Recycling of discarded Li-Ion batteries (LIBs)cc.oulu.fi/~kamahei/q/NRD8/Kero.pdf ·...
Transcript of Recycling of discarded Li-Ion batteries (LIBs)cc.oulu.fi/~kamahei/q/NRD8/Kero.pdf ·...
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Recycling of discarded Li-Ion batteries (LIBs)
Nordic Recycling Day VIII 27th of September 2017
Jakob Kero
PhD student LTU
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Outline
• Introduction to Li-ion battery market
• Li-ion battery composition and recycling
• Project: Recycling of spent Li-ion batteries
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Photo: Ssuaphoto
Introduction - Where are LIBs used? • Li-ion batteries are used in many applications • Increasing political and consumer focus on climate change
• Increase electric vehicle (EV) production • Increased lithium-ion battery (LIB) production
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Photo: Ssuaphoto
Introduction - Where are LIBs used?
1,67 1,78 1,79 4,04 5,89 12,48 60,65 179,23
383,09
706,77
1256,9
0
200
400
600
800
1000
1200
1400
2005 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015
Cars
(tho
usan
ds)
Year
Electric car stock (BEV and PHEV), 2005-15 (thousands)
Source: © OECD/IEA 2016, Global EV Outlook 2016, IEA Publishing
Almost 0.9% of
car market
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• Li-ion batteries are used in many applications • Increasing political and consumer focus on climate change
• Increase electric vehicle (EV) production • Increased lithium-ion battery (LIB) production
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Introduction - Why LIBs? • LIB is an important technology for electric vehicle (EV) – high specific
power, energy density and lifetime
• Ongoing development of battery composition
Development of battery energy density and cost
Source: © OECD/IEA 2016, Global EV Outlook 2016, IEA Publishing 5
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Introduction - Why LIBs? • LIB is an important technology for electric vehicle (EV) – high specific
power, energy density and lifetime
• Ongoing development of battery composition
Development of battery energy density and cost
Source: © OECD/IEA 2016, Global EV Outlook 2016, IEA Publishing
Energy density: 30-50 Wh/kg Lead acid battery 110-160 Wh/kg Li-ion battery
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LIB composition – What’s inside? • Cathode
• Lithium metal oxide, LiMeO2, graphite and PVDF binder on Al-foil
• Metals used: i.e. Co, Ni, Mn, Al, Fe
• Anode • Carbon and PVDF binder on Cu-foil
• Electrolyte • Li salts and organic solvents (flammable).
• Casing • Steel (Fe, Cr, Ni), Al
• Complex material to recycle
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Fig 2: Prismatic design of a battery (Battery, 2003)
Cathode Anode
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LIB recycling – challenges!
• Existing high temperature recycling process • Based on Co and Ni recovery
• Short circuiting / thermal runaway • Need of pre-treatment
• Battery chemistries • Development of cathode active material
• What to recycle in the future?
System Electrodes
NCA Graphite LFP(phosphate) Graphite
MS (spinel) Graphite
Positive (Cathode)
LiNi0.8Co0.15Al0.05O2
LiFePO4
LiMn2O4
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Recycling of spent LIBs project Recap:
• Increasing volumes of end of life LIBs
• Ongoing development of battery chemistry
• Recycling in existing processes
Aim:
• To investigate thermochemical feasibility of the processes – FactSage • To recycle spent LIBs in copper pyrometallurgical process
• Distribution of Li and Co between phases
Cu-system • Slag: Fe2SiO4 +
(CaO) • Matte: Cu2S • Metal: Cu
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FactSage results
Validation with experimental work!
Li to gas phase: • T increase >1300℃ • CaO addition • <logPO2 (-10)
Co to matte phase: • CaO addition • <logPO2(-10)
Slag
Matte
Atm. Ar
Li
(Li)
Co
(Co)
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Experimental method
Sample • Slag, Fe2SiO4 50g • Matte, Cu2S 75g • Metal, Cu 25g • 5% LiCoO2 (constant) • CaO addition
Parameter Low value Middle value High value
Temperature 1250℃ 1350℃ 1450℃
Fe/SiO2 1 1.3 1.6
CaO addition 0 wt.% 5 wt.% 10 wt.%
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• Inert atmosphere
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0,00
0,20
0,40
0,60
0,80
1,00
1,20
1,40
N1 N2 N3 N4 N5 N6 N7 N8 N9 N10 N11
Cont
ent (
%)
Samples
Li-content (wt.%)
Li, slag % Li, matte % Li, metal %
Experiment results – Li - CaO add
No CaO
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CaO add
Lithium in slag phase
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Experimental results – Li mass bal.
• No CaO addition • 88% Li in slag
• CaO addition 10% • 35% Li loss
• CaO addition 5% • 56% Li loss
• No/small effect
of Fe/SiO2 ratio
2,02 2,74 1,77 2,25 1,91 2,78 3,09 6,29 2,71 1,82 2,67
88,0 89,1 89,1 86,1
58,1 61,4 49,3
53,5
35,2 40,7 34,5
10,0 8,1 9,2 11,6
40,0 35,8 47,7
40,1
62,0 57,5 62,8
0
10
20
30
40
50
60
70
80
90
100
N1 N2 N3 N4 N5 N6 N7 N8 N9 N10 N11
Phas
e di
strib
utio
n (%
)
Sample
Li – mass balance (%) Li metal Li matte Li slag Li gas
CaO add 5 % CaO add.10 % No CaO add.
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Experimental results – Li
• Middle-point samples N9-N11
• Glassy amorphous slag • Verified by XRD and SEM • Consistent for all 3 samples • Most of Li reported as loss
(58-63 mass%)
Position [°2Theta] (Copper (Cu))
20 30 40 50 60 70
Counts
0
500
1000
Fredrik run 1580 1 hour ny_N9_slagg_1timme
Homogeneous phase
Conditions • T 1350°C • Fe/SiO2 1.3 • CaO add 5%
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0,00
1,00
2,00
3,00
4,00
5,00
6,00
7,00
N2 N4 N6 N8 N1 N3 N5 N7 N9 N10 N11
Cont
ent (
%)
Samples
Co, slag % Co, matte % Co, metal %
Experiment results – Co - Temp
15
1450°C
1250°C
Cobalt in metal phase
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0,00
1,00
2,00
3,00
4,00
5,00
6,00
7,00
N2 N4 N6 N8 N1 N3 N5 N7 N9 N10 N11
Cont
ent (
%)
Samples
Co, slag % Co, matte % Co, metal %
Experiment results – Co - Temp
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1250°C
1450°C
Cobalt in slag phase
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Experimental results – Co mass bal. • 1450°C
• 66% Co in metal
• 1250°C • 52% Co in
slag
• No/small effect of Fe/SiO2 ratio and CaO add
28,2 29,0 37,4
22,3 20,8 23,1 26,5 24,1 21,2 28,1
20,0
63,4 65,2 57,8
76,9
11,1 12,4
16,8 11,0
33,5 23,8
56,2
6,3 2,6 1,3 1,3
48,7 39,7
53,6 65,6 16,4
32,6
10,4
2,1 3,2 3,5
19,4 24,8
3,1
28,9 15,4 13,3
0,0
10,0
20,0
30,0
40,0
50,0
60,0
70,0
80,0
90,0
100,0
N2 N4 N6 N8 N1 N3 N5 N7 N9 N10 N11
Phas
e di
strib
utio
n Co
(%)
Samples
Co - mass balance (%) Matte Co distr(%) Metal Co distr(%) Slag Co distr(%) Loss Co distr(%)
T 1350°C T 1250°C T 1450°C.
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Summary
• Li is distributed between slag and gaseous phases (loss)
• CaO addition reduces the amount of Li reported to the slag phase
• Co is distributed between slag, matte and metal(mainly) phases
• Co is at 1250⁰C dissolved into the main slag phase • Co is at 1450⁰C in the metal phase and as diffused
metal droplets in the slag and matte phase • Co in matte phase as inclusions (metal droplets) –
no dissolution.
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Further work
• Investigate the influence of adding other metals as Al, Mn, Ni to the system
• Further investigation with spent LIBs instead of LiCoO2 addition to the Cu-system
• Pre-treatment of batteries, physical separation
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Thank you for your attention!
Project partners: Stena Recycling AB
KTH Chalmers