H2SO4 and 0.075 M NaHSO3; 4 h; 95 °C | 91.60% |
Chen et al. (2018) [50] | NMC | Leaching agent: H2SO4 Reducing agent: H2O2 | S/L ratio = 30 g/L; 1 M H2SO4; 4% v/v H2O2; 90 min; 70 °C | 98.5% Co |
Xuan et al. (2021) [51] | NMC | Leaching agent: HCl | S/L ratio = 20 g/L; 4 M HCl; 120 min; 82 °C | ~100% Co |
Vieceli et al. (2021) [52] | NMC | Leaching agent: H2SO4 | S/L ratio = 1/50; 2.5 M H2SO4; 60 min; 50 °C. Calcination at 500 °C for 90 min | 90% Co |
He et al. (2022) [47] | NMC | Assisted by ultrasound Leaching agent: H2SO4 | S/L ratio = 10 g/L; 1 M H2SO4; 250 W; 30 min; 90 °C | 30% Co |
Takahashi et al. (2020) [42] | LCO | Assisted by ultrasound Leaching agent: H2SO4 Reducing agent: H2O2 | S/L ratio = 1/5; pH 3; H2O2 dosage | 99% |
Chen et al. (2018) [53] | LCO, LMO, LFP, NMC | Leaching agent: H3PO4 Reducing agent: H2O2 | S/L = 1/50; 1 M H3PO4; 4% v/v H2O2; for 10 min; 40 °C | <20% Co (the goal was the Li extraction) |
2.1.2. Organic Acid Leaching
2.2. Consolidated Technologies for Co Separation
2.2.1. Solvent Extraction
2.2.2. Ion Exchange Resins
2.2.3. Precipitation
3. Emerging Technologies for Cobalt Separation
3.1. Ionic Liquids
3.1.1. Deep Eutectic Solvents
3.1.2. Supercritical Fluids
3.1.3. Nanotechnology
3.1.4. Biohydrometallurgy
- redoxolysis (reaction occurs as biooxidation and bioreduction)
- acidolysis (proton promotes dissolution with biogenic inorganic or organic acids)
- complexolysis (complexation promoted dissolution).
4. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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References | Li-Ion Battery Type | Leaching Agents | Conditions | Co Leaching Efficiency |
---|---|---|---|---|
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Esmaeili et al. (2020) [58] | NMC | Assisted by ultrasound: 37 kHz Leaching agent: lemon juice (citric acid = 90 mg/g, malic acid = 0.86 mg/g, and ascorbic acid 1.24 mg/g); Reducing agent: H2O2 | S/L ratio = 0.98% (w/v); 57.8% v/v lemon juice; 8.1% v/v H2O2 | 96% |
Sun et al. (2018) [62] | NMC (111) | Leaching agent: DL-malic Reducing agent: H2O2 | S/L ratio = 40 g/L; 1.2 M DL-malic; 1.5% v/v H2O2; 30 min 80 °C. | 94.3% |
Urias et al. (2020) [56] | LCO | Leaching agents: H2SO4, lactic, butyric, acetic and propionic; Reducing agents: H2O2 (6%, v/v), and glucose (0.09 mol/L) and lactose (0.09 mol/L) | S/L ratio = 20 g/L; 1.25 M H2SO4 + organic acids (from a fermentation effluent by an anaerobic microbial consortium) 0.75 M; 18.5 g/L; 300 rpm and 0.09 M lactose from MWP; 86 °C | 93.4% |
Golmohammadzadeh et al. (2017) [63] | LCO | Assisted by ultrasound Leaching agent: acetic acid Reducing agent: H2O2 | S/L ratio ratio = 30 g/L, citric acid = 2 M, 1.25% v/v H2O2; 2 h; 60 °C | 81% |
Nayaka et al. (2016a) [60] | LCO | Leaching agent: glycine Reducing agent: ascorbic acid | S/L ratio = 0.2 g LiCoO2/100 mL; 0.5 M glycine; 0.02 M ascorbic acid; 360 min; 80 °C | 95% |
Nayaka et al. (2016b) [64] | LCO | Leaching agent: tartaric acid Reducing agent: ascorbic acid | S/L ratio = 0.2 g LiCoO2/100 mL; 0.4 M tartaric acid; 0.02 M ascorbic acid; 5 h; 80 °C | >95% |
Ionic Liquid | Chemical Structure |
---|---|
Alkylammonium | |
Phosphonium | |
Dialkylimidazolium | |
N-alkyl pyridinium | |
Trifluoroacetate | |
Trifluorosulfonate | |
Tetrafluoroborate | |
Hexafluorophosphate | |
Bis(trifluoromethanesulfonyl)imide | |
Halides: chloride, bromide, iodide | Cl-, Br-, I- |
Nitrate, hydrogensulfate, sulfate | [NO3]-, [HSO4]-, [SO4]−2 |
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Botelho Junior, A.B.; Stopic, S.; Friedrich, B.; Tenório, J.A.S.; Espinosa, D.C.R. Cobalt Recovery from Li-Ion Battery Recycling: A Critical Review. Metals 2021, 11, 1999. https://doi.org/10.3390/met11121999
Botelho Junior AB, Stopic S, Friedrich B, Tenório JAS, Espinosa DCR. Cobalt Recovery from Li-Ion Battery Recycling: A Critical Review. Metals. 2021; 11(12):1999. https://doi.org/10.3390/met11121999
Chicago/Turabian StyleBotelho Junior, Amilton Barbosa, Srecko Stopic, Bernd Friedrich, Jorge Alberto Soares Tenório, and Denise Crocce Romano Espinosa. 2021. "Cobalt Recovery from Li-Ion Battery Recycling: A Critical Review" Metals 11, no. 12: 1999. https://doi.org/10.3390/met11121999
APA StyleBotelho Junior, A. B., Stopic, S., Friedrich, B., Tenório, J. A. S., & Espinosa, D. C. R. (2021). Cobalt Recovery from Li-Ion Battery Recycling: A Critical Review. Metals, 11(12), 1999. https://doi.org/10.3390/met11121999