EP1290749A4 - Electrolytes solides mineraux microporeux et procedes de preparation - Google Patents

Electrolytes solides mineraux microporeux et procedes de preparation

Info

Publication number
EP1290749A4
EP1290749A4 EP00927894A EP00927894A EP1290749A4 EP 1290749 A4 EP1290749 A4 EP 1290749A4 EP 00927894 A EP00927894 A EP 00927894A EP 00927894 A EP00927894 A EP 00927894A EP 1290749 A4 EP1290749 A4 EP 1290749A4
Authority
EP
European Patent Office
Prior art keywords
electrolyte
film
cell
electrolyte film
polymer
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.)
Withdrawn
Application number
EP00927894A
Other languages
German (de)
English (en)
Other versions
EP1290749A1 (fr
Inventor
Dong Hun Jang
Sa Heum Kim
Han Jun Kim
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Finecell Co Ltd
Original Assignee
Finecell Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Finecell Co Ltd filed Critical Finecell Co Ltd
Publication of EP1290749A1 publication Critical patent/EP1290749A1/fr
Publication of EP1290749A4 publication Critical patent/EP1290749A4/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0565—Polymeric materials, e.g. gel-type or solid-type
    • 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
    • H01M10/052—Li-accumulators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00—Electrolytes
    • H01M2300/0017—Non-aqueous electrolytes
    • H01M2300/0065—Solid electrolytes
    • H01M2300/0068—Solid electrolytes inorganic
    • H01M2300/0071—Oxides
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00—Electrolytes
    • H01M2300/0017—Non-aqueous electrolytes
    • H01M2300/0065—Solid electrolytes
    • H01M2300/0082—Organic polymers
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a solid electrolyte film usable in rechargeable cells. More particularly, it relates to a provision of pathways for ions mobile between a cathode and an anode during repeated charge and discharge of rechargeable cells by introducing liquid components and lithium salts (hereinafter, both are referred to as "liquid electrolytes") to a solid electrolyte film, having a microporous structure and containing an absorbent above the specific amount, according to the present invention.
  • liquid electrolytes liquid components and lithium salts
  • the rechargeable cell of the present invention includes three essential components, i.e., a cathode, an anode and an electrolyte.
  • the cell is made by laminating cathodes, anodes and electrolytes of sheet form.
  • Materials for said anode are carbons or polymer materials in which lithium metal or lithium ions can be intercalated/deintercalated.
  • Materials for said cathode are transition metal oxides or polymer materials in which lithium ions can be intercalated/deintercalated.
  • Materials for said electrolyte can be used the one according to the present invention, and a liquid electrolyte is introduced thereto after assembling the cell.
  • An electrolyte in the cell such as a rechargeable cell or an electrochemical reaction system is disposed between the conductive surfaces of cathode and anode.
  • the electrolyte is the insulator not having the electron conduction but has the ion conduction.
  • General electrolytes so far are consisted of only liquid components; however, more recent attentions are concentrated on the solid electrolytes having many advantages. Among them, the researches of using polymer as electrolytes have been tried.
  • the pure polymer electrolyte containing polar hetero-atoms has very low ionic conductivity of 10 "8 S/cm, it is difficult to use it at room temperature. Therefore, the main research on the polymer electrolytes focuses on the improvement of conductivity and, as a representative example, it was proposed to introduce liquid electrolyte component into the structure of polymer.
  • Gel-type electrolytes disclosed in US Patent 5,219,679 which contain liquid electrolytes in a polymer backbone have the proper conductivity while exhibiting properties of polymers. However, they already contain a large amount of liquid electrolytes during the manu acture of the polymer electrolytes, and thus said patent has problems as a vaporization/loss of liquid component, resulting in the change of composition and the decrease of conductivity. Furthermore, since lithium salts in the liquid electrolyte are very sensitive to moisture, the strict dehumidifying condition is required for the manufacture of gel electrolyte.
  • a hybrid polymer electrolyte system proposed in US Patent Nos. 5,296,318 and 5,418,091 can minimize the moisture effect on the process of manufacturing cells by adding liquid electrolytes after the packaging of cells, while taking advantage of the merits of gel-type polymer electrolytes. Since the liquid electrolytes are added after an electrolyte film is prepared, it is necessary for the inside of the electrolyte film to have sites capable of absorbing liquid components therein. To this end, plasticizers/processing aids are added in the step of preparing the electrolyte film, and after the assembly of cell is complete, they are extracted by the use of an organic solvent. However, due to such a process, the above methods have fatal demerits that the reproducibility is low, manufacturing yield is reduced, and the automation for mass production is difficult.
  • Japanese laid-open patent gazette No. 99-16561 discloses the polymer electrolyte system adding an inorganic filler to the porous structure made of a polyvinylidene fluoride-based resin.
  • This system provides a good ionic conductivity at room temperature and a mechanical strength possible to cast the form of film; however, the content of inorganic material is only 1.9 to 66% by weight (corresponding to 2 to
  • the electrolyte made of pure polymer has the poor ionic conductivity and thus it is difficult to apply that to the real process of manufacturing a cell.
  • the gel-type polymer electrolyte made under the condition containing a liquid electrolyte has a good ionic conductivity at room temperature because the ion conduction is carried out by the liquid electrolyte, but the process condition is limited and it is difficult to maintain the constant capacity.
  • the hybrid polymer electrolyte which is made by adding plasticizers/processing aids to make a film form and then removing them and resultantly rendering a liquid electrolyte absorbed, is advantageous in that its process is less affected by the manufacturing condition and it has a sufficient ion conductivity; however, the complicated multi-steps and the additional materials are required, and thus the process cost rises and the automation of process is difficult.
  • the polymer electrolyte into which the porosity is introduced by various methods such as solvent/non-solvent exchange, vulcanization, curing, extension, etc., has the problem that the microporous structure is collapsed at a lamination or pressing process and thus the abso ⁇ tion of liquid electrolyte is not sufficient.
  • the method of forming the film of porous structure on an electrode surface is advantageous in increasing the adhesive strength of the electrode surface, but its processing condition is not simple and thus it is not preferable.
  • the present inventors provided, in PCT 99/KR99/00798, the system wherein the conductivity of lithium ion can be increased by introducing the microporosity into the electrolyte film matrix containing an absorbent to make the abso ⁇ tion of liquid electrolyte easier.
  • the liquid electrolyte susceptible to moisture is added after the assembly of cell, whereby it is not necessary to remove said absorbent after the cell assembly.
  • the plasticizers or processing aids as in US patent Nos. 5,296,318, 5,418,091 and 5,631,103 are not required and the process is simple and the cost of process is low.
  • the present inventors found the fact that the problem may occur that the microporous structure of solid electrolyte film collapses and the abso ⁇ tive power drops at the step of binding a cathode and/or anode with the film. Therefore, the present inventors found that the absorbent of more than the specific amount is necessary so as to solve the above problem and thus accomplished the present invention.
  • the present invention provides adding inorganic materials, performing the functions of a structure filler as well as an absorbent, in more than the specific amount, to prevent the collapse of a porous structure and maintain the abso ⁇ tive power of solid electrolyte film and the conductivity of lithium ion at the cell- assembling process such as lamination or the pressing.
  • the absorbent particles contained in more than the specific amount, together with the porous structure improves the ability of absorbing the liquid electrolyte and, particularly, works as the structure element of improving the mechanical strength of electrolyte film and/or solid electrolyte. Therefore, the good conductivity of lithium ion can also be maintained even after the assembly of cell.
  • a separate operation is not necessary for the abso ⁇ tion of liquid electrolyte, and the essential feature can be exhibited that the liquid electrolyte is introduced after the assembly of cell.
  • the solid electrolyte according to the present invention contains an inorganic absorbent and also contains the electrolyte film of a microporous structure and an ion conductive liquid electrolyte.
  • the solid electrolyte for a rechargeable cell can be made by the activation process of rendering the ionic conductive liquid electrolyte absorbed into the microporous electrolyte film made of only the inorganic absorbent and a polymer binder.
  • electrolyte film used in the present specification refers to an electrolyte film which is in the dried condition and does not contain any liquid electrolytes.
  • solid electrolytes used in the present specification means said electrolyte film having an ionic conductivity by inco ⁇ orating liquid electrolytes thereto. Although the solid electrolytes are not in a complete solid state since they contain liquid electrolytes, they are called “solid electrolytes” in order to be distinguished from the liquid electrolytes because the basic backbone of solid electrolytes starts from the electrolyte film at a solid state.
  • Said electrolyte film can be preferably prepared by means of a phase inversion method.
  • Examples of such method include wet process and dry process.
  • the wet process refers to a process for the preparation of an electrolyte film, which comprises the steps of: dissolving a mixture of an absorbent and a polymer binder in a solvent for the polymer binder, making the resulting solution to a film form, exchanging the solvent with a non-solvent for the polymer binder, and then drying the resulting material to. form an electrolyte film.
  • the dry process refers to a process for the preparation of an electrolyte film, which comprises the steps of: mixing a mixture of an absorbent and a polymer binder with a solvent for dissolving the polymer binder, a non- solvent which does not dissolve the polymer binder, a pore former and a wetting agent, making the resulting mixture into a film form, and drying the resulting film completely.
  • the inorganic absorbent used in the present invention should absorb a liquid electrolyte due to the high affinity to the liquid electrolyte or increase the abso ⁇ tive power of the liquid electrolyte, and should not have the electron conductivity. Also, they should have the good mechanical, thermal, chemical and electrochemical properties.
  • As such inorganic absorbents it is possible to use one or two or more particles selected from the group consisting of mineral particles, synthetic oxide compound particles and mesoporous molecular sieves.
  • mineral particles include mineral particles having phyllosilicate structures such as clay, paragonite, montmorillonite and mica.
  • said synthetic oxide compounds particles include zeolite, porous silica, porous alumina and magnesium oxide.
  • mesoporous molecular sieves examples include mesoporous molecular sieves made of oxide compounds such as silica and having a pore diameter in 2 to 30 nm. Said mineral particles, synthetic oxide compounds particles and mesoporous molecular sieves may be used in the form of a mixture wherein two or more absorbents selected from the above mentioned absorbents are combined.
  • the particle size of inorganic absorbents is preferably not more than 40 ⁇ m, more preferably, not more than 20 ⁇ m so as not to decrease the mechanical strength and the uniformity of the electrolyte film.
  • the prior art such as Japanese laid-open patent gazette 1999-16561 uses the inorganic material of very small particle size (e.g., less than 20nm); however, in this case, the inorganic material cannot work as an absorbent and instead may prevent the crystallinity of filler or polymer film.
  • the inorganic absorbent should have the particle size of more than 50nm or the aggregated form in the several ⁇ m unit.
  • the form of inorganic absorbent is not particularly restricted and can be fiber, needle, plate or sphere form, but an asymmetric form is preferable so as to increase the mechanical strength of electrolyte film.
  • the first pu ⁇ ose of the present invention is to make the solid electrolyte maintaining the abso ⁇ tive power of liquid electrolyte and the ionic conductivity, which results from the fact that the microporous structure is not destroyed and have a mechanical strength even after the assembly of cell.
  • the amount of inorganic absorbent is preferably at least more than 70% by weight based upon the amount of electrolyte film consisting of the inorganic absorbent and the polymer binder, more preferably 70% to 95% by weight.
  • 70% by weight is the starting point where the below problems occur.
  • the inorganic amount is not more than 70% by weight
  • the absorptive power of liquid electrolyte and the ionic conductivity decrease largely because the porous structure of solid electrolyte film tends to collapse at the laminating or pressing step for the assembly of cell.
  • the present inventors made solid electrolyte films having the different amount of inorganic absorbents and then observed the change of the thickness and the change of ionic conductivity depending on the external pressure applied at the cell manufacturing process. From such an experiment, it was found the fact that the thickness of solid electrolyte film and the ionic conductivity change suddenly from 70% by weight. This fact was not suggested or taught at the prior arts and was discovered by the present inventors for the first time.
  • the inorganic amount is not more than 70% by weight, even though many absorbents are contained, it is difficult to solve completely the problems indicated at the electrolyte mainly comprising polymers.
  • the deterioration at low or high temperature occurs.
  • the motion of polymer chains directly affects the ionic conductivity in polymer electrolytes, the effect of temperature on the ionic conductivity becomes significant.
  • the motion of polymer chains is restricted, which significantly reduces the ionic conductivity, thereby resulting in severe deterioration in the performance of a cell.
  • using the inorganic absorbent as in the present invention increases the ionic conductivity.
  • the inorganic absorbent not being susceptible to the temperature, in more than the specific amount, minimizes the effect of temperature contrary to the property of the existing polymer electrolytes. Also, as the inorganic absorbent of a large amount is contained in an electrolyte, the electrolyte according to the present invention has a merit in that the resistance against ignition or explosion is improved compared to the electrolytes containing the organic material such as polymers at a large amount.
  • polystyrene resin As a polymer binder, it is possible to use most common polymers. Among them, it is preferred to use a mixture of one or two or more polymers selected from the group consisting of polyvinylidene fluoride, copolymers of vinylidene fluoride and hexafluoropropylene, copolymers of vinylidene fluoride and maleic anhydride, polyvinylchloride, polyvinylacohol, polyvinyl formal, polymethylmethacrylate, polymethacrylate, cellulose triacetate, polyurethane, polyimide, polycarbonate, polysulfone, polyether, polyethylene oxide, polyolefine such as polyethylene or polypropylene, polyisobutylene, polybutyldiene, polyacrylonitrile, acrylonitrilebutyldiene rubber, ethylene-propylene-diene-monomer, tetra(ethylene glycol)diacrylate, polydimethylsiloxane
  • the polymer binders of which the property changes largely or in which a crosslinking reaction, a curing reaction and the like occur by a heat and a pressure are not preferred. Also, it is not preferred to induce polymerization, copolymerization, crosslinking, curing reaction by adding at least one kind of material at the state of monomer. That is because unreacted monomers may be impregnated in the inorganic absorbent and later it reacts with electrolyte compounds to decrease the performance of cell, and thus the separate process of removing themi is necessary. Therefore, it is preferred to avoid the condition that the above problems may occur at the manufacturing process of electrolyte film or the assembly process of cell.
  • a solvent for the polymer binder which has the solubility for the polymer binder a mixture of one or two or more solvents selected from the group consisting of N-methylpyrrolidinone, dimethylformamide, dimethylacetamide, tetrahydrofuran, acetonitrile, cyclohexanone, chloroform, dichloromethane, hexamethylphosphoramide, dimethylsulfoxide, acetone and dioxane.
  • non-solvent for the polymer binder which does not have the solubility for the polymer binder or has little solubility and which has the compatibility for the solvents, it is possible to use a mixture of one or two or more selected from the group consisting of water, ethanol, ethylene glycol, glycerol, acetone, dichloroemethane, ethylacetate, butanol, pentanol, hexanol and ether.
  • the solid electrolyte having the porous structure according to the present invention can be prepared by wet process consisting of five steps, i.e., dissolving a polymer binder, mixing an inorganic absorbent, film casting, making porous polymer matrix and drying, and activation.
  • a polymer binder is dissolved in a solvent and then an inorganic absorbent is added in the solution and sufficiently mixed to be dispersed uniformly.
  • the solid content of said mixed solution is preferably 5 to 60% by weight based on the total weight of the solution. If the content is not more than 5% by weight, the mechanical strength of an electrolyte film decreases and if the content is more than 60% by weight, the inorganic absorbent cannot be dispersed sufficiently or the viscosity of the mixed solution becomes high, which is problematic.
  • a magnetic stirrer, a mechanical stirrer, a planetary mixer or a high-speed disperser can be used to stir the mixed solution. While stirring, an ultrasonic stirrer may be adopted to prevent the absorbent from agglomerating or bubbling during the mixing.
  • the mixed solution may be subjected to defoaming and filtration steps.
  • the resulting mixture is made to the form of film.
  • the mixed solution may be poured on a flat plate and then be subjected to casting.
  • the mixed solution may be extracted from a die with a fixed gap and then coated onto a substrate.
  • the substrate can be used materials which have a chemical, thermal and mechanical stability and can be separated from the electrolyte film during a lamination process.
  • polymer film such as polyester, polytetrafluoroethylene, paper, etc., can be used.
  • Various other application methods can be selected.
  • the film is contacted with a non-solvent to exchange the solvent for polymer binder.
  • a non-solvent for example, it is possible to extract the solvent by immersing the film in a non-solvent pool. Accordingly, it is preferable to select the combination of a miscible solvent and a non-solvent.
  • the immersion time in the non-solvent pool varies from one minute to one hour depending on the kinds of the solvents and non-solvents. When the time is shorter, it is difficult to obtain sufficient porosity. On the contrary, when the time exceeds the defined time, the productivity becomes decreased, which is not preferable.
  • the temperature in the pool is preferably from 10°C to 90°C, more preferably from 20°C to 80°C.
  • the solid electrolyte having a porous structure according to the present invention can be prepared by dry process consisting of five steps, i.e., dissolving a polymer binder, mixing an inorganic absorbent, adding additives (non-solvent, pore former, wetting agent), film casting and drying, and activation.
  • a polymer binder is dissolved in a solvent and then an inorganic absorbent is added in the solution and sufficiently mixed to be dispersed uniformly.
  • the dispersing or mixing step is identical with that in the wet process.
  • a non-solvent is added in an amount range of not causing the precipitation of the polymer binder.
  • the step of film casting is identical with that in the wet process. After the completion of making a film, the resulting electrolyte film is completely dried at 20°C to 200°C to make an electrolyte film.
  • the dry process has the below demerits, it is more preferable to use the wet process than the dry process.
  • the thickness of the film in the present invention is controlled in the range of 20 to 200 ⁇ m. If the thickness of the film is not more than 20 ⁇ m, the mechanical strength decreases and thus it is not preferable. On the contrary, if the thickness of the film exceeds 200 ⁇ m, the ionic conductivity decreases and thus it is not preferable. It is preferable for the electrolyte film of the present invention to have the pore diameter of less than 20 ⁇ m, more preferable less than lO ⁇ m, and further more preferable 0.01 to 5 ⁇ m. It is preferred for the electrolyte film of the present invention to have the porosity of 5 to 95%, more preferable 20 to 90%, and further more preferable 40 to 85%.
  • the liquid electrolyte to be absorbed in the microporous electrolyte film prepared as above can be prepared by dissolving lithium salt in an organic solvent.
  • said organic solvent has high polarity and no reactivity to lithium metal so as to improve the degree of dissociation of ions by raising the polarity of electrolyte and to facilitate ion conduction by lowering local viscosity around ions.
  • organic solvent examples include ethylene carbonate (EC), propylene carbonate (PC), butylenes carbonate (BC), dimethylcarbonate (DMC), diethylcarbonate (DEC), ethylmethylcarbonate (EMC), ⁇ -butyrolactone (GBL), dimethylsulfoxide (DMSO), 1,3-dioxane (DO), tetrahydrofuran (THF), 2-methyltetrahydrofuran, sulfolane, N,N-dimethylformamide (DMF), diglyme (DME), triglyme and tetraglyme.
  • the organic solvent is used in the form of mixed solutions of two or more solvents consisting of high viscosity solvents and low viscosity solvents.
  • Said lithium salt is preferred to have low lattice energy and a high degree of dissociation.
  • examples of such a lithium salt include LiClO , LiBF 4 , LiPF 6 , LiAsF 6 , LiSCN, LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 and LiC(CF 3 SO 2 ) 3 .
  • the selective mixtures thereof can also be used.
  • the concentration of the lithium salt is preferably 0.5M to 2M.
  • the liquid electrolyte can be added in the amount of 20 to 90 % by weight, preferably 40 to 85 % by weight, based on the total amount of electrolytes including the liquid electrolyte.
  • the lithium ion conductivity in the solid electrolyte is from 1 to 3mS/cm at room temperature.
  • the present invention is directed to a rechargeable cell, particularly to a rechargeable lithium cell wherein said porous solid electrolyte is used as an electrolyte.
  • the assembly of a cell is accomplished to bind a cathode and an anode with the inte ⁇ osed electrolyte film, which is made by the above steps, in the manner of lamination, pressing or the like.
  • the cathode and the anode are prepared separately, and the cathode is electrically connected to a cathode current collector, and the anode is electrically connected to an anode current collector.
  • the constructed assembly is activated to be able to absorb the liquid electrolyte, thereby obtaining an electrochemical cell which is ready to operate.
  • an electrolyte film and electrodes (cathode and anode) separately is preferable because the quality control, the process design and the equipment are simple. If necessary, in order to increase the binding ability between the electrode and the electrolyte film and render the thickness of the electrolyte film thinner, a solid electrolyte slurry consisting of an absorbent, a polymer binder, a solvent, etc. may be directly applied on the electrode to form an electrolyte film.
  • the above method is not preferable because it will be hard to adopt the method when the electrode and the electrolyte film do not correspond with each other, or when the electrode or the electrolyte film is easy to pollute or lose their performance in the course of manufacturing process.
  • an electrolyte film is placed between electrodes and then assembled or laminated to a cell by lamination or pressing may be modified in consideration of the performance of cell or the process condition, (i) An electrolyte film is first laminated on one electrode of a cathode and an anode, and then the other electrode is laminated on the other side of the electrolyte film, (ii) Electrolyte films are laminated on the surfaces of a cathode and an anode, respectively, and then the cathode and the anode are laminated at the state that the electrolytes face each other, (iii) A cathode, an electrolyte and an anode are simultaneously laminated in order.
  • the laminating condition so as to minimize the decrease of the electrolyte film within the range of not more than 50% by volume.
  • the volume decrease of the electrolyte film means the destruction of a porous structure, but a little decrease of volume is inevitable for the lamination by heating and or pressing. Therefore, it is advantageous to find the laminating condition capable of minimizing the decrease of volume.
  • the addition of inorganic absorbent over at least 70% by weight which is one of the most important features of the present invention, can minimize such volume decrease.
  • the method may be used to set a temperature and a pressure low as possible and to render the binding between electrodes and an electrolyte film conducted by an adhesive layer.
  • an adhesive layer For example, PE solution/dispersion, efhylene/ethylacrylate-based or ethylene/vinyl acetate- based adhesive, etc can be used.
  • these adhesive components should have the thermal, chemical and electrochemical stability, and the adhesive layer made of them should not destroy the porous structure of surface and not increase the resistance of surface. Therefore, it is not preferable to use the adhesive layer in view of the fabrication of a cell and the control of performance.
  • the procedures for the preparation of the cathode or anode are as follows.
  • the cathode or anode consists of a current collector and an active material layer.
  • the active material layer comprises of active materials, conducting materials and binders, etc.
  • various additives may be introduced in order to improve the performance of cells.
  • the current collectors, conducting materials, binders and additives, which are contained in the cathode or anode, may be identical or different, depending on desired objectives.
  • Each mixture of the cathode or anode materials is kneaded to give slurry.
  • the resulting slurry is made to a thin film by means of casting, coating and screen printing and then the resulting thin film is combined with a current collector by means of pressing or lamination to form a cathode and/or an anode.
  • the slurry may be directly coated on a current collector to form a cathode and/or an anode.
  • The. current collector provides mobile pathways for electrons, which are generated in the oxidation/reduction reaction, taking place in the cathode or the anode.
  • grids, foils, punching foils and etching foils, etc. may be generally used, depending on the performance or manufacturing processes of the cell.
  • the use of grids can increase the loading of the active material, but it may complicate the manufacturing process.
  • the use of foils can improve the performance of the cell and simplify the manufacturing process, but it may deteriorate the compactness of the active materials.
  • Copper, aluminum, nickel, titanium, stainless steel, carbon, etc. can be used as the current collector.
  • aluminum is used for the cathode and copper is used for the anode.
  • the current collector may be conducted, if desired, with the pretreatment such as washing, surface treatment or adhesive layer coating.
  • the active material is the most crucial component of an electrochemical cell since it determines the performance of cell in view of the fact that the charge and discharge reaction (or oxidation/reduction reaction) of cells take place on this material. Furthermore, the active material possesses the largest content in the active material layer. As a cathode active material, it is possible to use transition metal oxides/sulfides, organic compounds, polymer compounds, etc.
  • metal oxides or polymer materials such as lithium cobalt oxide (Li x CoO 2 ), lithium nickel oxide (Li x NiO 2 ), lithium nickel cobalt oxide (Li x NiyCOi.yO ⁇ , spinel type lithium manganese oxide (Li x Mn 2 O 4 ), manganese dioxide (MnO 2 ), etc.
  • anode active material alkali metals, alkali earth metals, carbon, oxide compounds or sulfide compounds of transition metals, organic compounds and polymer compounds may be used, preferably carbon or polymer materials can be used. It is essential that the active materials should be chosen in accordance with the desired performance or use of a cell.
  • the conducting material refers to a material that is added to the cathode or anode in order to improve the electronic conductivity, and is generally carbon.
  • the conducting material is preferably graphite, cokes, activated carbon and carbon black, more preferably graphite and carbon black.
  • One or two or more of conducting materials selected from the above group can be used and there is no difference whether they are synthetic or natural materials.
  • the conducting materials are added in an amount of 3 to 15% by weight based on the total weight of the electrode materials. If the amount of the conducting materials added is not more than 3% by weight, the electrical conductivity falls, causing the problem of over voltage. If the amount exceeds 15% by weight, the energy density per unit volume decreases and the side reaction due to the conducting materials become severe.
  • the binder refers to a component to be added to enhance the binding ability of the active material and is generally a polymer compound.
  • the polymer compounds that are used in the preparation of the solid electrolyte film may serve as binders. It is preferable to use binders, which are the same as polymers of the electrolyte film or have miscibility.
  • the binder may be added in an amount of 15% by weight or less based on the total weight of the electrode materials. If the amount of binder is less than required, the binding ability of the electrodes may decrease. If the amount of binder exceeds 15% by weight, the processability and porosity of the electrodes decrease.
  • the additives refer to materials, which are added to improve the performance of cells or electrodes and can be chosen within a wide range in accordance with desired performances or use.
  • the additives are added to improve the binding ability with composite electrodes inside or current collectors, to induce the porosity or non- crystallinity of the composite electrodes, to improve the dispersibility of the composite electrode constituting materials or the efficiency of the process for the manufacturing of the electrodes, to prohibit the overcharge/overdischarge of the active materials, to recombine or remove the side reaction products, or to improve the absorption ability of the liquid electrolytes.
  • salts, organic/inorganic compounds, minerals and polymer compounds can be used as additives, and absorbents added to the electrolyte film can be chosen.
  • the solid electrolyte according to the present invention and the rechargeable cell using it have the below merits compared to the prior art.
  • the manufacturing process and the requirement of materials are simple.
  • the formation of film is simple and the good porosity can be obtained by a simple method such as the wet process; therefore, it is very simple in comparison with the prior art, i.e., the method of vulcanization, curing or elongation, particularly, the method using plasticizers/processing aids.
  • the electrolyte film according to the present invention has a simple constitution containing the large amount of the inorganic absorbents and the small amount of the polymer binder, and plasticizers/processing aids, curing polymers, crosslinking polymers or fibrous structure materials are not required separately.
  • the performance and stability of the electrolyte is excellent.
  • the ionic conductivity is high because the conduction of ions proceeds via liquid phase impregnated in the porous structure.
  • the content of a polymer is low and the content of an inorganic absorbent is high, thereby (i) the ionic conductivity is not affected by a temperature, (ii) the mechanical, thermal and electrochemical stability is excellent, and (iii) the dimensional stability is good because the volume change is little.
  • the electrolyte according to the present invention has a broad electrochemical potential window and the resistance to ignition and explosion.
  • the inorganic absorbent contained in over the specific amount also works as a structure element, which improves the resistance to lamination or pressing process and thus the performance of electrolyte decreases little even after the assembly of cell.
  • Figure 1 shows graphs demonstrating the experimental results of linear sweep voltammetry to determine the electrochemical stability of the solid electrolyte according to the present invention.
  • Figures 2, 4 and 5 show a variation of discharge capacity of cell in which an inorganic absorbent according to the present invention is used.
  • Figure 3 shows a variation at the thickness and ionic conductivity of the films which were prepared with the different contents of inorganic absorbents, wherein the variation is expressed relatively compared to initial values.
  • the solid electrolyte according to the present invention and the process for the preparation of cells by using said solid electrolyte are explained in detail.
  • the production of the solid electrolyte and the examination of performances were carried out.
  • the solid electrolyte was assembled together with the anode and cathode to form a cell and then the procedure to examine the performance of the cell is described.
  • the present invention is not limited to those examples and various modifications are possible within the scope of the invention.
  • Example 1 Wet process: Experiment according to the kind and amount of inorganic absorbent and the kind of liquid electrolyte
  • ⁇ ab [amount of the liquid electrolyte absorbed (mg)]/[weight of the electrolyte film (mg)]
  • the case that the volumes of solvents comprising liquid electrolytes are not specified means that the solvents are mixed in the same volume.
  • Example 2 (Wet process: Experiments according to the kind of binders) Experiments were conducted by varying the kind of binders in the same manner to Example 1 and the results are summarized in Table 2.
  • the mixed solution thus prepared was coated onto a glass plate in thickness of lOO ⁇ m.
  • the coated film was dried at 40°C for approximately 2 hours, which was further dried for approximately 6 hours in a vacuum drier set to 50°C.
  • the electrolyte film thus prepared was soaked in an EC/DEC IM LiPF 6 solution for approximately 10 minutes. After the liquid electrolyte was completely absorbed, the weight change was determined. ⁇ a b value measured by the use of the weight change was 7.5.
  • the conductivity determined at room temperature by an alternate current impedance method was 2.0 mS/cm.
  • Example 4 Comparative Example: Experiment of preparing solid electrolyte having non-porous structure
  • Example 5 (Experiment of electrochemical stability)
  • the linear sweep voltammetry method was carried out by the use of a stainless steel (#304) as a working electrode and a lithium metal as a counter electrode and a reference electrode.
  • the electrochemical voltage applied in the linear sweep voltammetry was from an open circuit voltage to 5.5V, and the scan rate of the linear sweep voltammetry was lOmV/sec.
  • the results of the linear sweep voltammetry measured on the porous solid electrolyte prepared by the methods of Example l-(h), 1-(1), l-(n) and 2-(s) are shown as A, B, C and D, respectively, in Fig. 1.
  • the solid electrolyte according to the present invention is stable until 4.8V in the electrochemical aspect.
  • synthetic oxide absorbents are more stable than natural mineral absorbents.
  • cells were prepared as the below.
  • a cathode was prepared by mixing an oxide active material, a conducting carbon powder, a polymer binder and additives at the weight ratio of 82:7:8:3 as in a slurry phase, and coating the slurry on an aluminum grid, and then drying it.
  • An anode was prepared by mixing an artificial graphite, a conducting carbon powder, a polymer binder and additives at the weight ratio of 85:3:10:2 as in a slurry phase, and coating the slurry on copper grid, and then drying it.
  • the solid electrolyte refers to the conditions where a liquid electrolyte is absorbed into an electrolyte film.
  • the solid electrolyte obtained in Example 4 was not applied for cell tests.
  • Fig.2 illustrates the discharge capacity with repeated charge and discharge of the cell obtained by the respective examples in comparison with the first discharge capacity. From the test results, it was confirmed that the use of the solid electrolytes (Examples 6- u, v, x) obtained by the wet process (Examples 1 and 2) shows much better cell performances than that of the solid electrolyte (Example 6-w) obtained by the dry process (Example 3). Namely, the solid electrolyte containing inorganic absorbent and prepared by the wet process has a much better effect on the total cell performances (charge and discharge performance, etc.), although the electrolyte film or solid electrolyte itself does not show any significant differences in properties (ionic conductivity, mechanical strength, etc.).
  • Example 7 Example 7 (Experiment of the property according to the amount variation of Paragonite used as an inorganic absorbent)
  • Paragonite powders being the inorganic absorbent as in Example 1 and then pressed by an experimental pressing machine at 130°C during 15 sees with the pressure of 1 metric ton.
  • the change of thickness between before and after pressing was measured and the change of ionic conductivity between before and after pressing was also measured by the use of an alternate current impedance method, the results of which are summarized in Table 4.
  • Fig. 3 shows the results wherein the film thickness and the ionic conductivity after the pressing are expressed as the percentage based upon those before the pressing.
  • the liquid electrolyte used when measuring the ionic conductivity is EC/DMC/DEC IM LiPF 6 . Table 4
  • Example 8 (Experiment of the property according to the amount variation of Zeolite used as an inorganic absorbent) The experiment using Zeolite as an inorganic absorbent was conducted in the same manner as Example 7. The change in the electrolyte film and the ionic conductivity between before and after pressing are summarized in Table 5.
  • Example 7 As the results of Example 7, it is confirmed that, when the content of inorganic absorbent is more than 70% by weight (Example 8-11 and the next thereof), there is little difference between the film thickness and the ionic conductivity after pressing and those before pressing.
  • Example 8-11 and the next thereof When summarizing the results of Example 7 and the present Example, it can be seen that the characteristic phenomenon mentioned above is not largely related to the kind of inorganic materials. It can also be anticipated that, when fabricating cells with those electrolytes by a lamination or a pressing and then measuring the performance of the cells, the distinctive difference depending on the content of inorganic absorbents will be exhibited.
  • Example 9 Example 9 (Experiment of cell performance according to the variation of the kind and content of inorganic absorbent)
  • each of solid electrolytes is in the state that liquid electrolytes are absorbed in electrolyte films.
  • the present invention provides solid electrolytes having a good ionic conductivity by rendering a liquid electrolyte absorbed easily in the electrolyte film wherein an inorganic absorbent is added and the porosity is introduced; methods of preparing those solid electrolytes; and lithium rechargeable cells using the solid electrolytes as an electrolyte.
  • the solid electrolytes according to the present invention have merits in that the manufacturing process and the requirement of materials are simple, the capacity and stability of the electrolyte is good, and the assembly of cell using it is easy.
  • the porosity of the electrolyte film and the ability of absorbing the liquid electrolyte can be maintained at the lamination or pressing process due to the inorganic absorbent added in over the specific amount, whereby the good properties even after the assembly of cell as well as of the solid electrolyte by itself can be maintained.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Dispersion Chemistry (AREA)
  • General Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Secondary Cells (AREA)

Abstract

L'invention concerne un film électrolytique et/ou un électrolyte solide, possédant une structure microporeuse, destiné à une pile rechargeable. Selon l'invention, lors de la préparation du film électrolytique et/ou de l'électrolyte solide, un absorbant minéral est ajouté dans une quantité supérieure à 70 % en poids dans une matrice polymère afin d'empêcher la destruction de la structure poreuse lors du processus d'assemblage de la pile, tel que la lamination ou la mise sous presse, et de conserver la puissance d'absorption d'un électrolyte liquide sur le film électrolytique solide, ainsi que la conductivité ionique. L'absorbant minéral présent dans une certaine quantité, associé à la structure microporeuse, améliore la capacité d'absorption de l'électrolyte liquide et agit, notamment, comme un élément de structure d'augmentation de la résistance mécanique du film électrolytique et/ou de l'électrolyte solide. C'est pourquoi, la bonne conductivité ionique peut être conservée même après assemblage de la pile.
EP00927894A 2000-05-24 2000-05-24 Electrolytes solides mineraux microporeux et procedes de preparation Withdrawn EP1290749A4 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/KR2000/000482 WO2001099220A1 (fr) 2000-05-24 2000-05-24 Electrolytes solides mineraux microporeux et procedes de preparation

Publications (2)

Publication Number Publication Date
EP1290749A1 EP1290749A1 (fr) 2003-03-12
EP1290749A4 true EP1290749A4 (fr) 2004-09-22

Family

ID=19198207

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00927894A Withdrawn EP1290749A4 (fr) 2000-05-24 2000-05-24 Electrolytes solides mineraux microporeux et procedes de preparation

Country Status (4)

Country Link
EP (1) EP1290749A4 (fr)
JP (1) JP2003536233A (fr)
CN (1) CN1452794A (fr)
WO (1) WO2001099220A1 (fr)

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1836266B1 (fr) * 2004-12-03 2017-04-05 ExxonMobil Chemical Patents Inc. Charges stratifiees multicouches modifiees et utilisation dans des compositions nanocomposites
CN101075674B (zh) * 2007-05-28 2010-05-26 哈尔滨工业大学 水为分散剂制备聚环氧乙烯/锂盐/蒙脱土复合电解质的方法
KR101943647B1 (ko) 2009-02-23 2019-01-29 가부시키가이샤 무라타 세이사쿠쇼 비수 전해질 조성물, 비수 전해질 이차 전지 및 비수 전해질 이차 전지의 제조 방법
JP5509618B2 (ja) * 2009-02-23 2014-06-04 ソニー株式会社 非水電解質組成物及び非水電解質二次電池
JP5478473B2 (ja) * 2010-12-10 2014-04-23 トヨタ自動車株式会社 イオン伝導体及びその製造方法、並びに電池及びその製造方法
CN102394313B (zh) * 2011-08-22 2014-03-12 陈兆国 一种复合聚合物电解质
CN103834153A (zh) * 2012-11-27 2014-06-04 海洋王照明科技股份有限公司 凝胶聚合物电解质及其制备方法
JP6303412B2 (ja) * 2013-03-19 2018-04-04 株式会社村田製作所 電池、電解質層、電池パック、電子機器、電動車両、蓄電装置および電力システム
JP2016219134A (ja) * 2015-05-15 2016-12-22 旭化成株式会社 固体電解質
JP6861942B2 (ja) * 2015-08-10 2021-04-21 日本電気硝子株式会社 固体電解質シート及びその製造方法、並びにナトリウムイオン全固体二次電池
WO2017161160A1 (fr) 2016-03-16 2017-09-21 University Of Utah Research Foundation Électrolytes solides composites pour batteries au lithium
CN107474270B (zh) * 2016-06-07 2021-01-12 上海恩捷新材料科技有限公司 一种聚合物电解质膜的制备方法
US11456456B2 (en) 2016-06-23 2022-09-27 United States Of America As Represented By The Secretary Of The Air Force Bendable, creasable, and printable batteries with enhanced safety and high temperature stability—methods of fabrication, and methods of using the same
CN109690862A (zh) * 2016-09-13 2019-04-26 新加坡国立大学 固体电解质
KR101879503B1 (ko) * 2016-09-21 2018-07-18 주식회사 세븐킹에너지 이차 전지용 복합 고체 전해질 및 이의 제조방법
CN106450512A (zh) * 2016-09-29 2017-02-22 清华大学 一种具有分子筛固体电解质层的金属电池
KR101972145B1 (ko) * 2017-09-28 2019-04-24 주식회사 세븐킹에너지 일체형 전고체 이차전지
WO2019161301A1 (fr) * 2018-02-15 2019-08-22 University Of Maryland, College Park Structures électrolytiques à l'état solide poreuses ordonnées, dispositifs électrochimiques comprenant celles-ci, procédés de fabrication de ceux-ci
WO2019212314A1 (fr) * 2018-05-03 2019-11-07 주식회사 엘지화학 Procédé de fabrication de batterie entièrement solide comprenant un électrolyte solide à base de polymère et batterie entièrement solide fabriquée par ce procédé
JP7178347B2 (ja) * 2018-06-12 2022-11-25 アイメック・ヴェーゼットウェー 固体電解質、電極及び蓄電素子
CN109546210B (zh) * 2018-11-14 2020-09-29 山东大学 一种高电压全固态锂电池电解质及其制备方法
CN109935885B (zh) * 2019-01-29 2021-02-09 浙江隆劲电池科技有限公司 一种葡聚糖凝胶界面膜及其制备方法和在固态碱金属/碱土金属电池中的应用
CN109768321A (zh) * 2019-03-22 2019-05-17 广州大学 一种基于铝柱撑黏土的锂电池固态电解质及其制备方法
CN109935894A (zh) * 2019-03-22 2019-06-25 广州大学 一种基于蒙脱土的锂电池固态电解质及其制备方法
CN109962287A (zh) * 2019-03-22 2019-07-02 广州大学 一种钠离子固态电解质及其制备方法
EP3984080A4 (fr) * 2019-06-13 2023-11-01 Ampcera Inc. Membrane électrolytique à l'état solide
CN110265711B (zh) * 2019-07-11 2022-04-15 北京卫蓝新能源科技有限公司 一种固态电解质薄膜及其制备方法和应用
CN110808410B (zh) * 2019-10-10 2022-01-25 武汉瑞科美新能源有限责任公司 一种锂金属电池的固态电解质及其制备方法、应用和锂金属电池
CN111342120B (zh) * 2019-12-14 2021-08-31 武汉瑞科美新能源有限责任公司 聚合物固体电解质、纳米复合隔膜及其制备方法和锂金属电池
KR20210091597A (ko) * 2020-01-14 2021-07-22 주식회사 엘지에너지솔루션 고상-액상 하이브리드 전해질 막을 포함하는 전고체 전지의 제조방법 및 고상-액상 하이브리드 전해질 막
KR20210093797A (ko) * 2020-01-20 2021-07-28 주식회사 엘지에너지솔루션 고상-액상 하이브리드 전해질 막 및 이의 제조방법
CN111682258B (zh) * 2020-07-09 2021-09-03 常州赛得能源科技有限公司 一种介质电解质、锂离子电池及其制备方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994020996A1 (fr) * 1993-03-05 1994-09-15 Bell Communications Research, Inc. Batterie a intercalation au lithium rechargeable avec electrolyte polymere hybride
WO1998013889A1 (fr) * 1996-09-27 1998-04-02 Motorola Inc. Electrolyte polymere solide extremement charge
WO1998018173A1 (fr) * 1996-10-23 1998-04-30 Valence Technology, Inc. Electrolytes solides contenant des agents de renforcement et cellules electrolytiques obtenues a partir de ces electrolytes
WO1998026468A1 (fr) * 1996-12-12 1998-06-18 Valence Technology, Inc. Electrolytes polymeres renfermant des zeolites lithiees
WO2000038262A1 (fr) * 1998-12-22 2000-06-29 Finecell Co., Ltd. Electrolytes solides contenant un absorbant et procedes de preparation de ces derniers

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4812375A (en) * 1988-06-27 1989-03-14 The United States Of America As Represented By The Secretary Of The Army Separator for lithium batteries and lithium batteries including the separator
US5079109A (en) * 1989-05-16 1992-01-07 Kabushiki Kaisha Toshiba Nonaqueous electrolyte secondary battery
US5616437A (en) * 1996-06-14 1997-04-01 Valence Technology, Inc. Conductive metal oxide coated current collector for improved adhesion to composite electrode
JPH10208775A (ja) * 1997-01-24 1998-08-07 Toshiba Battery Co Ltd リチウムポリマー電池用電極要素の製造装置

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994020996A1 (fr) * 1993-03-05 1994-09-15 Bell Communications Research, Inc. Batterie a intercalation au lithium rechargeable avec electrolyte polymere hybride
WO1998013889A1 (fr) * 1996-09-27 1998-04-02 Motorola Inc. Electrolyte polymere solide extremement charge
WO1998018173A1 (fr) * 1996-10-23 1998-04-30 Valence Technology, Inc. Electrolytes solides contenant des agents de renforcement et cellules electrolytiques obtenues a partir de ces electrolytes
WO1998026468A1 (fr) * 1996-12-12 1998-06-18 Valence Technology, Inc. Electrolytes polymeres renfermant des zeolites lithiees
WO2000038262A1 (fr) * 1998-12-22 2000-06-29 Finecell Co., Ltd. Electrolytes solides contenant un absorbant et procedes de preparation de ces derniers

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
CROCE F ET AL: "NANOCOMPOSITE POLYMER ELECTROLYTES FOR LITHIUM BATTERIES", NATURE, MACMILLAN JOURNALS LTD. LONDON, GB, vol. 394, 30 July 1998 (1998-07-30), pages 456 - 458, XP001154504, ISSN: 0028-0836 *
SCROSATI B ET AL: "IMPEDANCE SPECTROSCOPY STUDY OF PEO-BASED NANOCOMPOSITE POLYMER ELECTROLYTES", JOURNAL OF THE ELECTROCHEMICAL SOCIETY, ELECTROCHEMICAL SOCIETY. MANCHESTER, NEW HAMPSHIRE, US, vol. 147, no. 5, 5 May 2000 (2000-05-05), pages 1718 - 1721, XP001051666, ISSN: 0013-4651 *
See also references of WO0199220A1 *

Also Published As

Publication number Publication date
EP1290749A1 (fr) 2003-03-12
CN1452794A (zh) 2003-10-29
JP2003536233A (ja) 2003-12-02
WO2001099220A1 (fr) 2001-12-27

Similar Documents

Publication Publication Date Title
WO2001099220A1 (fr) Electrolytes solides mineraux microporeux et procedes de preparation
EP1171927A1 (fr) Electrolytes solides microporeux et procedes de preparation
JP4884774B2 (ja) 電気化学電池用の電極の製造方法
KR100714135B1 (ko) 전해액용 재료 및 이의 용도
US6395419B1 (en) Solid polymer electrolyte, method of making, and electrochemical device using the same
KR100742959B1 (ko) 유/무기 복합 다공성 필름 및 이를 이용하는 전기 화학소자
JP2007510267A (ja) 高分子が独立的な相にコーティングされた電極及びこれを含む電気化学素子
EP1145354A1 (fr) Electrolytes solides contenant un absorbant et procedes de preparation de ces derniers
KR20030007659A (ko) 미세 다공성 고체 무기전해질 및 그의 제조방법
CN1363124A (zh) 非水电解质二次电池
WO2002061872A1 (fr) Polyelectrolyte multicouche et batterie secondaire au lithium renfermant celui-ci
KR101198672B1 (ko) 이차전지용 전극의 제조방법, 이에 의해 제조되는 이차전지용 전극, 및 이를 포함하는 이차전지
JP3443773B2 (ja) 非水電解質二次電池の製造方法
EP2683008B1 (fr) Électrode positive en trois dimensions pour générateur électrochimique primaire de technologie LiCFx
JP7326477B2 (ja) 固相－液相ハイブリッド電解質膜、その製造方法及びそれを含むリチウム二次電池
WO1997044290A1 (fr) Procedes de fabrication d'electrodes polymeres au lithium de basse impedance
KR19980019330A (ko) 폴리머 전해질이 충전된 전극 및 그의 제조 방법(polymer impregnated electrode and method of making the same)
CN112029212B (zh) 一种含配体修饰的团簇的凝胶聚合物电解质及制备方法
KR100327488B1 (ko) 리튬 고분자 이차전지 제조방법
JP3496287B2 (ja) イオン伝導性高分子化合物を用いた電池
KR100373728B1 (ko) 리튬 2차전지용 전극 활물질 조성물 및 이를 이용하여제조된 리튬 2차 전지
KR20010055897A (ko) 미세 다공성 고체 전해질 및 그의 제조방법
JPH1092416A (ja) 電極とその製法およびそれを用いた電池
KR20010055896A (ko) 이차전지용 고체 전해질 및 그의 제조방법
JPH10106546A (ja) 電池用電極の製造方法

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20021223

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

RIN1 Information on inventor provided before grant (corrected)

Inventor name: KIM, HAN JUN

Inventor name: KIM, SA HEUM

Inventor name: JANG, DONG HUN

RBV Designated contracting states (corrected)

Designated state(s): AT BE CH CY DE FR GB IT LI

A4 Supplementary search report drawn up and despatched

Effective date: 20040811

17Q First examination report despatched

Effective date: 20041230

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20050510