CA2095346C - Rechargeable lithiated thin film intercalation electrode battery - Google Patents
Rechargeable lithiated thin film intercalation electrode batteryInfo
- Publication number
- CA2095346C CA2095346C CA002095346A CA2095346A CA2095346C CA 2095346 C CA2095346 C CA 2095346C CA 002095346 A CA002095346 A CA 002095346A CA 2095346 A CA2095346 A CA 2095346A CA 2095346 C CA2095346 C CA 2095346C
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- Prior art keywords
- electrode
- metal oxide
- coating
- substrate
- thin film
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Links
- 238000009830 intercalation Methods 0.000 title claims description 37
- 230000002687 intercalation Effects 0.000 title claims description 36
- 239000010409 thin film Substances 0.000 title abstract description 43
- 239000000758 substrate Substances 0.000 claims abstract description 43
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 28
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 24
- 229910002097 Lithium manganese(III,IV) oxide Inorganic materials 0.000 claims abstract description 4
- 229910003005 LiNiO2 Inorganic materials 0.000 claims abstract 2
- 238000000576 coating method Methods 0.000 claims description 36
- 239000011248 coating agent Substances 0.000 claims description 32
- 150000001875 compounds Chemical class 0.000 claims description 31
- 239000000463 material Substances 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 16
- 229910044991 metal oxide Inorganic materials 0.000 claims description 13
- 150000004706 metal oxides Chemical class 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 229910000314 transition metal oxide Inorganic materials 0.000 claims description 9
- 229910001416 lithium ion Inorganic materials 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 8
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 7
- 239000003792 electrolyte Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 6
- 229910032387 LiCoO2 Inorganic materials 0.000 claims description 5
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000010931 gold Substances 0.000 claims description 4
- 229910052737 gold Inorganic materials 0.000 claims description 4
- 229910002804 graphite Inorganic materials 0.000 claims description 4
- 239000010439 graphite Substances 0.000 claims description 4
- 230000008016 vaporization Effects 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical group [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- DZKDPOPGYFUOGI-UHFFFAOYSA-N tungsten dioxide Inorganic materials O=[W]=O DZKDPOPGYFUOGI-UHFFFAOYSA-N 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 16
- 238000000137 annealing Methods 0.000 abstract description 13
- 230000015572 biosynthetic process Effects 0.000 abstract description 5
- 238000011065 in-situ storage Methods 0.000 abstract description 3
- 239000004065 semiconductor Substances 0.000 abstract description 3
- 229910018187 Li CoO2 Inorganic materials 0.000 abstract 1
- 229910006568 Li—CoO2 Inorganic materials 0.000 abstract 1
- 238000000313 electron-beam-induced deposition Methods 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 19
- 238000012360 testing method Methods 0.000 description 12
- 239000010408 film Substances 0.000 description 9
- 229910014549 LiMn204 Inorganic materials 0.000 description 6
- 239000012071 phase Substances 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 229910001220 stainless steel Inorganic materials 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- 238000000151 deposition Methods 0.000 description 5
- 230000008021 deposition Effects 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 238000005566 electron beam evaporation Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 238000004377 microelectronic Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 229910001218 Gallium arsenide Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- -1 e.g. Substances 0.000 description 3
- 238000010894 electron beam technology Methods 0.000 description 3
- 238000009501 film coating Methods 0.000 description 3
- DHKHKXVYLBGOIT-UHFFFAOYSA-N 1,1-Diethoxyethane Chemical compound CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 229910021450 lithium metal oxide Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 229910052582 BN Inorganic materials 0.000 description 1
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 1
- 229910013462 LiC104 Inorganic materials 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910003092 TiS2 Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 244000309464 bull Species 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
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- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000007888 film coating Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 229910002102 lithium manganese oxide Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000003380 quartz crystal microbalance Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 210000000352 storage cell Anatomy 0.000 description 1
- 238000012029 structural testing Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
- 238000002207 thermal evaporation Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical group [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C14/00—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
- C23C14/06—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the coating material
- C23C14/08—Oxides
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
- H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/49002—Electrical device making
- Y10T29/49108—Electric battery cell making
- Y10T29/49115—Electric battery cell making including coating or impregnating
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Secondary Cells (AREA)
Abstract
A thin film electrode (10) for a rechargeable (secondary) battery is prepared by electron beam deposition of LiMn2O4, Li-CoO2, or LiNiO2 on a smooth, amorphous substrate surface (14) and in situ annealing of the deposited lithium composition at a temperature below about 500 °C. The amorphous nature of the substrate surface prevents epitaxial growth or ordered orientation of the minute composition crystallites thus formed. The finely granular structure of the resulting electrode thin film (16) presents abundant surface area that enables a 4V battery to provide current densities in the range of 500 mic-roamps/cm2. The low annealing temperature enables formation of the electrode structure and subsequent battery assembly directly upon semiconductor devices and integrated circuitry.
Description
W092/~117 PCT/US91/~tl --1-- r ~ .
2o~s3~6 RECHAR6EABLE LIT~IATED THIN FILM
INTERCALATION ELECTRODE BATTERY
BACKGROUND OF THE INVENTION
This invention relates to secondary (rechargeable) lithium batteries which utilize thin film intercalation compounds, principally as the positive electrode. In particular, the invention provides means for fabricating such battery electrodes as thin films of lithiated ternary transition metal oxides, including LiMn2O4, LiCoO2, and 10 LiNio2.
Rapid growth in the use of electronics instrumentation ranging from sophisticated telecommunication equipment and computers to audio-visual systems, watches, and toys has generated a wide-spread requirement for electronic circuits that include devices having their own power sources and energy storage.
Therefore, there is a critical need for low-cost, miniaturized, rechargeable energy storage devices (batteries) that have high energy densities and can deliver power reliably at a constant voltage over many recharge cycles. As an additional requirement for most practical applications, the fabrication of these secondary batteries must be compatible with microelectronics technologies in order that such power sources may be fully integrated into complex microcircuits.
Thin-film, multilayer heterostructure systems including compounds capable of intercalating lithium ions SUBSTITUTE SHEE~
WO92/09117 ; PCT/US91/0~11 ~ ~.
209S3~6 have thus far offered the most promise of meeting the need for miniaturized secondary batteries. For example, Meunier et al., in Mat. Sci. and Eng., 83 (1989) 19-23, describe such layered structures that include TiS2 or TiSxoy positive electrode intercalation compounds with elemental lithium negative electrodes. These materials provide only about 1.25 to 2.6 V at a 1 microamp/cm2 current density, however. A similar lithium anode thin film cell described in U.S. 4,7Sl,159 employs AgMo6S8 as the positive electrode intercalation material and is reportedly capable of providing voltages of about 1.4 to 3 V at a current density of 300 microamps/cm2. Although this intercalation cathode compound shows improving performance capability, thin film battery composites continue to suffer from the disadvantage of depending upon dangerously reactive lithium metal anodes as the Li ion source.
Further improved performance with open circuit voltages in the range of 4 V at energy densities of 200 to 500 microamps/cm2 has been exhibited by secondary battery cells having bulk, pelletized positive intercalation electrodes of three-dimensional, spinel-structured LiMn204 (U.S. 4,828,834), and layered LiCoO2 (Mizushima et al., Mat. Res. Bull., 15, 783 (1980)) and LiNio2 (Dahn et al., Solid State Ionics, 44, 87 (1990)). These materials exhibit the additional benefits of being light weight and providing a source of lithium ions that enables substitution of similar or other intercalatable materials, e.g., graphite, Wo2, and Al, for the environmentally undesirable lithium metal anode.
Unfortunately, however, these lithiated transition metal oxides have properties that until now have detracted from their serious consideration as candidates in thin SUBSTITUTE SHEET
_3_ 4 6 film fabrication processes with widely-used electronic component materials such as GaAs and silicon.
Initially, the great disparity between the melting points and atomic masses of lithium and the transition metal constituent would ordinarily prevent stoichiometric deposition from a bulk intercalation compound source in commonly-employed fabrication processes such as reactive electron beam evaporation.
Further, the high temperatures, often in excess of 800C, at which these intercalation compounds are normally crystallized in bulk are inimical to their incorporation into microcircuits with GaAs decomposing above 350C or Si which deteriorates above about 500C.
Such high temperature processing of these lithiated ternary metal oxides has also been found to produce crystallite grain sizes generally larger than about one micrometer, thereby severely limiting the electrode surface area, and thus the intercalation kinetics, in typical 0.5 to 1.5 micrometer thin films.
In the present invention, we have found the means to avoid these disadvantages and to fabricate lithiated ternary transition metal oxide thin film intercalation electrodes for secondary batteries under conditions that are compatible with microelectronics technology and that produce high electrode surface area and resulting exceptional performance.
SUMMARY OF THE INVENTION
In accordance with one aspect of the invention there is provided a rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an electrolyte, and a counter-electrode ~f i -3a-consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode comprises a 1 to 5 micrometer thick coating of 0.05 to 0.1 micrometer crystallite grains of said metal oxide on a substrate coating surface consisting essentially of an amorphous, substantially chemically inert substance.
In accordance with another aspect of the invention there is provided a method of making a rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an - 15 electrolyte, and a counter-electrode consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode is prepared by a) situating in an air-tight enclosure with a supply of said lithiated metal oxide a substrate having a coating surface consisting essentially of an amorphous, substantially chemically inert substance; b) establishing within said enclosure a low pressure, carbon-free atmosphere; c) vaporizing at least a portion of said metal oxide; d) condensing said metal oxide vapor on said substrate surface in a coating having a thickness in the range of about 1 to 5 micrometers; and e) heating said coating within said atmosphere at a temperature and for a time sufficient to convert said coating to crystallites of said metal oxide having a grain size in the range of about 0.05 to 0.1 micrometer.
A thin film intercalation electrode of fine grain lithiated transition metal oxide is prepared in the present invention by low temperature annealing of a . ~.
~1V0 92/09117- : X ' " 5 PCl/US91/08411 ~09S346 stoichiometrically composed thin film lithiated oxide layer deposited by reactive electron beam evaporation onto a suitable substrate from a bulk source of the oxide compound. In order to obtain a desirable 0.05 to 0.1 micrometer crystallite grain size during annealing, any epitaxial influence there may be at the substrate surface which might promote ordered or preferential crystal growth is suppressed by interposing an amorphous, inert buffer layer between the substrate surface and the deposited film.
A crystalline substrate, for example, is typically coated with a thin film layer of gold in any evaporative or sputtering technique to provide such a buffer layer upon which the lithiated electrode compound condenses during the evaporative coating operation. In the subsequent annealing ~tep, the ternary lithiated composition film, having no contact with any influential substrate surface formation, crystallizes to the desired intercalatable phase in unordered, random fashion and thereby develops crystallites no larger than about 0.1 micrometer.
With less influential substrates, such as quartz, stainless steel, aluminum, and the like, the inert buffer layer is nonetheless useful in masking any physical 2S imperfections that might nucleate larger crystal growth.
The inert property of the buffer is particularly beneficial in preventing chemical reaction between a substrate and the highly reactive lithium component of the electrode composition film, even at annealing temperatures.
The unique physical and chemical properties of lithium which previously have prevented practical thi~
SU BSTITUTE SHEET
~92/09117- -- 2 0 9 5 3 4i6 PCT~USg1~0~11 i~
film coating of desirable intercalation compositions have been accounted for in the present method of electrode preparation. In order to minimize preferential evaporation of the lower melting lithium and to thus prevent disruption of the stoichiometric component balance of the ternary compound during the coating process, the preannealed intercalation composition source is presented in sufficiently small size to ensure that the non-scanning electron beam cone eminating from the coating apparatus ring filament contacts substantially the entire surface of the source material. Disproportionate accumulation of lithium at the substrate target due to lower atomic mass is limited by reducing the space, and thus the flight time, between the composition source and the target.
Finally, reevaporation loss of lithium from the target due to heat generated in the coating process is minimized by supplemental cooling of the substrate until the desired film thickness is deposited.
The lower temperature annealing of the coated ternary composition film that yields fine crystallite formation is made possible by eliminating intermediate exposure of the film to air. A heating element incorporated into the substrate support plate enables the coated film to remain in the evacuated arena throughout the coating and annealing operations. The reactive lithium film component is thereby prevented from otherwise forming the carbonate that requires destructively high annealing temperatures.
After in situ annealing and intercalation compound crystallite formation, the thin film electrode element may be safely removed to ambient atmosphere for completion of conventional storage cell assembly with appropriate electrolyte and anode elements. The thin film lithiated SUB~ 111 UTE SHEEl WO 92/09117~ ~ 3 ' 2 o-g 5-~6 PCT/US91/0~11~
intercalation materials prepared by the present method may be employed also as anodes where it is desired to replaced metallic lithium.
THE DRAWING
The present invention will be described with reference to the accompanying-drawing of which:
FIG. l is a representative elevation view, in cross-section, of a thin film intercalation electrode of the invention;
FIG. 2 is an exploded view of a test cell apparatus employed to test the efficacy of a thin film cathode prepared according to the invention; and FIG. 3 is a graph of test results of a thin film cathode of the invention charting voltage output and recharging characteristics against the-level of lithium in the intercalation composition.
- - - - ~. , - .
. ., ~ . ., DESCRIPTION OF THE INVENTION
- The thin film materials of the present invention are intended primarily for use as positive electrodes in secondary, i.e., rechargable, lithium battery cells with lithium metal or environmentally preferred lithium intercalated negative electrodes, such as Al, WO2, or SlJBsTlT~J~E SHEET
WO92/~117 ~?~ 2 0 9 S 3 4 6 PCT/US9~
_ -7- ~
graphite. The present intercalatable thin films may, of course, also find use as such substitute negative electrodes. In either event, the invention provides means for preparing these electrodes as thin films which, by generally accepted definition, range up to a few micrometers in thickness.
Previously, maintaining a stoichiometric balance of compound ingredients during the fabrication of such thin film electrodes of known lithium intercalation compounds, e.g., LiMn204, LiCoO2, and LiNio2, was considered markedly infeasible due to the contributing effects of chemical reactivity of lithium, the great disparity of its melting point and atomic mass from those properties of the component transition metals, and the high temperatures usually required in processing the compounds. For example, the accepted range of annealing temperatures, commonly in excess of 800C, used in the phase conversion of these lithiated intercalation compounds discouraged their consideration for use in integration of power supplies with microelectronic circuitry typically employing materials decomposing or deteriorating at such temperatures. The vulnerability of other desirable substrates, e.g., aluminum with a melting point of about 700C, and the exaggerated reactivity of lithium with useful substrate materials also detracted - from the appeal of thin film lithiated intercalation - compounds.
.
~ The present invention, however, avoids these apparent drawbacks in allowing fabrication of thin film electrodes using ternary lithiated transition metal oxides and comparatively low temperature substrate materials.
These electrodes not only maintain, but in fact improve upon the functional performance properties of prior bulk ~uB~ TE SHEET
WO92/09117 ~ PCT/US91/0~11~
or pelletized electrode applications of the same lithiated intercalation compounds in secondary batteries. This advance has been achieved primarily in the ability of the present processing to apply the thin film coating with S stoichiometric compound balance and to convert the coated compound to the desired intercalation phase at a lower temperature and in an environment that promote an exceptionally small crystallite, high surface area intercalation medium.
A typical electrode structure lo, such as used in the present examples, is depicted in FIG. 1 and consists essentially of a substrate 12, an inert buffer layer 14, and a thin film layer 16 of lithiated intercalation compound crystallites. The substrate may be selected from a wide range of materials according to intended application. In the development of the present invention, for instance, nickel and stainless steel substrates served effectively while providing structural testing support.
Further, as a means of confirming low temperature applicability of the process, an aluminum substrate later employed in exemplary test cells not only imposed a readily satisfied temperature limitation, but also provided an effective current collector in the test cell assembly. In ultimate use with integrated microelectronic circuitry, substrate 12 could comprise GaAs, Si, or other semiconductor device material. An insulating layer (not shown) of sio2 or the like would, of course, be interposed between the semiconductor device and the cell structure in order to maintain the autonomous function of each device.
Metallic buffer layer 14 could then serve as the electrical contact for the cell electrode. -Gold serves particularly well as the thin filmbuffer layer 14 at about 300 nm thickness, providing both SUB~ ~ JTE SHEET
W~ 92/09117 ~ ~ 2 0 9 5 3 4 6 PCr/US91/0~411 .
_g_ ~
the desired properties of chemical inertness for protection of the substrate and surface amorphism to minimize ordered crystallite growth. Where gold does not exhibit optimal adhesion to a substrate, a thin film titanium ground layer 13 at about 10 nm is useful to ensure effective bonding. Both these layers may be applied with conventional thermal or electron beam evaporation or sputtering techniques in preparation for deposition of the lithiated thin film intercalation layer 16 in the present process.
Coating of prepared substrates to provide test cell electrodes was carried out in a commercial electron beam evaporator (Edwards High Vacuum International, model E06A) that had been refitted with fixtures for implementing the ~rocess of the invention. The approximately 10 mm diameter multiple, carousel-mounted source compound crucibles of the apparatus each accommodated less than about 1 gram of source material and were employed in sequence when deposits of greater than about 1 micrometer thickness was desired. The vertical location of the crucibles was also controllable to enable selective positioning of the source material in the tungsten ring filament electron beam cone. In order to obtain an optimally representative composition of source compound vapors, the active crucible was normally situated during the coating operation on a level at which the beam diameter was substantially the same as that of the source crucible, thus ensuring vaporization over the entire source surface.
The mounting stage for the sample substrate included both a Neslab Coolflow II closed circuit cooling unit and a heater assembly fashioned of a Union Carbide Boralectric boron nitride/graphite resistive heater SUB~ JTE SHEE~
WO92~117 ,~ - i PCT/US91/0~11 ~
20953~G -lO-sandwiched between Hayns-alloy stainless steel plates.
The chilled water cooling system was capable of maintaining the substrate surface at about 140C during the evaporative coating procedure and the Variac powerstat controlled sample heating system enabled the in situ annealing of lithium metal oxide coating up to temperatures in excess of 900C. Having this wide range of temperature control during the entire electrode fabrication process was instrumental in eliminating the need for removing the coated substrate from the low pressure, oxygen background environment during transition between these operations. Thus isolating the thin film from atmospheric contact while in its amorphous coated phase avoids the carbonate contamination that previously dictated destructively high temperature phase conversion annealing and led to excessive crystal growth size of the intercalation composition.
Coating source compositions were initially prepared in the manner usually employed for obtaining the bulk, pelletized lithiated intercalation electrode materials. For example, well-mixed stoichiometric proportions of lithium carbonate and manganese oxide are normally reacted in air at 800C for at least 24 hours to obtain intercalatable LiMn204. LiCoO2 and LiNio2 source
2o~s3~6 RECHAR6EABLE LIT~IATED THIN FILM
INTERCALATION ELECTRODE BATTERY
BACKGROUND OF THE INVENTION
This invention relates to secondary (rechargeable) lithium batteries which utilize thin film intercalation compounds, principally as the positive electrode. In particular, the invention provides means for fabricating such battery electrodes as thin films of lithiated ternary transition metal oxides, including LiMn2O4, LiCoO2, and 10 LiNio2.
Rapid growth in the use of electronics instrumentation ranging from sophisticated telecommunication equipment and computers to audio-visual systems, watches, and toys has generated a wide-spread requirement for electronic circuits that include devices having their own power sources and energy storage.
Therefore, there is a critical need for low-cost, miniaturized, rechargeable energy storage devices (batteries) that have high energy densities and can deliver power reliably at a constant voltage over many recharge cycles. As an additional requirement for most practical applications, the fabrication of these secondary batteries must be compatible with microelectronics technologies in order that such power sources may be fully integrated into complex microcircuits.
Thin-film, multilayer heterostructure systems including compounds capable of intercalating lithium ions SUBSTITUTE SHEE~
WO92/09117 ; PCT/US91/0~11 ~ ~.
209S3~6 have thus far offered the most promise of meeting the need for miniaturized secondary batteries. For example, Meunier et al., in Mat. Sci. and Eng., 83 (1989) 19-23, describe such layered structures that include TiS2 or TiSxoy positive electrode intercalation compounds with elemental lithium negative electrodes. These materials provide only about 1.25 to 2.6 V at a 1 microamp/cm2 current density, however. A similar lithium anode thin film cell described in U.S. 4,7Sl,159 employs AgMo6S8 as the positive electrode intercalation material and is reportedly capable of providing voltages of about 1.4 to 3 V at a current density of 300 microamps/cm2. Although this intercalation cathode compound shows improving performance capability, thin film battery composites continue to suffer from the disadvantage of depending upon dangerously reactive lithium metal anodes as the Li ion source.
Further improved performance with open circuit voltages in the range of 4 V at energy densities of 200 to 500 microamps/cm2 has been exhibited by secondary battery cells having bulk, pelletized positive intercalation electrodes of three-dimensional, spinel-structured LiMn204 (U.S. 4,828,834), and layered LiCoO2 (Mizushima et al., Mat. Res. Bull., 15, 783 (1980)) and LiNio2 (Dahn et al., Solid State Ionics, 44, 87 (1990)). These materials exhibit the additional benefits of being light weight and providing a source of lithium ions that enables substitution of similar or other intercalatable materials, e.g., graphite, Wo2, and Al, for the environmentally undesirable lithium metal anode.
Unfortunately, however, these lithiated transition metal oxides have properties that until now have detracted from their serious consideration as candidates in thin SUBSTITUTE SHEET
_3_ 4 6 film fabrication processes with widely-used electronic component materials such as GaAs and silicon.
Initially, the great disparity between the melting points and atomic masses of lithium and the transition metal constituent would ordinarily prevent stoichiometric deposition from a bulk intercalation compound source in commonly-employed fabrication processes such as reactive electron beam evaporation.
Further, the high temperatures, often in excess of 800C, at which these intercalation compounds are normally crystallized in bulk are inimical to their incorporation into microcircuits with GaAs decomposing above 350C or Si which deteriorates above about 500C.
Such high temperature processing of these lithiated ternary metal oxides has also been found to produce crystallite grain sizes generally larger than about one micrometer, thereby severely limiting the electrode surface area, and thus the intercalation kinetics, in typical 0.5 to 1.5 micrometer thin films.
In the present invention, we have found the means to avoid these disadvantages and to fabricate lithiated ternary transition metal oxide thin film intercalation electrodes for secondary batteries under conditions that are compatible with microelectronics technology and that produce high electrode surface area and resulting exceptional performance.
SUMMARY OF THE INVENTION
In accordance with one aspect of the invention there is provided a rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an electrolyte, and a counter-electrode ~f i -3a-consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode comprises a 1 to 5 micrometer thick coating of 0.05 to 0.1 micrometer crystallite grains of said metal oxide on a substrate coating surface consisting essentially of an amorphous, substantially chemically inert substance.
In accordance with another aspect of the invention there is provided a method of making a rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an - 15 electrolyte, and a counter-electrode consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode is prepared by a) situating in an air-tight enclosure with a supply of said lithiated metal oxide a substrate having a coating surface consisting essentially of an amorphous, substantially chemically inert substance; b) establishing within said enclosure a low pressure, carbon-free atmosphere; c) vaporizing at least a portion of said metal oxide; d) condensing said metal oxide vapor on said substrate surface in a coating having a thickness in the range of about 1 to 5 micrometers; and e) heating said coating within said atmosphere at a temperature and for a time sufficient to convert said coating to crystallites of said metal oxide having a grain size in the range of about 0.05 to 0.1 micrometer.
A thin film intercalation electrode of fine grain lithiated transition metal oxide is prepared in the present invention by low temperature annealing of a . ~.
~1V0 92/09117- : X ' " 5 PCl/US91/08411 ~09S346 stoichiometrically composed thin film lithiated oxide layer deposited by reactive electron beam evaporation onto a suitable substrate from a bulk source of the oxide compound. In order to obtain a desirable 0.05 to 0.1 micrometer crystallite grain size during annealing, any epitaxial influence there may be at the substrate surface which might promote ordered or preferential crystal growth is suppressed by interposing an amorphous, inert buffer layer between the substrate surface and the deposited film.
A crystalline substrate, for example, is typically coated with a thin film layer of gold in any evaporative or sputtering technique to provide such a buffer layer upon which the lithiated electrode compound condenses during the evaporative coating operation. In the subsequent annealing ~tep, the ternary lithiated composition film, having no contact with any influential substrate surface formation, crystallizes to the desired intercalatable phase in unordered, random fashion and thereby develops crystallites no larger than about 0.1 micrometer.
With less influential substrates, such as quartz, stainless steel, aluminum, and the like, the inert buffer layer is nonetheless useful in masking any physical 2S imperfections that might nucleate larger crystal growth.
The inert property of the buffer is particularly beneficial in preventing chemical reaction between a substrate and the highly reactive lithium component of the electrode composition film, even at annealing temperatures.
The unique physical and chemical properties of lithium which previously have prevented practical thi~
SU BSTITUTE SHEET
~92/09117- -- 2 0 9 5 3 4i6 PCT~USg1~0~11 i~
film coating of desirable intercalation compositions have been accounted for in the present method of electrode preparation. In order to minimize preferential evaporation of the lower melting lithium and to thus prevent disruption of the stoichiometric component balance of the ternary compound during the coating process, the preannealed intercalation composition source is presented in sufficiently small size to ensure that the non-scanning electron beam cone eminating from the coating apparatus ring filament contacts substantially the entire surface of the source material. Disproportionate accumulation of lithium at the substrate target due to lower atomic mass is limited by reducing the space, and thus the flight time, between the composition source and the target.
Finally, reevaporation loss of lithium from the target due to heat generated in the coating process is minimized by supplemental cooling of the substrate until the desired film thickness is deposited.
The lower temperature annealing of the coated ternary composition film that yields fine crystallite formation is made possible by eliminating intermediate exposure of the film to air. A heating element incorporated into the substrate support plate enables the coated film to remain in the evacuated arena throughout the coating and annealing operations. The reactive lithium film component is thereby prevented from otherwise forming the carbonate that requires destructively high annealing temperatures.
After in situ annealing and intercalation compound crystallite formation, the thin film electrode element may be safely removed to ambient atmosphere for completion of conventional storage cell assembly with appropriate electrolyte and anode elements. The thin film lithiated SUB~ 111 UTE SHEEl WO 92/09117~ ~ 3 ' 2 o-g 5-~6 PCT/US91/0~11~
intercalation materials prepared by the present method may be employed also as anodes where it is desired to replaced metallic lithium.
THE DRAWING
The present invention will be described with reference to the accompanying-drawing of which:
FIG. l is a representative elevation view, in cross-section, of a thin film intercalation electrode of the invention;
FIG. 2 is an exploded view of a test cell apparatus employed to test the efficacy of a thin film cathode prepared according to the invention; and FIG. 3 is a graph of test results of a thin film cathode of the invention charting voltage output and recharging characteristics against the-level of lithium in the intercalation composition.
- - - - ~. , - .
. ., ~ . ., DESCRIPTION OF THE INVENTION
- The thin film materials of the present invention are intended primarily for use as positive electrodes in secondary, i.e., rechargable, lithium battery cells with lithium metal or environmentally preferred lithium intercalated negative electrodes, such as Al, WO2, or SlJBsTlT~J~E SHEET
WO92/~117 ~?~ 2 0 9 S 3 4 6 PCT/US9~
_ -7- ~
graphite. The present intercalatable thin films may, of course, also find use as such substitute negative electrodes. In either event, the invention provides means for preparing these electrodes as thin films which, by generally accepted definition, range up to a few micrometers in thickness.
Previously, maintaining a stoichiometric balance of compound ingredients during the fabrication of such thin film electrodes of known lithium intercalation compounds, e.g., LiMn204, LiCoO2, and LiNio2, was considered markedly infeasible due to the contributing effects of chemical reactivity of lithium, the great disparity of its melting point and atomic mass from those properties of the component transition metals, and the high temperatures usually required in processing the compounds. For example, the accepted range of annealing temperatures, commonly in excess of 800C, used in the phase conversion of these lithiated intercalation compounds discouraged their consideration for use in integration of power supplies with microelectronic circuitry typically employing materials decomposing or deteriorating at such temperatures. The vulnerability of other desirable substrates, e.g., aluminum with a melting point of about 700C, and the exaggerated reactivity of lithium with useful substrate materials also detracted - from the appeal of thin film lithiated intercalation - compounds.
.
~ The present invention, however, avoids these apparent drawbacks in allowing fabrication of thin film electrodes using ternary lithiated transition metal oxides and comparatively low temperature substrate materials.
These electrodes not only maintain, but in fact improve upon the functional performance properties of prior bulk ~uB~ TE SHEET
WO92/09117 ~ PCT/US91/0~11~
or pelletized electrode applications of the same lithiated intercalation compounds in secondary batteries. This advance has been achieved primarily in the ability of the present processing to apply the thin film coating with S stoichiometric compound balance and to convert the coated compound to the desired intercalation phase at a lower temperature and in an environment that promote an exceptionally small crystallite, high surface area intercalation medium.
A typical electrode structure lo, such as used in the present examples, is depicted in FIG. 1 and consists essentially of a substrate 12, an inert buffer layer 14, and a thin film layer 16 of lithiated intercalation compound crystallites. The substrate may be selected from a wide range of materials according to intended application. In the development of the present invention, for instance, nickel and stainless steel substrates served effectively while providing structural testing support.
Further, as a means of confirming low temperature applicability of the process, an aluminum substrate later employed in exemplary test cells not only imposed a readily satisfied temperature limitation, but also provided an effective current collector in the test cell assembly. In ultimate use with integrated microelectronic circuitry, substrate 12 could comprise GaAs, Si, or other semiconductor device material. An insulating layer (not shown) of sio2 or the like would, of course, be interposed between the semiconductor device and the cell structure in order to maintain the autonomous function of each device.
Metallic buffer layer 14 could then serve as the electrical contact for the cell electrode. -Gold serves particularly well as the thin filmbuffer layer 14 at about 300 nm thickness, providing both SUB~ ~ JTE SHEET
W~ 92/09117 ~ ~ 2 0 9 5 3 4 6 PCr/US91/0~411 .
_g_ ~
the desired properties of chemical inertness for protection of the substrate and surface amorphism to minimize ordered crystallite growth. Where gold does not exhibit optimal adhesion to a substrate, a thin film titanium ground layer 13 at about 10 nm is useful to ensure effective bonding. Both these layers may be applied with conventional thermal or electron beam evaporation or sputtering techniques in preparation for deposition of the lithiated thin film intercalation layer 16 in the present process.
Coating of prepared substrates to provide test cell electrodes was carried out in a commercial electron beam evaporator (Edwards High Vacuum International, model E06A) that had been refitted with fixtures for implementing the ~rocess of the invention. The approximately 10 mm diameter multiple, carousel-mounted source compound crucibles of the apparatus each accommodated less than about 1 gram of source material and were employed in sequence when deposits of greater than about 1 micrometer thickness was desired. The vertical location of the crucibles was also controllable to enable selective positioning of the source material in the tungsten ring filament electron beam cone. In order to obtain an optimally representative composition of source compound vapors, the active crucible was normally situated during the coating operation on a level at which the beam diameter was substantially the same as that of the source crucible, thus ensuring vaporization over the entire source surface.
The mounting stage for the sample substrate included both a Neslab Coolflow II closed circuit cooling unit and a heater assembly fashioned of a Union Carbide Boralectric boron nitride/graphite resistive heater SUB~ JTE SHEE~
WO92~117 ,~ - i PCT/US91/0~11 ~
20953~G -lO-sandwiched between Hayns-alloy stainless steel plates.
The chilled water cooling system was capable of maintaining the substrate surface at about 140C during the evaporative coating procedure and the Variac powerstat controlled sample heating system enabled the in situ annealing of lithium metal oxide coating up to temperatures in excess of 900C. Having this wide range of temperature control during the entire electrode fabrication process was instrumental in eliminating the need for removing the coated substrate from the low pressure, oxygen background environment during transition between these operations. Thus isolating the thin film from atmospheric contact while in its amorphous coated phase avoids the carbonate contamination that previously dictated destructively high temperature phase conversion annealing and led to excessive crystal growth size of the intercalation composition.
Coating source compositions were initially prepared in the manner usually employed for obtaining the bulk, pelletized lithiated intercalation electrode materials. For example, well-mixed stoichiometric proportions of lithium carbonate and manganese oxide are normally reacted in air at 800C for at least 24 hours to obtain intercalatable LiMn204. LiCoO2 and LiNio2 source
2~ materials are similarly prepared in known, and even more stringent, process conditions. Scanning electron microscope measurement of these bulk materials indicate a crystal grain size range, e.g., about 1 to 3 micrometers for LiMn204, that is adequate for pellet cathode "button"
batteries, but is grossly excessive for use in thin film electrode fabrication. Since these compounds are physically reconstituted from the vapor phase during the present coating process, however, the bulk-prepared source compound loaded into a coating apparatus crucible provides ~UBSTITUTE SHEET
WO92/~117~ 20 9~C PCT/~S91/0~11 '~'`J
an effective source.
In the fabrication of an exemplary LiMn204 thin film test cell electrode, a 0.5 mm thick prepared aluminum substrate of about lO mm diameter was affixed to the coating apparatus support stage above the ring filament.
The source compound crucibles were arranged on the carousel with one directly below the mounted substrate at a distance of about 225 mm. This separation between the source and substrate was considerably less than commonly employed in the commercial coating apparatus and was selected to minimize the vapor "flight time" to the deposition surface and thereby compensate for the significant difference between the atomic masses of lithium and manganese. Without such compensation, the more rapid movement of the lighter lithium could significantly disrupt the stoichiometric balance of the deposited thin film.
The coating operation generally followed common electron beam evaporation procedures with evacuation of the sealed apparatus at the outset to a base pressure of about 3 to 5xlO 7 torr. A pure oxygen background gas was -then added to obtain a stable initial operating pressure of about 3xlO 5 torr which, due to coating material vaporization, would ultimately increase further to about 3xlO 4 torr. The ring filament was then energized at-5.5 KV and about lO0 mA to initiate evaporation of the source compound with resulting deposition of the lithiated metal oxide on the substrate. The substrate temperature thereafter increased gradually from the combined affects of the heat radiating from the source and the heat of condensation of the deposited composition. This temperature was allowed to increase to about 140C at which it was maintained throughout the remainder of the SUB~ 111 LITE SHEE~
W~92/~117~ u~ 3~ ` , PCT/US91/0~11~~rJ
coating operation by controlling the flow of coolant to the substrate support stage.
Deposition of lithiated compound was monitored by means of the integral quartz crystal microbalance thickness gauge of the coating apparatus and was maintained at a uniform rate of about 0.5 to l nm/sec by responsive control of power to the filament. Upon completion of the desired thin film coating of about l micrometer, filament power was discontinued. For thin film electrode coatings of up to about 5 micrometers, the nearly depleted source compound crucible was replaced as required during the coating operation with other carousel-mounted crucibles.
At the completion of the coating operation, cooling was discontinued and the oxygen background atmosphere was increased to a range of about lO to lO0 torr. The substrate support stage heating element was then energized to raise the substrate and thin film lithium metal oxide coating to about 400C where it was maintained for about 2 hours to effect the desired intercalatable crystalline phase. After natural cooling to ambient temperature, the completed electrode element coating was analyzed by RBS, NMR, and X-ray diffraction techniques and was determined to consist essentially of LixMn204 with x nearly l and the Li/Mn ratio smaller-than the crystal grains of bulk LixMn204 intercalation compound annealed at 800 C. ~ -The intercalation kinetics of the sample electrodethus prepared were tested in a conventional Swagelock test cell generally depicted in FIG.-2. This device comprises a body fitting 23 in which are assembled insulating polypropylene inserts 24 and the active cell elements S~I~UT ~HE-~
WO92/09117 ~ 2 0 9 S 3 4 6; . ~ ~ - PCT/US91/0~11.~
consisting of the sample cathode of substrate 12 and electrode thin film 16, an anode 21 of lithium-plated stainless steel, and an intermediate electrolyte separator 22 of glass cloth saturated with a 1 molar solution of LiC104 in equal parts of ethylene carbonate and diethoxyethane. A stainless steel backing plate 25 and compression spring 26 are added and the assembly is completed with stainless steel plungers 27 mounted in and electrically insulated from end caps 28. When caps 28 are threaded upon body 23, the electrolyte and electrode elements are brought into firm active contact to form the test cell.
A sample electrode having a 1.5 micrometer thin film layer of about 350 micrograms of LiMn204 was tested over series of charge/discharge cycles at varying current densities. FIG. 3 shows a representative performance of the test cell over the first 14 cycles at a current density of 10 microamps/cm2. The efficacy of the cell is apparent in the exceptionally small voltage difference in the charge and discharge cycling between about 3.5 and 4.4 V which demonstrates the limited polarization of the charges and the ability of the cell to maintain high charge and discharge current densities. Performance at other current densities was likewise superior to prior art thin film electrode cells. For example, even at S5C and a current density of 200 microamps/cm2 the sample positive electrode was able to maintain about 70% of the first discharge capacity after more than 200 charge/discharge cycles. Room temperature discharge of the test cell within about 7 minutes at a current density of 500 microamps/cm2 showed polarization of only about 0.1 volt and a capacity decrease of less than about 10% from that exhibited at 100 microamps/cm2.
SUBsTlTuTE~ SHEET
WO92/09tl7 ~ PCT/US91/0~11 2~`9 53~6 -14-The admirable performance of the lithiated thin film electrode batteries of the present invention is due in large measure to its capability of maintaining a stoichiometric balance of the coated thin film composition throughout the fabrication process and of enabling a low temperature, unordered formation of fine, high surface area crystallite layers that enhance lithium ion intercalation. These advantageous properties have heretofore not been achieved in other attempted li-thiated thin film batteries, nor has the performance of the present test cells been approached with prior thin film batteries of other intercalation compositions. In addition to the suggested variations in electrode composition and processing, it is anticipated that other embodiments of l~ the present invention will undoubtedly occur to the skilled artisan in the light of the foregoing description.
Such embodiments are likewise intended to be encompassed within the scope of the invention as recited in the following claims.
SUB~ 111 UTE SHEET
batteries, but is grossly excessive for use in thin film electrode fabrication. Since these compounds are physically reconstituted from the vapor phase during the present coating process, however, the bulk-prepared source compound loaded into a coating apparatus crucible provides ~UBSTITUTE SHEET
WO92/~117~ 20 9~C PCT/~S91/0~11 '~'`J
an effective source.
In the fabrication of an exemplary LiMn204 thin film test cell electrode, a 0.5 mm thick prepared aluminum substrate of about lO mm diameter was affixed to the coating apparatus support stage above the ring filament.
The source compound crucibles were arranged on the carousel with one directly below the mounted substrate at a distance of about 225 mm. This separation between the source and substrate was considerably less than commonly employed in the commercial coating apparatus and was selected to minimize the vapor "flight time" to the deposition surface and thereby compensate for the significant difference between the atomic masses of lithium and manganese. Without such compensation, the more rapid movement of the lighter lithium could significantly disrupt the stoichiometric balance of the deposited thin film.
The coating operation generally followed common electron beam evaporation procedures with evacuation of the sealed apparatus at the outset to a base pressure of about 3 to 5xlO 7 torr. A pure oxygen background gas was -then added to obtain a stable initial operating pressure of about 3xlO 5 torr which, due to coating material vaporization, would ultimately increase further to about 3xlO 4 torr. The ring filament was then energized at-5.5 KV and about lO0 mA to initiate evaporation of the source compound with resulting deposition of the lithiated metal oxide on the substrate. The substrate temperature thereafter increased gradually from the combined affects of the heat radiating from the source and the heat of condensation of the deposited composition. This temperature was allowed to increase to about 140C at which it was maintained throughout the remainder of the SUB~ 111 LITE SHEE~
W~92/~117~ u~ 3~ ` , PCT/US91/0~11~~rJ
coating operation by controlling the flow of coolant to the substrate support stage.
Deposition of lithiated compound was monitored by means of the integral quartz crystal microbalance thickness gauge of the coating apparatus and was maintained at a uniform rate of about 0.5 to l nm/sec by responsive control of power to the filament. Upon completion of the desired thin film coating of about l micrometer, filament power was discontinued. For thin film electrode coatings of up to about 5 micrometers, the nearly depleted source compound crucible was replaced as required during the coating operation with other carousel-mounted crucibles.
At the completion of the coating operation, cooling was discontinued and the oxygen background atmosphere was increased to a range of about lO to lO0 torr. The substrate support stage heating element was then energized to raise the substrate and thin film lithium metal oxide coating to about 400C where it was maintained for about 2 hours to effect the desired intercalatable crystalline phase. After natural cooling to ambient temperature, the completed electrode element coating was analyzed by RBS, NMR, and X-ray diffraction techniques and was determined to consist essentially of LixMn204 with x nearly l and the Li/Mn ratio smaller-than the crystal grains of bulk LixMn204 intercalation compound annealed at 800 C. ~ -The intercalation kinetics of the sample electrodethus prepared were tested in a conventional Swagelock test cell generally depicted in FIG.-2. This device comprises a body fitting 23 in which are assembled insulating polypropylene inserts 24 and the active cell elements S~I~UT ~HE-~
WO92/09117 ~ 2 0 9 S 3 4 6; . ~ ~ - PCT/US91/0~11.~
consisting of the sample cathode of substrate 12 and electrode thin film 16, an anode 21 of lithium-plated stainless steel, and an intermediate electrolyte separator 22 of glass cloth saturated with a 1 molar solution of LiC104 in equal parts of ethylene carbonate and diethoxyethane. A stainless steel backing plate 25 and compression spring 26 are added and the assembly is completed with stainless steel plungers 27 mounted in and electrically insulated from end caps 28. When caps 28 are threaded upon body 23, the electrolyte and electrode elements are brought into firm active contact to form the test cell.
A sample electrode having a 1.5 micrometer thin film layer of about 350 micrograms of LiMn204 was tested over series of charge/discharge cycles at varying current densities. FIG. 3 shows a representative performance of the test cell over the first 14 cycles at a current density of 10 microamps/cm2. The efficacy of the cell is apparent in the exceptionally small voltage difference in the charge and discharge cycling between about 3.5 and 4.4 V which demonstrates the limited polarization of the charges and the ability of the cell to maintain high charge and discharge current densities. Performance at other current densities was likewise superior to prior art thin film electrode cells. For example, even at S5C and a current density of 200 microamps/cm2 the sample positive electrode was able to maintain about 70% of the first discharge capacity after more than 200 charge/discharge cycles. Room temperature discharge of the test cell within about 7 minutes at a current density of 500 microamps/cm2 showed polarization of only about 0.1 volt and a capacity decrease of less than about 10% from that exhibited at 100 microamps/cm2.
SUBsTlTuTE~ SHEET
WO92/09tl7 ~ PCT/US91/0~11 2~`9 53~6 -14-The admirable performance of the lithiated thin film electrode batteries of the present invention is due in large measure to its capability of maintaining a stoichiometric balance of the coated thin film composition throughout the fabrication process and of enabling a low temperature, unordered formation of fine, high surface area crystallite layers that enhance lithium ion intercalation. These advantageous properties have heretofore not been achieved in other attempted li-thiated thin film batteries, nor has the performance of the present test cells been approached with prior thin film batteries of other intercalation compositions. In addition to the suggested variations in electrode composition and processing, it is anticipated that other embodiments of l~ the present invention will undoubtedly occur to the skilled artisan in the light of the foregoing description.
Such embodiments are likewise intended to be encompassed within the scope of the invention as recited in the following claims.
SUB~ 111 UTE SHEET
Claims (7)
1. A rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an electrolyte, and a counter-electrode consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode comprises a 1 to 5 micrometer thick coating of 0.05 to 0.1 micrometer crystallite grains of said metal oxide on a substrate coating surface consisting essentially of an amorphous, substantially chemically inert substance.
2. A battery according to claim 1 c h a r a c t e r i z e d i n t h a t said counter-electrode is selected from the class consisting of LiMn2O4, LiCoO2, and LiNiO2.
3. A battery according to claim 1 c h a r a c t e r i z e d i n t h a t said first electrode comprises a material selected from the class consisting of Li, Al, WO2, and graphite.
4. A battery according to claim 1 c h a r a c t e r i z e d i n t h a t said substrate coating surface substance is gold.
5. A method of making a rechargeable lithium battery comprising a first electrode providing a source of lithium ions, an electrolyte, and a counter-electrode consisting of a ternary lithiated transition metal oxide intercalation compound c h a r a c t e r i z e d i n t h a t said counter-electrode is prepared by a) situating in an air-tight enclosure with a supply of said lithiated metal oxide a substrate having a coating surface consisting essentially of an amorphous, substantially chemically inert substance;
b) establishing within said enclosure a low pressure, carbon-free atmosphere;
c) vaporizing at least a portion of said metal oxide;
d) condensing said metal oxide vapor on said substrate surface in a coating having a thickness in the range of about 1 to 5 micrometers; and e) heating said coating within said atmosphere at a temperature and for a time sufficient to convert said coating to crystallites of said metal oxide having a grain size in the range of about 0.05 to 0.1 micrometer.
b) establishing within said enclosure a low pressure, carbon-free atmosphere;
c) vaporizing at least a portion of said metal oxide;
d) condensing said metal oxide vapor on said substrate surface in a coating having a thickness in the range of about 1 to 5 micrometers; and e) heating said coating within said atmosphere at a temperature and for a time sufficient to convert said coating to crystallites of said metal oxide having a grain size in the range of about 0.05 to 0.1 micrometer.
6. A method according to claim 5 c h a r a c t e r i z e d i n t h a t said substrate is maintained at a temperature below about 140°C during said vapor condensing step.
7. A method according to claim 5 c h a r a c t e r i z e d i n t h a t said lithiated metal oxide is LiMn2O4 and said heating is effected at about 400°C in an atmosphere consisting essentially of oxygen at a pressure in the range of about 10 to 100 torr.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US61208690A | 1990-11-09 | 1990-11-09 | |
| US612,086 | 1990-11-09 | ||
| US733,224 | 1991-07-22 | ||
| US07/733,224 US5110696A (en) | 1990-11-09 | 1991-07-22 | Rechargeable lithiated thin film intercalation electrode battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2095346A1 CA2095346A1 (en) | 1992-05-10 |
| CA2095346C true CA2095346C (en) | 1995-02-14 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002095346A Expired - Fee Related CA2095346C (en) | 1990-11-09 | 1991-11-08 | Rechargeable lithiated thin film intercalation electrode battery |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US5110696A (en) |
| JP (1) | JPH06510621A (en) |
| AU (1) | AU9070891A (en) |
| CA (1) | CA2095346C (en) |
| WO (1) | WO1992009117A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US4340652A (en) * | 1980-07-30 | 1982-07-20 | The United States Of America As Represented By The United States Department Of Energy | Ternary compound electrode for lithium cells |
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-
1991
- 1991-07-22 US US07/733,224 patent/US5110696A/en not_active Expired - Fee Related
- 1991-11-08 CA CA002095346A patent/CA2095346C/en not_active Expired - Fee Related
- 1991-11-08 AU AU90708/91A patent/AU9070891A/en not_active Abandoned
- 1991-11-08 JP JP4501919A patent/JPH06510621A/en active Pending
- 1991-11-08 WO PCT/US1991/008411 patent/WO1992009117A1/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| US5110696A (en) | 1992-05-05 |
| AU9070891A (en) | 1992-06-11 |
| WO1992009117A1 (en) | 1992-05-29 |
| JPH06510621A (en) | 1994-11-24 |
| CA2095346A1 (en) | 1992-05-10 |
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