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TOWARD LITFSI ECO-EFFICIENT MANUFACTURING AND
RECYCLING PROCESSES
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
François METZ Open Innovation responsible
SOLVAY Aroma Performance
STATE OF THE ART
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Reference : LiPF6 Since the pioneering Sony Li-ion cell (early’s 90), still
almost exclusively implemented in modern LiB
Competitor Li salts : LiClO4, LiAsF6, LiBF4, LiB(C6H5)4, LiCl, LiBr,
Li(O3SCH3) and LiOTf
Maybe the most promising :
LiTFSI (CF3SO2)2NLi
M. Armand, (1985, 1990)
OBJECTIVES
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
TO PROMOTE THE USE OF LiTFSI
• Comparative physic, chemical and cycling
properties,
• Reducing LiTFSI FMC :
• Optimising the manufacturing process,
• Setting-up a recycling procedure
STATE OF THE ART
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Physic and chemical
properties
→ standoff
LiPF6 LiTFSI
MW 152 287
% Li 4,7 2,42
g Li per mol 7,14 6,95
mp °C 195,5 235,8
decomposition
°C
(TGA)
107 > 330
H Yang, G. V. Zhuang, P. N. Ross Jr,
Journal of Power Sources 161 (2006) 573–579
Solvay internal results
Electrochemical
properties
→ standoff
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Viscosity
→ advantage LiTFSI
Water resistance
Operating conditions :
1% w/w H2O, 40°C, 60h
→ advantage LiTFSI
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Battery lifetime
→ advantage LiTFSI
Battery second life
→ advantage LiTFSI
SUMMARY
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Compared to LiPF6, LiTFSI displays
interesting properties : • Thermic stability
• Water resistance
• Viscosity
• Battery second life
• Battery lifetime
• Cell capacity after storage
as additive
To reduce it, 2 directions were proposed to Elibama : • LiTFSI manufacturing process : Optimisation of the chemical key
step (CF3CO2K sulfination)
• LiTFSI recycling : set-up of a scalable process
However, LiTFSI main drawback is its FMC
(Full Manufacturing Cost).
STATE OF THE
ART
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
SOLVAY
Competitor
s
: key steps
KEY STEP
CHARACTERISTICS
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Key step : TFAK sulfination
yiel
d %
conversion %
TFAK sulfination
An apparently simple reaction…
but with severe constraints…
• TFAK conversion has to be limited
to minimise TFSK degradation
• Remaining TFAK has to be
separated and recycled
1
1
11
• Identify reaction by-products
• Understand their formation pathways
• Evaluate their kinetics
• Establish a kinetic model
Identified and/or
quantified products
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Real time measurements :
[TFAK], [TFSK] : Raman in liquid phase
[CO2], [SO2], [CF3H],… : μGC in gas phase
Results assessed by 19F NMR
condensor
Gas meter
CST + Rushton
μGC
Raman
T °C
• Mastering CO2 and SO2 concentrations, both in liquid and gas
phases : in situ, on line analyses
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
7550
90
70
Conversion rate
Se
lecti
vit
y
Sulfination @ P atmo : performance curve
Current process
Targeted performance
Experimental Curve
ELIBAMA WP2
Progress linked to
X + 10
x
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Proof of concept established with a synthetic electrolyte
LiTFSI 65,4g 0,1mol
EC 114ml Homogeneous
DMC 114ml medium
CH2Cl2 225ml
water 450ml AL : LiTFSI 0,095mol 96%
OL : LiTFSI 0,0044mol 4%
dilution
LiTFSI recycling from synthetic electrolyte : 02GM059
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Extension to a « real case » : CEA used pouched cells
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Extension to a « real case » : CEA used pouched cells
• Separator PE/PP 110 x 3,5 cm
m = ~1,1g
• Cathode 38 x 3,3 cm
LiFePO4 (LFP) m = ~ 5,8 g
• Anode 46,5 x 3,2 cm
Graphite (G) m = ~ 4,5 g
17
17 ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
LiTFSI recycling :
Blocks diagramm 90% LiTFSI extraction
Further purification necessary
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
• Compared to LiPF6, LiTFSI displays interesting
physical, chemical and cycling properties ( 2
commercial flyers have been issued)
• The performances of its chemical process key step
has been significantly improvement (10%
selectivity gain → 7% FMC reduction)
• A scalable LiTFSI recovery process has been
developped,
• 2 patents have been issued (TFAK sulfination,
LiTFSI recycling)
But LiTFSI promotion still remains challenging
ELIBAMA STAKEHOLDERS CONFERENCE
Newcastle, Oct 14. 2014
Industrial implementation of the
optimised TFSK process (« New TFSK »)
scheduled for 2015,
Further improvements under progress