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This project has received funding from the European Union’s Horizon 2020
research and innovation programme under grant agreement No 776851
Lithium-Ion Batteries towards Circular
Economy: a Literature Review of
Opportunities and Issues of Recycling
Treatments
E. Mossali, N. Picone, O. Rodríguez, J.M. Pérez, M.
Colledani
Summary
• CarE-Service Project: motivation, concept and partnership
• Introduction
• Circular economy for Li-ion batteries
• Waste preparation and pre-treatment processes
• Hydrometallurgical processes
• Pyrometallurgical processes
• Industrial processes and patents
• Conclusions
• Jobplaces and welfare
(12 million jobplaces, 780 billion
turnover, 140 billion value added)
• Citizens’ quality of life
• Environmental sustainability
• Sustains other supply chains
(materials, electronics, machine tools,
automation, …)
• Triggers innovation in other sectors
Project motivation: The paradigm shift in automotive industry
Automotive
industry
one of the most
relevant manufacturing
industries in Europe
By 2040
the 35% of the
newly sold vehicles
will be electric
Paradigm shift
Traditional
fuel cars
Electric &
Hybrid Electric
Vehicles
(E&HEVs)
• Redesign E&HEVs for circular economy
• Develop EU leadership in advanced
technologies for re-use of E&HEVs
• Reduce TCO of E&HEVs
• Create new value chains and businesses in
EU around Circular Economy of E&HEVs
The concept of CarE-Service
New
technologies
and business
models for
re-use value
chains
Innovative
mobility
services for
citizens
based on
E&HEVs
• Increase citizens’ quality of life
through circular economy of E&HEVs
• Increase market acceptance and
change consumers’ behavior
• Guarantee return-flow of E&HEVs
• Increase market of innovative services
• Create a suitable regulatory framework
Concept
Partnership
Introduction: Li-ion batteries
Cell components Chemical composition %wt. Additional information
External casing
Fe-Ni alloy 20-26 Steel case is typical of cylindrical cells.
Aluminium case is found in prismatic cells.Al 10
Cathode 25-30
Aluminium Al Current collector foil 5-8
Binder Usually PVDF 1-2
Alternatives: PTFE, butadiene-styrene or
modified cellulose.
Metal oxide Li 1.5-7
LCO gives better performances but is highly
expensive. It is replaced by NMC, LMO
(where Mn gives structural stability) or C-
coated LFP (LiFePO4) that is safer.
Co LCO (LiCoO2) 5-20
Ni
LNO (LiNiO2)
NCA (LiNi0.8Co0.15Al0.05O2) 5-10
Mn LMO (LiMnO2)
NMC (LiNixCoyMnzO2)
5
Polymeric separator Microporous PP or PE 4-10
Electrolyte 10-15 EC is the most used organic solvent, combined
with others to lower its high melting T.
LiPF6 has high conductivity in any medium.
Li salts LiPF6, LiAsF6, LiClO4, LiBF4
Organic solvents DMC-EC, PC-DME, BL-THF
Anode 15-25
Copper Cu Current collector foil 8-10
Binder Usually PVDF 1-2
Inert, thermo-resistant and current-resistant
binder helping the adhesion.
Graphite 15-17
Low storage capacity of graphite (372
mAh/g).
Alternatives: C-NT, Sn compounds, metallic
NP.
Circular economy for Li-ion batteries
Circular economy for Li-ion batteries
Process
Value (US $/ton)
2001 2017
Cathode
Al 1,250 2,000
Li 7,500 9,000
Co 38,000 55,000
Ni 8,600 10,000
Mn 1,100 2,000
Anode
Cu 1,800 5,500
Graphite 550 1,000
Economic value of Li-ion batteries components
Circular economy for Li-ion batteries
Waste preparation and pre-treatment processes
✗ Ionic contamination
Waste preparation
Aim: lower the risks associated to the LIBs handling, manipulation
and treatment due to the presence of residual energy
• Discharge (salts saturated solution)
Pre-treatments Processes: Objectives
1) Enrichment of metallic fraction
2) Reduction of scrap volumes
3) Reduction of energy consumption
4) Improvement of recovery rate
5) Improvement of the management safety issues
Pre-treatments are necessary before hydrometallurgical processes to minimize
the presence of impurities
Pre-treatments: Thermal Processes
1) Calcination
2) Oxygen-free roasting
3) Enclosed-vacuum environment
4) Vacuum pyrolysis
✔ Cell opening and deactivation
✔ Binder and organic compound removal
✔ Easiness
✔ Economically sustainable
✗ Cu corrosion
✗ Toxic gaseous emmision
✗ High energy consumption
Pre-treatments: Mechanical Processes
• Grinding
✔ Valuable metal segregation ✗ Not complete segregation
Pre-treatments: Physical Processes
1) Sieving
2) Ultrasonic washing
3) Floatation
✔ Scrap volume reduction
✔ Reduces costs and high throughput
✔ Flexibility
✔ Increased hydrometallurgical selectivity
✔ Low energy consumption
✔ No external impurities
✗ Impurities
✗ Gaseous emissions
✗ Cathodic powder input
✗ LiCoO2-graphite contamination
Pre-treatments: Chemical Processes
1) Electrolyte dissolution
2) Binder dissolution
✗ Wastewater production
Pre-treatments: Mechano-chemical Processes
✔ Room temperature
✔ Low energy consumption
✔ Simple procedure
✔ Economically sustainable
✔ Environmentally-friendly
✗ Long reaction times
✗ Noise generation
✔ Complete dissolution
Hydrometallurgical processes
Leaching agent
Metal recovery rates
Li (%) Co (%)
Organic Oxalate 98 97
Ascorbic acid 98 95
Acetic acid 75 30
Lactic acid + H2O2 98 99
Iminodiacetic acid + H2O2 99 91
Maleic acid 100 97
DL-malic acid + H2O2 91 84
Citric acid + H2O2 92 84
Citric acid + H2O2 99 98
Citric acid + H2O2 100 90
Citric acid + H2O2 100 100
Citric acid + TW 98 96
Succinic acid 100 96
Tartaric acid + H2O2 99.1 98.6
Hydrometallurgical processes
Leaching agent
Metal recovery rates
Li (%) Co (%)Inorganic
H2SO4/HNO3/HCl >80 100
H2SO4 + NaHSO3 96.7 91.6
H2SO4 + H2O2 >99.7 >99.7
NH3 +(NH4)2SO3+(NH4)2CO3 - 80
Inorganic
+organic
Phosphoric acid + glucose 100 98
Pyrometallurgical processes
1) Pyrolysis: the thermal degradation of organic LIBs components
2) Metals reduction: the production of metal alloys using ≈1500°C
and proper reductive agents
3) Gas incineration: the pyrolysis and quenching of gases at
≈1000°C to avoid dioxins release
The initial pyrolysis of electrolyte and plastic could be used to supply energy for metals
recovery, when in the shaft furnace is obtained the valuable alloy containing Cu, Co, Ni and
Fe
Hydrometallurgical Processes
✗ High energy consumption
✗ Hazardous gaseous emissions
✗ Material loss (Li in the slag)
✗ Need of Co LIBs chemistries
Pyrometallurgical Processes
✔ High recovery efficiency
✔ Moderate energy consumption
✔ No gaseous emissions
✔ Recovery of all LIBs cathodics metals
✔ Mild reaction conditions
✗ Wastewater productions
✗ Incomplete binder/electrolyte recyclin
✗ Complexity of the procedure
✗ Need of pre-treatments
✗ Selectivity of reagents
✔ Easiness of the procedure
Industrial processes and patents
Company Process type Capacity Recovery
Accurec GmBH
(Germany)
Pyrometallurgy
Hydrometallurgy
4000 ton/year
Co-alloy
Li (slag)
AEA Technology
(UK)
Hydrometallurgy
Electrolysis
-
LiOH
CoO
Akkuser Ltd
(Finland)
Pre-treatment 4000 ton/year Metal powders
Batrec Industrie AG
(Switzerland)
Hydrometallurgy 200 ton/year
Glencore plc (Xstrata)
(Canada, Norway)
Pyrometallurgy
Hydrometallurgy
7000 ton/year Metal alloys
Imteco
(USA)
Pyrometallurgy 6000 ton/year Co-alloy
Lithorec
(Germany)
Hydrometallurgy -
CoO
Li salts
OnTo Technology
(USA)
Pre-treatment - Metal powders
Recupyl (Valibat Process)
(France)
Hydrometallurgy 110 ton/year
Co(OH)2
Li2CO3
Retriev Technology (Toxco)
(Canada)
Hydrometallurgy 4500 ton/year
CoO
Li2CO3
SNAM
(France)
Pre-treatmen 300 ton/year Electrode powder
Sony (Sumimito Process)
(Japan)
Pyrometallurgy
Hydrometallurgy
150 ton/year CoO
Umicore (Val’eas Process)
Belgium
Pyrometallurgy
Hydrometallurgy
7000 ton/year
LiCoO2
Ni(OH)2
Industrial Processes and Patents
✔ Accurec GmBH (Germany): 4000 ton/year
★ Co-alloy
★ Li slag
✔ Glencore plc (Xstrata) (Canada, Norway): 7000 ton/year
★ Metals alloy
✔ Sony(Sumimoto Process) (Japan): 150 ton/year
★ CoO
✔ Umicore (Val’eas Process) (Belgium): 7000 ton/year
★ LiCoO2
★ Ni(OH)2
Ø Pyrometallurgy + Hydrometallurgy Processes
Ø Hydrometallurgy Processes
✔ Batrec Industries (Switzerland): 200 ton/year
★ Valuable metals
Lithorec (Germany): 4000 ton/year
★ CoO
★ Li salts
✔ Recupyl (Valibat Processs) (France): 110 ton/year
★ Co(OH)2
★ Li2CO3
✔ Retriev Technology (Toxco) (Canada): 4500 ton/year
★ CoO
★ Li2CO3
Conclusions
• Rechargeable LIBs are the prominent technology to store energy in
portable devices, EVs and energy systems.
• The unavoidable increase of LIBs usage and production is
accompanied by a spasmodic race for raw materials, reduction of costs
and always new and powerful pack design and assembly.
• The increasing amount of wasted LIBs is becoming an urgent issue to
face in order to protect the environment from pollution, to save the
natural resources from an unrestrainable mining and to avoid safety
hazards for humans.
Conclusions
•All the technical solutions investigated in this paper underline the strong
fragmentation of current processes and the economic and environmental
barriers to be faced in the near future, when the return amounts of LIBs
will become significant. A final huge effort should be done to summarize
all achievements in a unique, environmentally-friendly and efficient
recycling process.
This project has received funding from the European Union’s Horizon 2020
research and innovation programme under grant agreement No 776851
www.csic.es
www.cenim.csic.es
olga.rodriguez@csic.es

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Lithium-Ion Batteries towards Circular Economy: A Literature Review of Opportunities and Issues of Recycling Treatments

  • 1. This project has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 776851 Lithium-Ion Batteries towards Circular Economy: a Literature Review of Opportunities and Issues of Recycling Treatments E. Mossali, N. Picone, O. Rodríguez, J.M. Pérez, M. Colledani
  • 2. Summary • CarE-Service Project: motivation, concept and partnership • Introduction • Circular economy for Li-ion batteries • Waste preparation and pre-treatment processes • Hydrometallurgical processes • Pyrometallurgical processes • Industrial processes and patents • Conclusions
  • 3. • Jobplaces and welfare (12 million jobplaces, 780 billion turnover, 140 billion value added) • Citizens’ quality of life • Environmental sustainability • Sustains other supply chains (materials, electronics, machine tools, automation, …) • Triggers innovation in other sectors Project motivation: The paradigm shift in automotive industry Automotive industry one of the most relevant manufacturing industries in Europe By 2040 the 35% of the newly sold vehicles will be electric Paradigm shift Traditional fuel cars Electric & Hybrid Electric Vehicles (E&HEVs)
  • 4. • Redesign E&HEVs for circular economy • Develop EU leadership in advanced technologies for re-use of E&HEVs • Reduce TCO of E&HEVs • Create new value chains and businesses in EU around Circular Economy of E&HEVs The concept of CarE-Service New technologies and business models for re-use value chains Innovative mobility services for citizens based on E&HEVs • Increase citizens’ quality of life through circular economy of E&HEVs • Increase market acceptance and change consumers’ behavior • Guarantee return-flow of E&HEVs • Increase market of innovative services • Create a suitable regulatory framework
  • 7. Introduction: Li-ion batteries Cell components Chemical composition %wt. Additional information External casing Fe-Ni alloy 20-26 Steel case is typical of cylindrical cells. Aluminium case is found in prismatic cells.Al 10 Cathode 25-30 Aluminium Al Current collector foil 5-8 Binder Usually PVDF 1-2 Alternatives: PTFE, butadiene-styrene or modified cellulose. Metal oxide Li 1.5-7 LCO gives better performances but is highly expensive. It is replaced by NMC, LMO (where Mn gives structural stability) or C- coated LFP (LiFePO4) that is safer. Co LCO (LiCoO2) 5-20 Ni LNO (LiNiO2) NCA (LiNi0.8Co0.15Al0.05O2) 5-10 Mn LMO (LiMnO2) NMC (LiNixCoyMnzO2) 5 Polymeric separator Microporous PP or PE 4-10 Electrolyte 10-15 EC is the most used organic solvent, combined with others to lower its high melting T. LiPF6 has high conductivity in any medium. Li salts LiPF6, LiAsF6, LiClO4, LiBF4 Organic solvents DMC-EC, PC-DME, BL-THF Anode 15-25 Copper Cu Current collector foil 8-10 Binder Usually PVDF 1-2 Inert, thermo-resistant and current-resistant binder helping the adhesion. Graphite 15-17 Low storage capacity of graphite (372 mAh/g). Alternatives: C-NT, Sn compounds, metallic NP.
  • 8. Circular economy for Li-ion batteries
  • 9. Circular economy for Li-ion batteries Process Value (US $/ton) 2001 2017 Cathode Al 1,250 2,000 Li 7,500 9,000 Co 38,000 55,000 Ni 8,600 10,000 Mn 1,100 2,000 Anode Cu 1,800 5,500 Graphite 550 1,000 Economic value of Li-ion batteries components
  • 10. Circular economy for Li-ion batteries
  • 11. Waste preparation and pre-treatment processes
  • 12. ✗ Ionic contamination Waste preparation Aim: lower the risks associated to the LIBs handling, manipulation and treatment due to the presence of residual energy • Discharge (salts saturated solution)
  • 13. Pre-treatments Processes: Objectives 1) Enrichment of metallic fraction 2) Reduction of scrap volumes 3) Reduction of energy consumption 4) Improvement of recovery rate 5) Improvement of the management safety issues Pre-treatments are necessary before hydrometallurgical processes to minimize the presence of impurities
  • 14. Pre-treatments: Thermal Processes 1) Calcination 2) Oxygen-free roasting 3) Enclosed-vacuum environment 4) Vacuum pyrolysis ✔ Cell opening and deactivation ✔ Binder and organic compound removal ✔ Easiness ✔ Economically sustainable ✗ Cu corrosion ✗ Toxic gaseous emmision ✗ High energy consumption
  • 15. Pre-treatments: Mechanical Processes • Grinding ✔ Valuable metal segregation ✗ Not complete segregation Pre-treatments: Physical Processes 1) Sieving 2) Ultrasonic washing 3) Floatation ✔ Scrap volume reduction ✔ Reduces costs and high throughput ✔ Flexibility ✔ Increased hydrometallurgical selectivity ✔ Low energy consumption ✔ No external impurities ✗ Impurities ✗ Gaseous emissions ✗ Cathodic powder input ✗ LiCoO2-graphite contamination
  • 16. Pre-treatments: Chemical Processes 1) Electrolyte dissolution 2) Binder dissolution ✗ Wastewater production Pre-treatments: Mechano-chemical Processes ✔ Room temperature ✔ Low energy consumption ✔ Simple procedure ✔ Economically sustainable ✔ Environmentally-friendly ✗ Long reaction times ✗ Noise generation ✔ Complete dissolution
  • 17. Hydrometallurgical processes Leaching agent Metal recovery rates Li (%) Co (%) Organic Oxalate 98 97 Ascorbic acid 98 95 Acetic acid 75 30 Lactic acid + H2O2 98 99 Iminodiacetic acid + H2O2 99 91 Maleic acid 100 97 DL-malic acid + H2O2 91 84 Citric acid + H2O2 92 84 Citric acid + H2O2 99 98 Citric acid + H2O2 100 90 Citric acid + H2O2 100 100 Citric acid + TW 98 96 Succinic acid 100 96 Tartaric acid + H2O2 99.1 98.6
  • 18. Hydrometallurgical processes Leaching agent Metal recovery rates Li (%) Co (%)Inorganic H2SO4/HNO3/HCl >80 100 H2SO4 + NaHSO3 96.7 91.6 H2SO4 + H2O2 >99.7 >99.7 NH3 +(NH4)2SO3+(NH4)2CO3 - 80 Inorganic +organic Phosphoric acid + glucose 100 98
  • 19. Pyrometallurgical processes 1) Pyrolysis: the thermal degradation of organic LIBs components 2) Metals reduction: the production of metal alloys using ≈1500°C and proper reductive agents 3) Gas incineration: the pyrolysis and quenching of gases at ≈1000°C to avoid dioxins release The initial pyrolysis of electrolyte and plastic could be used to supply energy for metals recovery, when in the shaft furnace is obtained the valuable alloy containing Cu, Co, Ni and Fe
  • 20. Hydrometallurgical Processes ✗ High energy consumption ✗ Hazardous gaseous emissions ✗ Material loss (Li in the slag) ✗ Need of Co LIBs chemistries Pyrometallurgical Processes ✔ High recovery efficiency ✔ Moderate energy consumption ✔ No gaseous emissions ✔ Recovery of all LIBs cathodics metals ✔ Mild reaction conditions ✗ Wastewater productions ✗ Incomplete binder/electrolyte recyclin ✗ Complexity of the procedure ✗ Need of pre-treatments ✗ Selectivity of reagents ✔ Easiness of the procedure
  • 21. Industrial processes and patents Company Process type Capacity Recovery Accurec GmBH (Germany) Pyrometallurgy Hydrometallurgy 4000 ton/year Co-alloy Li (slag) AEA Technology (UK) Hydrometallurgy Electrolysis - LiOH CoO Akkuser Ltd (Finland) Pre-treatment 4000 ton/year Metal powders Batrec Industrie AG (Switzerland) Hydrometallurgy 200 ton/year Glencore plc (Xstrata) (Canada, Norway) Pyrometallurgy Hydrometallurgy 7000 ton/year Metal alloys Imteco (USA) Pyrometallurgy 6000 ton/year Co-alloy Lithorec (Germany) Hydrometallurgy - CoO Li salts OnTo Technology (USA) Pre-treatment - Metal powders Recupyl (Valibat Process) (France) Hydrometallurgy 110 ton/year Co(OH)2 Li2CO3 Retriev Technology (Toxco) (Canada) Hydrometallurgy 4500 ton/year CoO Li2CO3 SNAM (France) Pre-treatmen 300 ton/year Electrode powder Sony (Sumimito Process) (Japan) Pyrometallurgy Hydrometallurgy 150 ton/year CoO Umicore (Val’eas Process) Belgium Pyrometallurgy Hydrometallurgy 7000 ton/year LiCoO2 Ni(OH)2
  • 22. Industrial Processes and Patents ✔ Accurec GmBH (Germany): 4000 ton/year ★ Co-alloy ★ Li slag ✔ Glencore plc (Xstrata) (Canada, Norway): 7000 ton/year ★ Metals alloy ✔ Sony(Sumimoto Process) (Japan): 150 ton/year ★ CoO ✔ Umicore (Val’eas Process) (Belgium): 7000 ton/year ★ LiCoO2 ★ Ni(OH)2 Ø Pyrometallurgy + Hydrometallurgy Processes Ø Hydrometallurgy Processes ✔ Batrec Industries (Switzerland): 200 ton/year ★ Valuable metals Lithorec (Germany): 4000 ton/year ★ CoO ★ Li salts ✔ Recupyl (Valibat Processs) (France): 110 ton/year ★ Co(OH)2 ★ Li2CO3 ✔ Retriev Technology (Toxco) (Canada): 4500 ton/year ★ CoO ★ Li2CO3
  • 23. Conclusions • Rechargeable LIBs are the prominent technology to store energy in portable devices, EVs and energy systems. • The unavoidable increase of LIBs usage and production is accompanied by a spasmodic race for raw materials, reduction of costs and always new and powerful pack design and assembly. • The increasing amount of wasted LIBs is becoming an urgent issue to face in order to protect the environment from pollution, to save the natural resources from an unrestrainable mining and to avoid safety hazards for humans.
  • 24. Conclusions •All the technical solutions investigated in this paper underline the strong fragmentation of current processes and the economic and environmental barriers to be faced in the near future, when the return amounts of LIBs will become significant. A final huge effort should be done to summarize all achievements in a unique, environmentally-friendly and efficient recycling process.
  • 25. This project has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 776851 www.csic.es www.cenim.csic.es olga.rodriguez@csic.es