DRILL Determine the formation of the following ionic bonds. Li and Br Na and P.
Sodium Ion Batteries for Grid Storagepower-our-future-2012.cicenergigune.com/wp-content/... · 0.9V...
Transcript of Sodium Ion Batteries for Grid Storagepower-our-future-2012.cicenergigune.com/wp-content/... · 0.9V...
Sodium Ion Batteries for Grid
StorageMarca M. Doeff, Lawrence Berkeley National Laboratory
An early example of an Na ion cell
Na0.7CoO2/P(EO)8NaCF3SO3/Na15Pb4, 100°C, 0.5 mA/cm2
Doeff et al., J. Electrochem. Soc. 140 2726 (1993)
An uptick of interest in sodium
Interest in Li ionbatteries intensifies
Scopus- “sodium ion battery”
Lithium-Do we have enough?
Bolivia has lithium, and the president intends to make world pay for itBy Simon Romero
Published: Monday, February 2, 2009RECOMMEND
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UYUNI, Bolivia — In the rush to build the next generation of hybrid or electric cars, a sobering fact confronts both automakers and governments seeking to lower their reliance on foreign oil: almost half of the world's lithium, the mineral needed to power the vehicles, is found here in Bolivia - a country that may not be willing to surrender it so easily.
Source: NY Times, February 2, 2009
Lithium and batteries
Consumer batteries currently use >¼ of world’s lithium production
Research Center for Energy Economics (http://www.ffe.de/en/)
Vehicular applications will increase demand for lithium further. This will put pressure on prices.Current price=$500/kWh for EV cellsLarge format cells (grid storage) worsen the situation
Cost and production of lithium
http://www.lithiumsite.com/Lithium_Market.html
Chemetall SCL
and Silver Peak, NV
operations
SQM starts production
floods market
5000 $/ton
Li ion batteries
take off
Production can’t
keep pace1990s
2000s
Recession hits
Production drops
Prices level
Lithium supply security is the issue
• 2 brine operations in Chile dominate world market (others in Argentina, China, US)
• Hard rock ores (spodumene) are 13% of reserves, but more expensive to process
• Recycling is another source. As lower cost components (Mn, Fe, P) are used in batteries, recycling becomes less cost effective and less appealing
• Large amounts of recycled lithium will only become available after sufficient numbers of batteries reach the end of life (~10 years for vehicular batteries)
• Lithium supply security is a top priority for technical companies
“Lithium Use in Batteries” http://pubs.usgs.gov/circ/1371/pdf/circ1371_508.pdf
spodumene
Sodium Carbonate Price and Availability
http://minerals.usgs.gov/minerals/pubs/commodity/http://www.icis.com/
Trona ((Na3H(CO3)2.2H2O
Trona, CA (Searles dry lake bed)
Largest deposit of trona in the worldis in Green River, WY500,000 tons/yr�1.2 million tons in 201423 billion tons in reserveSearles Lake, Owens Lake, CA62 identified deposits in world, Kenya,Botswana, etc. (not all quantified)can obtain from brines and NaCl +limestoneMajor uses: glass, chemicals, soap
Na2CO3 from trona costs$165/ton (2012)
Materials Costs in Li ion Batteries
Source: “Costs of Lithium-Ion Batteries for Vehicles” Report,Center for Transportation Research, ANL, May 2000
Cathode, electrolyte, and separator are the most expensive componentsCathode-depends on cell design and type of material ~50%-13%For electrolytes: salt is 2/3 the cost.
2006 data for an HEVcell with spinelcathode
Raw Materials Cost of LiFePO4
Going from LiCoO2 to LiFePO4 will potentially reduce cathode costs from 50% to 10% of a high energy cell (Jugovich et al., J. Power Sources, 190, 538 (2009).Hydrothermal synthesis of LiFePO4 (Sudchemie) Carbothermal reduction (Valence Technologies)
�FeSO4.7H2O + H3PO4 + 3LiOH.H2O 0.5Fe2O3 +LiH2PO4+0.5C
reagentFeSO4
.7H2
OH3PO4 LiOH.H2O
g needed 278.01 115.3 125.88
$/kg* 99 24.05 67.75
cost $27.52 $2.77 $8.53
% of total($38.82)
71 7 22
*Aldrich, reagent grade
reagent Fe2O3 LiH2PO4 C
g needed 79.85 103.93 7.5**
$/kg* 38.80 154.60 10.00***
cost $3.10 $16.07 $0.075
% of total($19.245)
16.1 83.5 0.4
** 25% excess required*** Denka acetylene black
In some cases, the lithium source is the most expensive raw material
Raw Materials Cost of Manganese Oxidesusing lowest cost ingredients0.5LiOH.H2O + MnO2�0.5LiMn2O4 0.5NaOH + MnO2�Na0.5MnO2 (“Na0.44MnO2”)
reagent LiOH.H2O MnO2
g needed 20.98 78.94
$/kg* 67.75 31.56
cost $1.42 $2.49
% of total ($3.91)
36 64
* Aldrich, reagent grade
reagent NaOH MnO2
g needed 20 78.94
$/kg* 14.25 31.56
cost $0.285 $2.49
% of total ($2.775)
10.3 89.7
Using a sodium compound instead of a lithium compound lowers raw materials costs by about 1/3.
Cost of Electrolyte Salts
Salt $/kg* $/mol
LiPF6 3575 543.22
NaPF6 1792 300.96
LiCF3SO3 1685 262.88
NaCF3SO3 4400 757.06
Li2SO4 143.50 15.78
Na2SO4 24.60 3.49
LiClO4 271 28.83
NaClO4 140.80 17.24
* Aldrich reagent grade
Fluorinated anions dominate costBut what if we could use a nonfluorinated sodium salt?
What about energy density?
In dual intercalation systems, energy density is determinedmainly by the weight of the host. Na ion in theory could matchthe energy density of a Li ion system. Aqueous batteries willhave lower energy density than those with organic electrolytes
The Challenge
Identify a suitable anode material
Electrolyte dependent (organic or aqueous)
Carbon anodesNa intercalation into graphite is minimal (NaC64)
lattice mismatch? Dresselhaus and Dresselhaus, Adv. in Physics, 51, 1 (2002).
Na will co-intercalate with Cs and K (improves lattice match)
Na cannot reduce graphite sufficiently (in LixC6, most activity takes place at -2.94V vs. S.H.E., Na/Na+ -2.71V vs. S.H.E).
Disordered carbons are easier to reduce
Tirado et al. Electrochem. and Solid State Lett., 8, A222 (2005). Na/pyrolyzed resorcinol-formaldehyde cells, 285 mAh/gNa/NaClO4, EC-DEC/pyrolyzed glucose, 300 mAh/g
Dahn et al., J. Electrochem. Soc. 147, 1271 (2000)
Na/NaClO4, DME/Petroleum coke
Doeff et al. J. Electrochem. Soc., 140, L169 (1993).
Carbon anodes-a “capbattery”Na0.44MnO2/Na2SO4, H2O/activated carbon
44Tech, Inc. (now Aquion)Received $5 million from DOE for grid storage
Aqueous Electrolytes-Considerations
• Select anodes and cathodes stable in water (Na2SO4, Na3PO4, NaOHsolution)
• Some leeway, especially for cathode, since oxygen evolution is slow
• High pH needed to minimize dissolution and proton intercalation (buffer)
• Operating outside voltage stability window may generate protons
• Materials should be robust (layered structures may co-intercalate water).
• Cheap, readily available, environmentally friendly
Pourbaix diagram
pH region of interest
NaxMnO
2
Find anode here
sodium titanates
Na-Ti-O phase diagram from the Materials Projecthttp://www.materialsproject.org/
TiO2-R
O2
TiO2
Na2O
Na4TiO4
Na2Ti3O7
Na2Ti6O13
Na2O2
NaO2
NaO3
x16:10:28x4:3:8
x4:5:12x 2:4:9
x x2:7:152:9:19
Na2Ti6O13
Na2Ti3O7
Na4Ti5O12
Cost and Resource Availability Calculations
Methods from Wadia, Albertus, Srinivasan., J. Power Sources 196 (2011) 1593.Estimates for Na ion systems courtesy of Paul Albertus, Bosch
Raw materials costs Production ReservesLimiting Material
Results Na2Ti3O7
Palacin et al., Chem. Mater. 2011, 23, 4109–4111
0.5
1
1.5
2
2.5
3
0 10 20 30 40 50
Ew
e/V
DchCap1
vs. Li
vs. Na
Sodium insertion processes reported in2011 by Palacin et. al. 0.3V vs. Na/Na+
But 1.5V vs Li/Li+!Not good for aqueous electrolytes, but could be used with organic electrolytes
200 mAh/g
Results Na2Ti6O13
Na2Ti6O13
0.5
1
1.5
2
2.5
3
0 20 40 60 80 100 120 140
Pote
ntial (V
)
Capacity (mAh/g)
vs. LiSolid state synthesis
0.9V (sloping) vs Na/Na+, 1.5V/1V vs. Li/Li+
Na cell capacity of about 55 mAh/g reversibleCorresponds to filling of 4i sites (2/3 full in as-made materialFor Li: capacity depends on identity of A in A2Ti6O13 (Perez-Flores et al., J. Power Sources,
196, 1378 (2011).
vs. Na
Results: Nasicon NaTi2(PO4)3
Solid state synthesis
135 mAh/g at 2V vs Na/Na+
Good candidate for Gen 1 aqueous cellsPair with 3V cathodes like Na0.44MnO2 or Na2FePO4F
Doeff et al., J. Electrochem. Soc.,141, L145 (1994). Doeff et al., Mat. Res. Soc. Proc., 393, 107 (1995).
Na0.44MnO2 Cathode Material
Na1
Na2 Na3
Easily synthesized by solid state methods, hydrothermal, sol-gel, combustion methods, etc.Partially sodiated in the as-made stateNa0.66MnO2=fully sodiated state~170 mAh/g theoreticalVery good reversibility for Na (and Li)
Na0.44MnO2 cycling
Liu et al, Adv. Mater., 23, 3155 (2011)
Na/NaClO4 EC-DMC/nanowires
Whitacre et al., Electrochem. Commun. 12, 463 (2010)
Activated C/Na2SO4, H2O/Na0.44MnO2
Na0.44MnyTi1-yO2
Solid solutions for 0≤y≤0.55
y=0 y=0.11
y=0.22 y=0.33
y=0.44 y=0.55
Stepped potential experimentsin lithium cells. Highest capacities fory=0.22.
Ti substitution slows (stops?) Mn dissolutionin electrolyte solution at 55°C
Doeff et al., J. Power Sources, 135, 240 (2004).Doeff et al., J. Power Sources, 165, 573, (2007).
Na0.44MnO2 as a cathode… and an anode!
Na0.44MnO2/Na0.44MnO2 cell
Thanks to:Lawrence Berkeley National Lab for an LDRDExploratory Research Program (ETR), now BATT for funding old workCIC Energigune for supporting our Na ion effort
View of the San Francisco Bay from LBNL
Cyclotron at night