Steven J. Visco, Eugene Nimon, Bruce Katz, May-Ying Chu, and
Lutgard De Jonghe
PolyPlus Battery Company
2431 5th Street, Berkeley, CA 94710
[email protected]
Scalable Energy Storage: Beyond Li-Ion, Almaden Institute, August 26, 27, 2009
LITHIUM/AIR SEMI-FUEL CELLS: HIGH
ENERGY DENSITY BATTERIES BASED
Technologies Under
Development
•
Lithium/Sulfur - rechargeable (licensed product)
•
Lithium/Air - (primary & secondary)
Water-stable, Li
+conductive
solid electrolyte
Li/Aqueous Batteries?
Lithium reacts with water:
Li + H
2O = LiOH + 1/2 H
2Unstable to reduction by Li
Li
+electrolyte stable to both
lithium metal & solid electrolyte
Lithium Electrode
SOLID ELECTROLYTES
•
Lisicon - LiM
2(PO
4)
3σ
=10
-4to 10
-3S/cm
•
RbAg
4I
5σ
=0.27 S/cm
•
Na-
β
”
-alumina
σ
=0.2 S/cm (350
oC)
•
LiI
•
Li
2S
•
P
2S
5σ
=10
-3S/cm
•
LiPON (Li
3PO
4N
x)
σ
=10
-6S/cm
Solid-State PLE
Solid-state protected anode - Cycling of solid-state protected anode in 1M LiOH at varying current densities: 1) 1 mA/cm2; 2) 5 mA/cm2; 3) 10 mA/cm2; 4) 15 mA/cm2; 5) 1 mA/cm2
U.S. Patent 7,491,458; “Active metal fuel cells,” S.J. Visco; Y.S. Nimon, B D. Katz; and L.C. De Jonghe; filed April 14, 2004
U.S. Patent 7,282,295; “Protected active metal electrode and battery cell structures with non-aqueous interlayer architecture”; S.J. Visco; Y.S. Nimon; , B D. Katz; and L.C. De Jonghe filed April 14, 2004
12th International Meeting on Lithium Batteries,
Nara, Japan, June 27th – July 2nd, 2004
1ST PUBLIC PRESENTATION OF THE
PROTECTED LITHIUM ELECTRODE (PLE)
“Lithium Metal Aqueous Batteries,” Abstract No. 53,
“Lithium Fuel Cells,” Abstract No. 396
“Lithium Air Batteries,” Abstract No. 397
Lithium/Water Chemistry
(Low equivalent weight of lithium combined with the high voltage for the Li/Seawater couple leads to unprecedented energy density for practical Li/Seawater Cells)
Li/O2 in aqueous electrolytes:
Basic electrolyte: 4Li + O
2+ 2H
2O = 4LiOH
Acidic electrolyte: 4Li + O
2+ 4H+ = 2H
2O + 4Li
Li/O2 in non-aqueous electrolytes:
Li + O
2= Li
2O
2(peroxide)
Li/Water:
Basic electrolyte: 2Li + 2H
2O = 2LiOH + H
2Seawater (pH=8.2): 2Li + 2H
2O = 2LiOH + H
2E = 3.45 V
E = 4.27 V
E = 2.96 V
E = 2.22 V
E ~ 2.60 V
The gravimetric capacity of lithium is 3800 mAh/g; Li/Seawater batteries make use of both the dissolved oxygen (E=3.45 V) and water reduction (E=2.6 V) leading to a nominal voltage of about 2.8 volts for Li/Seawater battery under discharge. According, the theoretical specific energy is 3800 mA/g x 2.8 V ~ 10,000 Wh/kg.
Stability Window for H
2
O
Conventional Technology
(Conventional vs. Solid Electrolyte Protected Li)
Expanded potential window enables development of stable Li/Air & Li/Water cells
ProtectedAnode
Li/Air Aqueous
Solid-state, non-aqueous, ionic liquid, polymer electrolyte
Solid state/Aqueous Interface
Discharge of Protected Lithium Metal Electrodes
Figure. 5. Discharge of thick protected anodes (Li foil is 5.3-5.6 mm) in aqueous neutral electrolyte used in Li/Air batteries. Discharge current density: 1) 2.0 mA/cm2; 2)1.0 mA/cm2; 3) 0.5 mA/cm2. End of cell
discharge corresponds to Li depletion. Data provided by PolyPlus Battery Company.
0.5 mA/cm2
1.0 mA/cm2
2.0 mA/cm2
More than 5 mm lithium discharged in in each test at 100% utilization
Protected Li electrode Li/Air Technology
Flexible seal allows
volume change and
maintains hermetic
enclosure
(Tested to 10,000 psi)
Compliant seal
Commercial air electrode & Aqueous LiOH electrolyte PolyPlus air electrodes & PolyPlus catholytes
Discharge of lithium/air cells having double-sided PLEs with compliant seals in aqueous catholyte at varying current density: 1) 1.0 mA/cm2; 2) 0.5 mA/cm2 ; and 3) 0.2 mA/cm2
Discharge of Aqueous Li/Air using PLE
Li/Air Cell (800 Wh/kg)
Li2O2
insoluble
Non-Aqueous Li/Air
Corrosion of Li electrode by water
is unavoidable with this approach
Corrosion of Li electrode is
eliminated with this approach
PolyPlus issued US Patent
Choice of catholytes is limited
Choice of catholytes nearly unlimited
Li2O2
Cycling of Li/Air Cell with Protected Li Anode and Non-Aqueous
Catholyte
Li electrode thickness: 40 µm Discharge/Charge: 0.1 mA/cm2 for 10 hrs (~5 µm of Li)
Time, hrs
Cell V
oltage, V
22nd cycle
5th cycle
Cycling performance of Li/Air cell with non-aqueous electrolyte. Charge/discharge: 0.4 mA/cm2
for 5 hrs; thickness of Li plated and stripped during cycling is ~10 μm 2 mAh/cm2/cycle
Cycling performance of Li/air cell with nonaqueous catholyte comprising LiTFSI in DMF–EG.
Charge/discharge: 0.4 mAcm2 for 5 h; thickness of Li plated and stripped during cycling: 10 microns
Rechargeable Li/Air using PLE and
non-aqueous catholyte
Rechargeable Li/Air
•
Develop thin or wind-able solid electrolyte
membranes to increase cell surface area
•
Develop electrocatalysts for the non-aqueous
oxygen electrode
•
Explore non-aqueous electrolytes and
complexing agents to increase solubility of
Li
2O
2•
Develop suitable electrode microstructures
for deep reversible cycling of oxygen electrode
•
Demonstrate suitable cycling of lithium
electrode for traction applications
ADVANTAGES OF LITHIUM/AIR
•
Extremely high specific energy (rivaling that possible for
hydrocarbon fuel cells); commercial cells should reach 1000
Wh/kg
•
Energy for reaction is not contained in cell; large battery packs
may have a safety advantage for that reason
•
Environmentally benign system
Li/Air Cell (800 Wh/kg)
Providing Power for Marine Devices
Slide courtesy of Dr. James Bellingham
Monterey Bay Aquarium Research Institute (MBARI)
The majority of the oxygen in the earth’s
atmosphere is produced
from photosynthetic processes occurring in
the ocean. This is approximately sixty to
The Protected Anode
Fully functional protected lithium electrode; lithium electrode is
stable to a broad range of protic and aprotic solvents including
water; 2400 Wh/kg with a 2.8 V cathode.
Discharge of Protected Li Electrode In Seawater at Variety of Rates
Time, days
Anode potential vs. SHE, V
1.0 mA/cm2 0.8 mA/cm2 0.2 mA/cm2 0.1 mA/cm2 ~ 15 months of discharge Li Thickness: 5.1-5.4 mm
End of discharge corresponds to Li depletion
Discharge of Li/Seawater (O
2) Cells
Having Double-Sided Protected Lithium Anodes in 65-L Tank
Cell voltage, V
Time, hrs
End of discharge corresponds to lithium depletion
Glass-ceramic plates 150 µm in thickness
1.0 mA/cm2 0.5 mA/cm2
Discharge at 0.5 mA/cm2: 2268 mAh (1.14 mm Li)
Discharge at 1.0 mA/cm2: 2247 mAh (1.13 mm Li)
3.0 V
Discharge of Double-Sided Ceramic-Protected Lithium Anodes
Having Flexible Seal in Seawater
Anode potential vs. SHE, V
Time, hrs
Sintered ceramic plates 260-270 µm in thickness Lithium thickness: 1.1-1.3 mm (2.2-2.6 mm total)
1.0 mA/cm2 0.5 mA/cm2 0.2 mA/cm2 0.15 mA/cm2
For all cells end of discharge corresponds to lithium depletion
0.1
mA/cm2
105 days of discharge
Protected Li anode
Li = Li+ + e
-Testing Under Realistic Ocean Conditions
Will Biofouling Occur on Protected Anode?
PolyPlus, MBARI, Scripps
Pacific Ocean
10 meters
Li+ Li+ Li+ Li+ Lithium Li+ Toxic Non-ToxicDeep Water Batteries
Best marine batteries deliver 50 to 250 Wh/kg Li/Seawater should exceed 1000 - 1500 Wh/kg
MARKETS
The Protected Anode
Fully functional protected lithium electrode; lithium electrode is stable to a broad range of protic and aprotic solvents including water; 2400 Wh/kg with a 2.8 V cathode.
OHARA
Glass-Ceramic and Tape-Cast Membranes
Glass-ceramic membranes: Ohara Japan Tape-cast membranes: OHARA U.S.
MANUFACTURING
•
PolyPlus is working with Quallion
LLC, a potential manufacturer of Li/
Air and Li/Seawater batteries.
•
Quallion is now developing pack
designs for commercial Li/Air
products.
NEW OPPORTUNITIES
IMPLANTABLE
POWER
SUPPLIES
Should last 2 times longer
than Li/I
2IMPLANTABLE
POWER
SUPPLIES
Should last 2 times longer
than Li/I
2Novel Drug Delivery Systems
Ionotophoretic Li+ Drug Delivery
Li blood conc
.
Time
oral lithium
therapeutic
toxic
Electrochemical drug delivery (iontophoresis)
ultra-compact Li source
+
_
Biological medium
Live pig skin
Protected Li Electrode
Ag/AgCl Electrode
Li
+
Li + AgCl = LiCl + Ag
-Intellectual Property (IP) Assets
Intellectual Property Assets
•
Innovate & Protect IP
‣
72 Issued Patents & 60 Pat. Apps.‣
Domestic and foreign patent coverage‣ Internal IP Circle leads to new innovations
•
Solidify Core IP
‣ Employee Retention = IP Retention
‣ Internal IP Circle strengthens core protection
•
Monetize IP Assets
‣ Leverage IP (JV, Gov’t funding, strategic alliances)
‣ License secondary IP (field of use)
‣ Sell prepackaged secondary IP portfolios
‣ New IP = New Business
E N E R G Y T E C H N O L OG Y Ot her Bio me dic al B a t t e r i e s Li-Seaw ater Li-P olym er S olid Sta te Th in M etal Elec tro lyz ers L i-Pa tch Ne w Li - S OCl 2 Li Sulfu r
Li-Air Li -Air
F ilm F uel C ells Secon dary Primary Poly Plu s A no de Pr ot ec tion P
olyPlus Anode Protectio
n P oly Plu s A nod e Pro tecti on Lithiu m (metal) Li Cx (carb on) Li M x (all oys) L ithi um (me tal) Li Cx (c ar bo n) PolyPlus Protected Anode Technology )0#IRCLE INN OVATEPR OT EC T DEV ELO P
U.S. Patent Application No. U.S. Patent Application Title
20070172739 COMPOSITE SOLID ELECTROLYTE FOR PROTECTION OF ACTIVE METAL ANODES
20070117007 LI/AIR NON-AQUEOUS BATTERIES
20070051620 Polymer adhesive seals for protected anode architectures
20070037058 Compliant seal structures for protected active metal anodes
20060078790 Solid electrolytes based on lithium hafnium phosphate for active metal anode protection
20050175894 Protected active metal electrode and battery cell structures with non-aqueous interlayer architecture
20050100793 Active metal electrolyzer
20050100792 Active metal fuel cells
20040197641 Active metal/aqueous electrochemical cells and systems
20040191617 Ionically conductive membranes for protection of active metal anodes and battery cells
20040142244 Ionically conductive composites for protection of active metal anodes
20040131944 Compositions and methods for protection of active metal anodes and polymer electrolytes
20040126653 Ionically conductive composites for protection of active metal anodes
20030088971 Encapsulated alloy electrodes
20020182508 Coated lithium electrodes
20010041294 Plating metal negative electrodes under protective coatings