CA1042503A - Method of preparing a lithium-aluminum electrode using heat and pressure - Google Patents
Method of preparing a lithium-aluminum electrode using heat and pressureInfo
- Publication number
- CA1042503A CA1042503A CA248,830A CA248830A CA1042503A CA 1042503 A CA1042503 A CA 1042503A CA 248830 A CA248830 A CA 248830A CA 1042503 A CA1042503 A CA 1042503A
- Authority
- CA
- Canada
- Prior art keywords
- lithium
- aluminum
- sandwich
- sheets
- sheet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- JFBZPFYRPYOZCQ-UHFFFAOYSA-N [Li].[Al] Chemical compound [Li].[Al] JFBZPFYRPYOZCQ-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims description 33
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 71
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 70
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 47
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000002844 melting Methods 0.000 claims abstract description 10
- 230000008018 melting Effects 0.000 claims abstract description 10
- 229910000838 Al alloy Inorganic materials 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims description 11
- 230000002093 peripheral effect Effects 0.000 claims description 8
- 238000002791 soaking Methods 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 2
- 235000011890 sandwich Nutrition 0.000 abstract description 51
- 229960001078 lithium Drugs 0.000 description 59
- 235000010210 aluminium Nutrition 0.000 description 36
- 229910045601 alloy Inorganic materials 0.000 description 17
- 239000000956 alloy Substances 0.000 description 17
- 230000015572 biosynthetic process Effects 0.000 description 6
- 239000003792 electrolyte Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000012300 argon atmosphere Substances 0.000 description 4
- 239000012298 atmosphere Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- FPBFIOYAKGHRLY-UHFFFAOYSA-N alumane;lithium Chemical compound [Li].[AlH3].[AlH3] FPBFIOYAKGHRLY-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001989 lithium alloy Substances 0.000 description 2
- -1 lithium halide salt Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010310 metallurgical process Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 229910001148 Al-Li alloy Inorganic materials 0.000 description 1
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 description 1
- 101100130497 Drosophila melanogaster Mical gene Proteins 0.000 description 1
- 241001364889 Helius Species 0.000 description 1
- 229910000733 Li alloy Inorganic materials 0.000 description 1
- 101100345589 Mus musculus Mical1 gene Proteins 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound 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
-
- 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
- H01M4/362—Composites
- H01M4/366—Composites as layered products
-
- 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
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/46—Alloys based on magnesium or aluminium
-
- 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
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/027—Negative electrodes
-
- 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
- H01M4/04—Processes of manufacture in general
- H01M4/049—Manufacturing of an active layer by chemical means
- H01M4/0495—Chemical alloying
-
- 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
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/40—Alloys based on alkali metals
- H01M4/405—Alloys based on lithium
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
A lithium-aluminum negative electrode for an electrochemical cell is prepared by forming a sandwich comprised of lithium and aluminum such that lithium is disposed between the aluminum layers of the sandwich. The sand-wich is heat soaked at a temperature below the melting point of lithium while pressure is applied to the sandwich thereby causing the lithium and aluminum to chemically react to form a lithium-aluminum alloy.
A lithium-aluminum negative electrode for an electrochemical cell is prepared by forming a sandwich comprised of lithium and aluminum such that lithium is disposed between the aluminum layers of the sandwich. The sand-wich is heat soaked at a temperature below the melting point of lithium while pressure is applied to the sandwich thereby causing the lithium and aluminum to chemically react to form a lithium-aluminum alloy.
Description
~04'~503 This invention relates to methods for preparing negative electrodes or anodes for use in electrical energy storage devices or batteries. More particularly, it relates to methods for preparing lithium-aluminum negative electrodes for use in such devices or batteries.
It may be explained here that high power delivery and rapid charge, and discharge above the range of a conventional lead-acid storage battery can be obtained from a high temperature electrical energy storage battery or cell comprising a pair of electrodes, at least one of which is a negat;ve electrode rnGrs~d in ~ comprised of lithium and aluminum~the electrode being ~ d or in contact with a fused alkali halide electrolyte. The fast charging characteristics of ~ such a cell are mainly attributable to the highly reversible lithium-aluminum ', negative electrode of the cell. The positive electrode of such a cell can be '~ carbon or any other suitable material.
The prior art methods for producing the lithium-aluminum negative electrode have been primarily either electrochemical or metallurgical.
In the electrochemical method, lithium-aluminum electrodes were produced by electrochemically charging a substantially pure aluminum electrode in an electrolyte containing lithium halide salt or salts. This electrochemi-;~ cal method was essentially effected by immersing a positive electrode, such as ;~
carbon, and a negative electrode, the aluminum electrode, into a molten lith-ium containing electrolyte and impressing an appropriate voltage across the two electrodes. Lithium in the electrolyte would diffuse into the aluminum electrode structure to form the desired lithium-aluminum electrode. - ~-~; In the metallurgical method, lithium-aluminum electrodes were pro-duced by melting a mixture containing a predetermined amount of each metal to form an alloy of lithium-aluminum. ~ ;
.1 One of the difficulties associated with the above described elec-~i troch~mical method of preparing lithium-aluminum electrodes is that after they have been elect~olytically for~ed, it is necessary to precondition the ~1li 3o electrodes by initially operating them through a number of time consuming ~i . j , :
:, . , , , . . ~ , .
~04'~503 cycles of slow charge and discharge. If the initial cycles are carried out too quickly, regions of liquid metal alloy can be produced resulting in pit-ting of the electrode. Another difficulty presented in the use of electro-chemically prepared lithium-aluminum electrodes is their lack of dimensional stability due to the fact that during the forming and preconditioning steps, they have been found to sometimes expand.
The preparation of lithium-aluminum electrodes by metallurgical techniques has also presented problems in that it has been difficult in the past to obtain lithium-aluminum alloys with compositions much in excess of 5 weight percent lithium with acceptable purity levels and lack of fragility.
Due to this less than desirable percentage of lithium, it was necessary to place the 5 weight percent lithium-aluminum electrodes in a molten salt formation tank and electrolytically "pump-up" the electrode with lithium from the electrolyte, to lithium percentages of at least about 12%, with the pre-ferred range being about 6 to 25 weight percent lithium. Manufacturers of lithium alloys have attempted to fabricate lithium-aluminum electrodes having the preferred range of weight percent lithium by melting the components together in low humidity, dry, and a~gon atmospheres, and then pouring the molten liquid into molds, but they have not been entirely successful for the reasons that the handling of such a molten liquid is extremely hazardous and unusuallydifficult in an inert atmosphere~ At the elevated temperatures required to melt the components, the lithium acts as a getter for oxygen, nitrogen and water vapor. The resulting alloy by these procedures is generally ;
brittle, contaminated and in the form of thick slabs that are difficult and literally impossible to ùtilize for battery manufacture.
Another problem associated with metallurgically prepared lithium-aluminum electrodes is that of providing low impurity levels while casting~
and after crushing, remelting af the metals or compacting the powder by powder metallurgical ~etho~s to ~o~ the lithium-aluminum alloy. High impurity levels in the lithium-alu~inum allo~ required t~at the fabricated elect~odes be cleaned 'i .i :
., ... . .. . , , ~ , .. .. . .. . .... . . . .
:.. .
by electrolytic methods similar to those described above for the preparation of electrodes by electrolytic methods.
Therefore, in view of the above, it is a primary object of the present invention to provide a method of preparing negative electrodes com-prised of a lithium-aluminum alloy relatively free of impurities for use in high-temperature electrochemical cells.
Another object of the present invention is to provide a method of preparing solid lithium-aluminum electrodes comprised of from about 6 to 25 weight percent, based on total composition, lithium without employing lengthy electrochemical processes or the necessity of handling or working with molten metals as in the case of prior art metallurgical methods of preparing such ~, electrodes.
Still another object of the present invention, is to provide es-sentially uniform and dimensionally stable electrodes comprised of lithium in amounts of from about 6 to 25 weight percent, based on total composition, and :t . : :
from about 75 to 94 weight percent, based on total composition, aluminum.
The foregoing and other objects and features of the invention will i be evident from the following detailed description thereof.
;1 :
j In the broadest aspect of this invention, the method for preparing ~ -the lithium-aluminum electrode comprises forming a sandwich comprised of sheets of lithium and aluminum such that the lithium is disposed between the aluminum layers of the sandwich. The thus formed sandwich is then heat soaked at a temperature below the melting point of lithium while simultaneously applying pressure to the sandwich to assure contact between the abutting : 3 ~ :
surfaces of lithium and aluminum sheets making up the sandwich thereby causing the lithium and aluminum to chemically react to form a lithium-alumi-num alloy.
A more complete understanding of the invention will be had from the following detailed description taken in conjunction with the accompanying drawin~s.
Figure 1 is a diagrammatic exploded view of a lithium-aluminum i~ ~
A
A
~ ., ;. ' ~
' ' ' . ' . ' .
electrode in the process of abrication in accordance with the method of the invention;
Figure 2 is a diagrammatic assembled view of a lithium-aluminum electrode in the process of fabrication in accordance with the method of the invention; and Figure 3 is a view taken along the line III-III of Figure 2.
Before explaining the present invention in detail, it is to be understood that the invention is not limited in its application to the part- -.
icular construction and arrangements of parts illustrated in the accompanying drawings, since the invention is capable of other embodiments and of being practiced and carried on in various ways. Also, it is to be understood that ' the phraseology or terminology employed herein as well as the example-given if hereinafter is for the purpose of description and not of limitation.
! This invention will be further understood by reference to the drawings wherein diagrammatic views illustrating the method in accordance with the invention are shown in Figures 1-3. ~ ' f'f In Figure 1, 10 generally represents a thin sheet of substantially pure aluminum. The peripheral edges 12 of the sheet 10 are turned upwardly along fold-lines 14 to, in effect, form an open topped, shallow rectangular box. Illustrated above the rectangular box is a thin sheet or ribbon 16 of ' :~
Y substantially pure lithium. The lithium sheet 16 is preferably sized to fit substantially exactly within the fold-lines 14. Positioned above the lithium ~: sheet 16 is another sheet of aluminum 18 which is also sized to fit substant-tially exactly within the fold-lines 14.
In accordance with the invention, the lithium sheet 16 is placed within the rectangul~r box ormed by the aluminum sheet 10 and the aluminum sheet 18 îs placed on top of the lithium sheet 16 thereby orming a sandwich comprised'o alu~inum lithium-alu~inu~ as is best illustrated in Figure 3.
Thereafter, the'peripheral edgesl2 of aluminum s~eet 10 are folded over on to .`!
the peripheral edges of the'aluminum sheet 18 thereby enveloping the lithium f sheet 16.
e ~ ' ".. . ~ , . ' ' . , . `
" ~ ' ' ' ' ` ' '' " ' ' ' ~ ' . '' ' . ', '. :
'~ ; ;
104;ZS03 It should be pointed out here that the sandwich ~ust described is merely exemplary of various ways of actually forming the sandwich. The sand-wich may, for example, be formed of multiple layers of three or more planar sheets of lithium and aluminum in various configurations, e.g. square, CiTCU-lar, etc., or from one continuous sheet of aluminum folded in half or on ~ ~-itself multiple times with a lithium sheet or sheets being disposed between the folds of the aluminum sheet. Thus, a multilayered sandwich is envisioned comprised of lithium and aluminum with lithium being disposed between the aluminum layers of the sandwich. Of course, combinations of these examples are possible and other ways of forming the sandwich will be obvious to those -~
skilled in the art.
In the just given examples, the dimensions of the aluminum sheet or sheets may be, if ~esired, sized so as to allow the peripheral edges there- ^
of to be folded over to enclose all or some of the peripheral edges of the lithium sheet or sheets. Also, it is not required that the lithium sheet or sheets be coextensive in their surface areas with those of the aluminum sheet or sheets surface areas within which or between which they are disposed. All ~-that is required is that a layered sandwich of lithium and aluminum be formed such that lithium is disposed between the aluminum layers of the sandwich with the required amounts of each material being present to form the desired alloy composition for the electrode to be fabricated.
After the sandwich is fabricated, sufficient heat and pressure for appropriate lengths of time are applied to the sandwich in order to permit the lithium sheet 16 to alloy with the aluminum sheets 10 and 18. - `
The order in which the manulative steps of the method of the inven-tion are carried out is not to be considered limiting. Furthermore, except ~or an aspect of the invention described below in Example VI, it is preferred that the steps of the method be carried out in an inert atmosphere, e.g., argon, heliu~ or other rare gases.
~30 The uniform formation OI the desired lithium-aluminum electrode by .. . .
., ~- . ,, - - . . , . . : . . ~ . . , .. ; , .. . .. . . . .
the novel method of the invention depends on an initial close cantact between the lithium and aluminum sheets of the sandwich. To insure a high degree of contact between the abuting faces of the lithium~aluminum sheets of the sand-` wich, the sandwich can be placed in a press during the alloy formation. Also, while the desired alloy will form by the mere contact of the sheets of lithium and aluminum, the application of heat to the sandwich during alloy formation will increase the speed Of the reaction.
It should be pointed out here that during experiments in carrying out the method of the invention, variations existed from sample to sample with respect to alloy completion, and also, that the peripheral edges 12 of the aluminum sheet 10 are not in direct contact with the lithium sheet 16 resulting in non-completion of the alloy along the edges of the sandwich.
These results do not, however, prevent the use of electrodes formed by the , method of the invention as anodes in cells since after a few cycles of charge and discharge of the cell in which they are utilized the non-alloyed aluminum will be alloyed with lithium contained in the molten salt bath. This would also be so in the case in which the surface dimensions of the lithium sheet 1 are not coextensive with the dimensions of the surfaces of the aluminum sheets `1 between which it is sandwiched.
A better understanding of the present invention can be obtained from the following examples.
!~ .
In a glove box having an argon atmosphere, a sandwich of aluminum-lithium-aluminum was prepared such that the total percentage of lithium in the ~, sandwich was equivalent to about 12-18 weight percent, based on total composi-tion. The sandwich constructed was of the type illustrated ln Figures 1-3.
The sandwich was placed between the heatable plattens of a small Burton Press and heat and p~essure were applied to the sandwich. The sandwich was heat soaked at a te~peratu~e below, close to, hut not equal to the melting point of lithium C179C.~. Sufficient pressure was applied to assure contact between 'i ~' , .
the abuting faces o the sandwich. It may be pointed out here that the amount of pressure applied to the sand~ich is not critical other than it should be enough to assure contact. In this example, the pressure applied was approx-imately 30 psi. The time of heat soaking was sufficient for the lithium to alloy with the aluminum. Of course, the time of heat soaking will vary with the thickness of the layers of the sandwich. In this particular example, the aluminum sheets were about 32 mils thick and the lithium about 40 mils thick and it required about 175C. for approximately 8 hours. Upon cooling the thus formed lithium-aluminum electrode was assembled into a cell of the type here -contemplated. -EXAMPLE II
~ ~ . . . - ,, .
In a glove box having an argon atmosphere, an aluminum-lithium-aluminum sandwich was fabricated in accordance with the type illustrated in Figures 1-3. The lithium in the sandwich was equivalent to about 17.4 weight percent) based on total composition and the sandwich was approximately 4 in.
by 4 in. The sandwich was placed in a room temperature furnace and the "
temperature was gradually raised to approximately 450C. which took about 20 - -minutes. Thereafter, the sandwich was cooled and examined. Examination showed that there was no uniformity in alloy formation, the sandwich was badly mis~
shapened and unusable as a cell electrode. It is believed that these results were effected because there was no containment of the sandwich other than the j sandwich package itself and because the 450C. temperature was above the melt-ing point of the lithium contained in the sandwich.
EXAMPLE III
An alloy sandwich was prepared as in Example II with a lithium content equivalent to about 16.4 weight percent, based on total composition.
The sand~ich was placed between the heatable plattens of a press. The pressure applied was approximately 8Q psi and the temperature of the plattens was raised to~about 28~C. Lithium melted and spurted out of the sandwich at the edges 3Q thereof, Some alloy formed but was only about 6.4% lithium~ The lithium ' ,, ~;~ ' ' ' ' '' ', `~ , " '',"' ' .'' ' ,'`,'` ', " ' ' ~ '' ` ' ` " '` '` I' ' ` ' ' that escaped vigorously attacked the press plattens. Again, the temperature utilized in this example ~as aboYe the melting point of lithium.
EXAMPLE rv An alloy sandwich was prepared as in Example II with a lithium con-tent equivalent to about 15.8 weight percent, based on total co~position.
The sandwich was placed between the heatable plattens of a press. The pressure applied was 30 psi. The temperature of the plattens was gradually !, raised from room temperature. A fast reaction was noted at about 149C. At -this point, the electric power to plattens was removed and the temperature of the plattens was monitored. The te~perature rose to about 208C. due to the exothermic nature of the reaction. After cooling, examination of the sandwich showOEd substantially complete alloying and no loss of lithium. The electrode was usable as a cell electrode.
EXAMPLE V
This example involves two sandwiches fabricated as in Example II, which, also in an argon atmosphere, were placed in a steel cell container together with a separator and carbon cathode in a mock-up of a battery cell a without a top or electric current collectors. Each anode was about 15.9%
lithium by weight. The entire assembly was placed between press plattens at room temperature and approximately 13 psi of pressure were applied to the assembly. The actual pressure applied to the anode sandwiches was unknown, but all components were tightly pressed into the cell's steel container and ¦l thereby formed a holder or container for the anode sandwiches. The plattens -'~ were heated for approximately 6 minutes and the platten temperature reached approximately 176C. At this point, electric power to the plattens was remo~ed. The temperature had not reached the melting point of lithium, 179C.~
'~ and co~ponent temperature naturally lagged and could not exceed 176C. A reac-3 tîon was noted 7 minutes later and platten te~perature rose to about 187C. for -~ about 1 minute and then gradually rose to a peak temperature of about 225C.
~ 30 Ater cooling and disassembly~ examination showed that both anodes were well .:
., :.j ~ . - . . .. . .
.: .: , .
~)4Z503 formed. No attack of molten lithium on adjacent components was noted nor were there any beads of free unreacted lithium present.
EXAMPLE VI
A complete cell was fabricated in an argon atmosphere i~nd was sealed completely, leak checked and was removed to a normal room atmosphere. The anodes were fabricated as in Example II with a lithium content of about 8% -by weight. The cell was placed in an oven at room temperature with a set point of about 170C. The temperature at the cell's surface was monitored as the oven warmed. It took about 105 minutes for the 170C. set point of the oven to be reached. A reaction was apparent at about 153C. and the temper-ature rose to 176C. although heat was turned off at 153C. The cell was I cooled and then placed in a furnace set-up to cycle cells through chaTge and `~ discharge cycles. The cell was cycled for 13 cycles, found to perform ade-.~ - - . .
~t quately and to reach a rating of 10 ampere hours.
¦ These examples, among other things, illustrate the alternatives of ~; forming the aluminum-lithium alloy in accordance with the invention in argon or inert gas atmospheres if only anodes are desired or causing the formation ;~ -of such alloys in the cell container, in situ, in the ambient atmosphere, if -~ -desired.
; Electrodes or anodes fabricated by the method of the invention afford the lowest possible contamination by oxides, nitrides, carbonates, etc.
since the lithium sheets can be the purest state of lithium, and the aluminum sheets can be virgin, electrical grade, aluminum of 99.5 minimum percent alumi-num. Initial low contamination is not the only advantage for method of the s~ invention. Cost of manufacture of lithium-aluminum electrodes is drastically i reduced since the extra costs of grinding, casting etc., normally attendant ,~ with metallurgical processes for forming lithium-aluminum elect~odes a~e ellminated. The simplicity of sandwich making, and unattended heat soaking of the sandwich further reduces costs by avoiding the, only partially success-ful, anode cleaning procedures required of prior art lithium-aluminum imodes : g_ ~
. .
~04Z5~)3 prepared by the metallurgical processes of melting and casting the alloy con-stituents.
~:
3~
'1;`::: :
.-~
.,~
~i ,Y~
.
:, . :. ~ :-' :
. .
It may be explained here that high power delivery and rapid charge, and discharge above the range of a conventional lead-acid storage battery can be obtained from a high temperature electrical energy storage battery or cell comprising a pair of electrodes, at least one of which is a negat;ve electrode rnGrs~d in ~ comprised of lithium and aluminum~the electrode being ~ d or in contact with a fused alkali halide electrolyte. The fast charging characteristics of ~ such a cell are mainly attributable to the highly reversible lithium-aluminum ', negative electrode of the cell. The positive electrode of such a cell can be '~ carbon or any other suitable material.
The prior art methods for producing the lithium-aluminum negative electrode have been primarily either electrochemical or metallurgical.
In the electrochemical method, lithium-aluminum electrodes were produced by electrochemically charging a substantially pure aluminum electrode in an electrolyte containing lithium halide salt or salts. This electrochemi-;~ cal method was essentially effected by immersing a positive electrode, such as ;~
carbon, and a negative electrode, the aluminum electrode, into a molten lith-ium containing electrolyte and impressing an appropriate voltage across the two electrodes. Lithium in the electrolyte would diffuse into the aluminum electrode structure to form the desired lithium-aluminum electrode. - ~-~; In the metallurgical method, lithium-aluminum electrodes were pro-duced by melting a mixture containing a predetermined amount of each metal to form an alloy of lithium-aluminum. ~ ;
.1 One of the difficulties associated with the above described elec-~i troch~mical method of preparing lithium-aluminum electrodes is that after they have been elect~olytically for~ed, it is necessary to precondition the ~1li 3o electrodes by initially operating them through a number of time consuming ~i . j , :
:, . , , , . . ~ , .
~04'~503 cycles of slow charge and discharge. If the initial cycles are carried out too quickly, regions of liquid metal alloy can be produced resulting in pit-ting of the electrode. Another difficulty presented in the use of electro-chemically prepared lithium-aluminum electrodes is their lack of dimensional stability due to the fact that during the forming and preconditioning steps, they have been found to sometimes expand.
The preparation of lithium-aluminum electrodes by metallurgical techniques has also presented problems in that it has been difficult in the past to obtain lithium-aluminum alloys with compositions much in excess of 5 weight percent lithium with acceptable purity levels and lack of fragility.
Due to this less than desirable percentage of lithium, it was necessary to place the 5 weight percent lithium-aluminum electrodes in a molten salt formation tank and electrolytically "pump-up" the electrode with lithium from the electrolyte, to lithium percentages of at least about 12%, with the pre-ferred range being about 6 to 25 weight percent lithium. Manufacturers of lithium alloys have attempted to fabricate lithium-aluminum electrodes having the preferred range of weight percent lithium by melting the components together in low humidity, dry, and a~gon atmospheres, and then pouring the molten liquid into molds, but they have not been entirely successful for the reasons that the handling of such a molten liquid is extremely hazardous and unusuallydifficult in an inert atmosphere~ At the elevated temperatures required to melt the components, the lithium acts as a getter for oxygen, nitrogen and water vapor. The resulting alloy by these procedures is generally ;
brittle, contaminated and in the form of thick slabs that are difficult and literally impossible to ùtilize for battery manufacture.
Another problem associated with metallurgically prepared lithium-aluminum electrodes is that of providing low impurity levels while casting~
and after crushing, remelting af the metals or compacting the powder by powder metallurgical ~etho~s to ~o~ the lithium-aluminum alloy. High impurity levels in the lithium-alu~inum allo~ required t~at the fabricated elect~odes be cleaned 'i .i :
., ... . .. . , , ~ , .. .. . .. . .... . . . .
:.. .
by electrolytic methods similar to those described above for the preparation of electrodes by electrolytic methods.
Therefore, in view of the above, it is a primary object of the present invention to provide a method of preparing negative electrodes com-prised of a lithium-aluminum alloy relatively free of impurities for use in high-temperature electrochemical cells.
Another object of the present invention is to provide a method of preparing solid lithium-aluminum electrodes comprised of from about 6 to 25 weight percent, based on total composition, lithium without employing lengthy electrochemical processes or the necessity of handling or working with molten metals as in the case of prior art metallurgical methods of preparing such ~, electrodes.
Still another object of the present invention, is to provide es-sentially uniform and dimensionally stable electrodes comprised of lithium in amounts of from about 6 to 25 weight percent, based on total composition, and :t . : :
from about 75 to 94 weight percent, based on total composition, aluminum.
The foregoing and other objects and features of the invention will i be evident from the following detailed description thereof.
;1 :
j In the broadest aspect of this invention, the method for preparing ~ -the lithium-aluminum electrode comprises forming a sandwich comprised of sheets of lithium and aluminum such that the lithium is disposed between the aluminum layers of the sandwich. The thus formed sandwich is then heat soaked at a temperature below the melting point of lithium while simultaneously applying pressure to the sandwich to assure contact between the abutting : 3 ~ :
surfaces of lithium and aluminum sheets making up the sandwich thereby causing the lithium and aluminum to chemically react to form a lithium-alumi-num alloy.
A more complete understanding of the invention will be had from the following detailed description taken in conjunction with the accompanying drawin~s.
Figure 1 is a diagrammatic exploded view of a lithium-aluminum i~ ~
A
A
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' ' ' . ' . ' .
electrode in the process of abrication in accordance with the method of the invention;
Figure 2 is a diagrammatic assembled view of a lithium-aluminum electrode in the process of fabrication in accordance with the method of the invention; and Figure 3 is a view taken along the line III-III of Figure 2.
Before explaining the present invention in detail, it is to be understood that the invention is not limited in its application to the part- -.
icular construction and arrangements of parts illustrated in the accompanying drawings, since the invention is capable of other embodiments and of being practiced and carried on in various ways. Also, it is to be understood that ' the phraseology or terminology employed herein as well as the example-given if hereinafter is for the purpose of description and not of limitation.
! This invention will be further understood by reference to the drawings wherein diagrammatic views illustrating the method in accordance with the invention are shown in Figures 1-3. ~ ' f'f In Figure 1, 10 generally represents a thin sheet of substantially pure aluminum. The peripheral edges 12 of the sheet 10 are turned upwardly along fold-lines 14 to, in effect, form an open topped, shallow rectangular box. Illustrated above the rectangular box is a thin sheet or ribbon 16 of ' :~
Y substantially pure lithium. The lithium sheet 16 is preferably sized to fit substantially exactly within the fold-lines 14. Positioned above the lithium ~: sheet 16 is another sheet of aluminum 18 which is also sized to fit substant-tially exactly within the fold-lines 14.
In accordance with the invention, the lithium sheet 16 is placed within the rectangul~r box ormed by the aluminum sheet 10 and the aluminum sheet 18 îs placed on top of the lithium sheet 16 thereby orming a sandwich comprised'o alu~inum lithium-alu~inu~ as is best illustrated in Figure 3.
Thereafter, the'peripheral edgesl2 of aluminum s~eet 10 are folded over on to .`!
the peripheral edges of the'aluminum sheet 18 thereby enveloping the lithium f sheet 16.
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" ~ ' ' ' ' ` ' '' " ' ' ' ~ ' . '' ' . ', '. :
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104;ZS03 It should be pointed out here that the sandwich ~ust described is merely exemplary of various ways of actually forming the sandwich. The sand-wich may, for example, be formed of multiple layers of three or more planar sheets of lithium and aluminum in various configurations, e.g. square, CiTCU-lar, etc., or from one continuous sheet of aluminum folded in half or on ~ ~-itself multiple times with a lithium sheet or sheets being disposed between the folds of the aluminum sheet. Thus, a multilayered sandwich is envisioned comprised of lithium and aluminum with lithium being disposed between the aluminum layers of the sandwich. Of course, combinations of these examples are possible and other ways of forming the sandwich will be obvious to those -~
skilled in the art.
In the just given examples, the dimensions of the aluminum sheet or sheets may be, if ~esired, sized so as to allow the peripheral edges there- ^
of to be folded over to enclose all or some of the peripheral edges of the lithium sheet or sheets. Also, it is not required that the lithium sheet or sheets be coextensive in their surface areas with those of the aluminum sheet or sheets surface areas within which or between which they are disposed. All ~-that is required is that a layered sandwich of lithium and aluminum be formed such that lithium is disposed between the aluminum layers of the sandwich with the required amounts of each material being present to form the desired alloy composition for the electrode to be fabricated.
After the sandwich is fabricated, sufficient heat and pressure for appropriate lengths of time are applied to the sandwich in order to permit the lithium sheet 16 to alloy with the aluminum sheets 10 and 18. - `
The order in which the manulative steps of the method of the inven-tion are carried out is not to be considered limiting. Furthermore, except ~or an aspect of the invention described below in Example VI, it is preferred that the steps of the method be carried out in an inert atmosphere, e.g., argon, heliu~ or other rare gases.
~30 The uniform formation OI the desired lithium-aluminum electrode by .. . .
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the novel method of the invention depends on an initial close cantact between the lithium and aluminum sheets of the sandwich. To insure a high degree of contact between the abuting faces of the lithium~aluminum sheets of the sand-` wich, the sandwich can be placed in a press during the alloy formation. Also, while the desired alloy will form by the mere contact of the sheets of lithium and aluminum, the application of heat to the sandwich during alloy formation will increase the speed Of the reaction.
It should be pointed out here that during experiments in carrying out the method of the invention, variations existed from sample to sample with respect to alloy completion, and also, that the peripheral edges 12 of the aluminum sheet 10 are not in direct contact with the lithium sheet 16 resulting in non-completion of the alloy along the edges of the sandwich.
These results do not, however, prevent the use of electrodes formed by the , method of the invention as anodes in cells since after a few cycles of charge and discharge of the cell in which they are utilized the non-alloyed aluminum will be alloyed with lithium contained in the molten salt bath. This would also be so in the case in which the surface dimensions of the lithium sheet 1 are not coextensive with the dimensions of the surfaces of the aluminum sheets `1 between which it is sandwiched.
A better understanding of the present invention can be obtained from the following examples.
!~ .
In a glove box having an argon atmosphere, a sandwich of aluminum-lithium-aluminum was prepared such that the total percentage of lithium in the ~, sandwich was equivalent to about 12-18 weight percent, based on total composi-tion. The sandwich constructed was of the type illustrated ln Figures 1-3.
The sandwich was placed between the heatable plattens of a small Burton Press and heat and p~essure were applied to the sandwich. The sandwich was heat soaked at a te~peratu~e below, close to, hut not equal to the melting point of lithium C179C.~. Sufficient pressure was applied to assure contact between 'i ~' , .
the abuting faces o the sandwich. It may be pointed out here that the amount of pressure applied to the sand~ich is not critical other than it should be enough to assure contact. In this example, the pressure applied was approx-imately 30 psi. The time of heat soaking was sufficient for the lithium to alloy with the aluminum. Of course, the time of heat soaking will vary with the thickness of the layers of the sandwich. In this particular example, the aluminum sheets were about 32 mils thick and the lithium about 40 mils thick and it required about 175C. for approximately 8 hours. Upon cooling the thus formed lithium-aluminum electrode was assembled into a cell of the type here -contemplated. -EXAMPLE II
~ ~ . . . - ,, .
In a glove box having an argon atmosphere, an aluminum-lithium-aluminum sandwich was fabricated in accordance with the type illustrated in Figures 1-3. The lithium in the sandwich was equivalent to about 17.4 weight percent) based on total composition and the sandwich was approximately 4 in.
by 4 in. The sandwich was placed in a room temperature furnace and the "
temperature was gradually raised to approximately 450C. which took about 20 - -minutes. Thereafter, the sandwich was cooled and examined. Examination showed that there was no uniformity in alloy formation, the sandwich was badly mis~
shapened and unusable as a cell electrode. It is believed that these results were effected because there was no containment of the sandwich other than the j sandwich package itself and because the 450C. temperature was above the melt-ing point of the lithium contained in the sandwich.
EXAMPLE III
An alloy sandwich was prepared as in Example II with a lithium content equivalent to about 16.4 weight percent, based on total composition.
The sand~ich was placed between the heatable plattens of a press. The pressure applied was approximately 8Q psi and the temperature of the plattens was raised to~about 28~C. Lithium melted and spurted out of the sandwich at the edges 3Q thereof, Some alloy formed but was only about 6.4% lithium~ The lithium ' ,, ~;~ ' ' ' ' '' ', `~ , " '',"' ' .'' ' ,'`,'` ', " ' ' ~ '' ` ' ` " '` '` I' ' ` ' ' that escaped vigorously attacked the press plattens. Again, the temperature utilized in this example ~as aboYe the melting point of lithium.
EXAMPLE rv An alloy sandwich was prepared as in Example II with a lithium con-tent equivalent to about 15.8 weight percent, based on total co~position.
The sandwich was placed between the heatable plattens of a press. The pressure applied was 30 psi. The temperature of the plattens was gradually !, raised from room temperature. A fast reaction was noted at about 149C. At -this point, the electric power to plattens was removed and the temperature of the plattens was monitored. The te~perature rose to about 208C. due to the exothermic nature of the reaction. After cooling, examination of the sandwich showOEd substantially complete alloying and no loss of lithium. The electrode was usable as a cell electrode.
EXAMPLE V
This example involves two sandwiches fabricated as in Example II, which, also in an argon atmosphere, were placed in a steel cell container together with a separator and carbon cathode in a mock-up of a battery cell a without a top or electric current collectors. Each anode was about 15.9%
lithium by weight. The entire assembly was placed between press plattens at room temperature and approximately 13 psi of pressure were applied to the assembly. The actual pressure applied to the anode sandwiches was unknown, but all components were tightly pressed into the cell's steel container and ¦l thereby formed a holder or container for the anode sandwiches. The plattens -'~ were heated for approximately 6 minutes and the platten temperature reached approximately 176C. At this point, electric power to the plattens was remo~ed. The temperature had not reached the melting point of lithium, 179C.~
'~ and co~ponent temperature naturally lagged and could not exceed 176C. A reac-3 tîon was noted 7 minutes later and platten te~perature rose to about 187C. for -~ about 1 minute and then gradually rose to a peak temperature of about 225C.
~ 30 Ater cooling and disassembly~ examination showed that both anodes were well .:
., :.j ~ . - . . .. . .
.: .: , .
~)4Z503 formed. No attack of molten lithium on adjacent components was noted nor were there any beads of free unreacted lithium present.
EXAMPLE VI
A complete cell was fabricated in an argon atmosphere i~nd was sealed completely, leak checked and was removed to a normal room atmosphere. The anodes were fabricated as in Example II with a lithium content of about 8% -by weight. The cell was placed in an oven at room temperature with a set point of about 170C. The temperature at the cell's surface was monitored as the oven warmed. It took about 105 minutes for the 170C. set point of the oven to be reached. A reaction was apparent at about 153C. and the temper-ature rose to 176C. although heat was turned off at 153C. The cell was I cooled and then placed in a furnace set-up to cycle cells through chaTge and `~ discharge cycles. The cell was cycled for 13 cycles, found to perform ade-.~ - - . .
~t quately and to reach a rating of 10 ampere hours.
¦ These examples, among other things, illustrate the alternatives of ~; forming the aluminum-lithium alloy in accordance with the invention in argon or inert gas atmospheres if only anodes are desired or causing the formation ;~ -of such alloys in the cell container, in situ, in the ambient atmosphere, if -~ -desired.
; Electrodes or anodes fabricated by the method of the invention afford the lowest possible contamination by oxides, nitrides, carbonates, etc.
since the lithium sheets can be the purest state of lithium, and the aluminum sheets can be virgin, electrical grade, aluminum of 99.5 minimum percent alumi-num. Initial low contamination is not the only advantage for method of the s~ invention. Cost of manufacture of lithium-aluminum electrodes is drastically i reduced since the extra costs of grinding, casting etc., normally attendant ,~ with metallurgical processes for forming lithium-aluminum elect~odes a~e ellminated. The simplicity of sandwich making, and unattended heat soaking of the sandwich further reduces costs by avoiding the, only partially success-ful, anode cleaning procedures required of prior art lithium-aluminum imodes : g_ ~
. .
~04Z5~)3 prepared by the metallurgical processes of melting and casting the alloy con-stituents.
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. .
Claims (5)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1 The method for preparing a negative lithium-aluminum electrode comprising the steps of:
a) forming a sandwich comprised of sheets of lithium and aluminum such that lithium is disposed between the aluminum layers of the sandwich;
and b) heat soaking the sandwich of step (a) at a temperature below the melting point of lithium while simultaneously applying pressure to the sandwich to assure contact between the abuting surfaces of lithium and aluminum sheets making up the sandwich of step (a) thereby causing the lithium and aluminum to chemically react to form a lithium-aluminum alloy.
a) forming a sandwich comprised of sheets of lithium and aluminum such that lithium is disposed between the aluminum layers of the sandwich;
and b) heat soaking the sandwich of step (a) at a temperature below the melting point of lithium while simultaneously applying pressure to the sandwich to assure contact between the abuting surfaces of lithium and aluminum sheets making up the sandwich of step (a) thereby causing the lithium and aluminum to chemically react to form a lithium-aluminum alloy.
2. A method in accordance with Claim 1 wherein the sandwich of step (a) is placed in a cell container and step (b) is effected while the sandwich of step (a) is in the cell container.
3. The method of Claim 1 wherein the sandwich of step (a) is com-prised of a pair of sheets of aluminum having a sheet of lithium disposed therebetween.
4. The method of Claim 2 wherein the pair of sheets of aluminum are rectangular in shape and one of the sheets of the pair is sized larger in its peripheral dimensions in order that the peripheral edges thereof may be folded over onto the face of the other aluminum sheet thereby enveloping the lithium contained in the sandwich of step (a).
5. The method of Claim 1 wherein the lithium-aluminum alloy formed is comprised of lithium in amounts of from about 6 to 25 weight percent, based on total composition, and from about 75 to 94 weight percent, based on total composition, aluminum.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/584,629 US3981743A (en) | 1975-06-06 | 1975-06-06 | Method of preparing a lithium-aluminum electrode |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1042503A true CA1042503A (en) | 1978-11-14 |
Family
ID=24338168
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA248,830A Expired CA1042503A (en) | 1975-06-06 | 1976-03-25 | Method of preparing a lithium-aluminum electrode using heat and pressure |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3981743A (en) |
| CA (1) | CA1042503A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5278005A (en) * | 1992-04-06 | 1994-01-11 | Advanced Energy Technologies Inc. | Electrochemical cell comprising dispersion alloy anode |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4056885A (en) * | 1976-12-15 | 1977-11-08 | Exxon Research & Engineering Co. | Method of preparing lithium-aluminum alloy electrodes |
| US4172926A (en) * | 1978-06-29 | 1979-10-30 | The United States Of America As Represented By The United States Department Of Energy | Electrochemical cell and method of assembly |
| US4448861A (en) * | 1983-06-24 | 1984-05-15 | Rayovac Corporation | Lithium-thionyl chloride cell with lithium surface alloys to reduce voltage delay |
| US4824744A (en) * | 1984-09-14 | 1989-04-25 | Duracell Inc. | Method of making cell anode |
| JPH0630246B2 (en) | 1985-03-12 | 1994-04-20 | 日立マクセル株式会社 | Button type lithium organic secondary battery |
| JPS62119877A (en) * | 1985-11-19 | 1987-06-01 | Fuji Elelctrochem Co Ltd | Manufacture of negative electrode for secondary cell of nonaqueous electrolytic solution |
| JPS63202851A (en) * | 1987-02-17 | 1988-08-22 | Fuji Elelctrochem Co Ltd | Manufacture of negative electrode for nonaqueous electrolyte secondary battery |
| JP2934449B2 (en) * | 1989-03-23 | 1999-08-16 | 株式会社リコー | Rechargeable battery |
| DE4030205C3 (en) * | 1989-09-25 | 1994-10-06 | Ricoh Kk | Negative electrode for secondary battery and a method of manufacturing this electrode |
| US8318342B2 (en) * | 2007-06-22 | 2012-11-27 | Panasonic Corporation | All solid-state polymer battery |
| JP7401317B2 (en) * | 2020-01-21 | 2023-12-19 | 本田技研工業株式会社 | solid state battery |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3462312A (en) * | 1966-01-03 | 1969-08-19 | Standard Oil Co | Electrical energy storage device comprising fused salt electrolyte,tantalum containing electrode and method for storing electrical energy |
| US3428493A (en) * | 1966-01-03 | 1969-02-18 | Standard Oil Co | Electrical energy storage device comprising aluminum-lithium electrode and mechanical screen surrounding the electrode |
| US3751298A (en) * | 1971-05-21 | 1973-08-07 | Union Carbide Corp | Thermal, rechargeable electrochemical cell having lithium monoaluminide electrode and lithium tetrachloroaluminate electrolyte |
-
1975
- 1975-06-06 US US05/584,629 patent/US3981743A/en not_active Expired - Lifetime
-
1976
- 1976-03-25 CA CA248,830A patent/CA1042503A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5278005A (en) * | 1992-04-06 | 1994-01-11 | Advanced Energy Technologies Inc. | Electrochemical cell comprising dispersion alloy anode |
Also Published As
| Publication number | Publication date |
|---|---|
| US3981743A (en) | 1976-09-21 |
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