US20170005309A1 - Organic/inorganic composite porous film and electrochemical device prepared thereby - Google Patents

Organic/inorganic composite porous film and electrochemical device prepared thereby Download PDF

Info

Publication number
US20170005309A1
US20170005309A1 US15/266,838 US201615266838A US2017005309A1 US 20170005309 A1 US20170005309 A1 US 20170005309A1 US 201615266838 A US201615266838 A US 201615266838A US 2017005309 A1 US2017005309 A1 US 2017005309A1
Authority
US
United States
Prior art keywords
inorganic particles
organic
porous film
composite porous
inorganic composite
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.)
Abandoned
Application number
US15/266,838
Inventor
Hyun Hang Yong
Sang Young Lee
Seok Koo Kim
Soon Ho AHN
Jung Don Suk
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.)
Toray Battery Separator Film Co Ltd
LG Chem Ltd
Original Assignee
Toray Battery Separator Film Co Ltd
LG Chem 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
Priority claimed from KR1020040070096A external-priority patent/KR100895196B1/en
Priority claimed from KR1020050009999A external-priority patent/KR20060041650A/en
Application filed by Toray Battery Separator Film Co Ltd, LG Chem Ltd filed Critical Toray Battery Separator Film Co Ltd
Priority to US15/266,838 priority Critical patent/US20170005309A1/en
Publication of US20170005309A1 publication Critical patent/US20170005309A1/en
Priority to US15/890,229 priority patent/US20180166671A1/en
Priority to US16/374,483 priority patent/US20190229316A1/en
Priority to US17/358,433 priority patent/US20210320380A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • H01M2/166
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/446Composite material consisting of a mixture of organic and inorganic materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • H01M2/145
    • H01M2/1686
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403Manufacturing processes of separators, membranes or diaphragms
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/451Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/463Separators, membranes or diaphragms characterised by their shape
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/491Porosity
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/497Ionic conductivity
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/60Other road transportation technologies with climate change mitigation effect
    • Y02T10/70Energy storage systems for electromobility, e.g. batteries
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2982Particulate matter [e.g., sphere, flake, etc.]
    • Y10T428/2991Coated
    • Y10T428/2998Coated including synthetic resin or polymer

Definitions

  • the present invention relates to a novel organic/inorganic composite porous film that can show excellent thermal safety and lithium ion conductivity and a high degree of swelling with electrolyte compared to conventional polyolefin-based separators, and an electrochemical device comprising the same, which ensures safety and has improved quality.
  • Secondary batteries are chemical batteries capable of repeated charge and discharge cycles by means of reversible interconversion between chemical energy and electric energy, and may be classified into Ni-MH secondary batteries and lithium secondary batteries.
  • Lithium secondary batteries include lithium secondary metal batteries, lithium secondary ion batteries, lithium secondary polymer batteries, lithium secondary ion polymer batteries, etc.
  • lithium secondary batteries have drive voltage and energy density higher than those of conventional batteries using aqueous electrolytes (such as Ni-MH batteries), they are produced commercially by many production companies. However, most lithium secondary batteries have different safety characteristics depending on several factors. Evaluation of and security in safety of batteries are very important matters to be considered. Therefore, safety of batteries is strictly restricted in terms of ignition and combustion in batteries by safety standards.
  • the first type is a solid composite electrolyte obtained by using inorganic particles having lithium ion conductivity alone or by using inorganic particles having lithium ion conductivity mixed with a polymer matrix. See, Japanese Laid-Open Patent No. 2003-022707, [“Solid State Ionics”-vol. 158, n. 3 , p. 275, (2003)], [“Journal of Power Sources”-vol. 112, n. 1, p.
  • the second type is an electrolyte obtained by mixing inorganic particles having lithium ion conductivity or not with a gel polymer electrolyte formed of a polymer and liquid electrolyte.
  • inorganic materials are introduced in a relatively small amount compared to the polymer and liquid electrolyte, and thus merely have a supplementary function to assist in lithium ion conduction made by the liquid electrolyte.
  • electrolytes prepared as described above have no pores therein or, if any, have pores with a size of several angstroms and low porosity, formed by introduction of an artificial plasticizer, the electrolytes cannot serve sufficiently as separator, resulting in degradation in the battery quality.
  • FIG. 1 is a schematic view showing an organic/inorganic composite porous film according to the present invention
  • FIG. 2 is a photograph taken by Scanning Electron Microscope (SEM) showing the organic/inorganic composite porous film (PVdF-HFP/BaTiO 3 ) according to Example 1;
  • FIG. 3 is a photograph taken by SEM showing a polyolefin-based separator (PP/PE/PP) used in Comparative Example 1;
  • FIG. 4 is a photograph taken by SEM showing a porous film manufactured by using a plasticizer according to Comparative Example 4;
  • FIG. 5 is a photograph showing the organic/inorganic composite porous film (PVdF-HFP/BaTiO 3 ) according to Example 1 compared to a currently used PP/PE/PP separator and PE separator, after each of the samples is maintained at 150 °C. for 1 hour;
  • FIG. 6 is a picture showing the results of an overcharge test for the lithium secondary battery including a currently used PP/PE/PP separator according to Comparative Example 1 and the battery including the organic/inorganic composite porous film (PVdF-HFP/BaTiO 3 ) according to Example 1; and
  • FIG. 7 is a graph showing variations in ion conductivity depending on the content of inorganic particles, in the organic/inorganic composite porous film according to the present invention.
  • an organic/inorganic composite porous film formed by using (1) inorganic particles and (2) a binder polymer, improves poor thermal safety of a conventional polyolefin-based separator. Additionally, we have found that because the organic/inorganic composite porous film has a micropore structure formed by the inorganic particles present in the film, it provides an increased volume of space into which a liquid electrolyte infiltrates, resulting in improvements in lithium ion conductivity and degree of swelling with electrolyte. Therefore, the organic/inorganic composite porous film can improve the quality and safety of an electrochemical device using the same as separator.
  • an object of the present invention to provide an organic/inorganic composite porous film capable of improving the quality and safety of an electrochemical device, a method for manufacturing the same and an electrochemical device comprising the same.
  • an organic/inorganic composite porous film which comprises (a) inorganic particles; and (b) a binder polymer coating layer formed partially or totally on the surface of the inorganic particles, wherein the inorganic particles are interconnected among themselves and are fixed by the binder polymer, and interstitial volumes among the inorganic particles form a micropore structure.
  • an electrochemical device preferably, a lithium secondary battery comprising the same.
  • a method for manufacturing an organic/inorganic composite porous film which includes the steps of: (a) dissolving a binder polymer into a solvent to form a polymer solution; (b) adding inorganic particles to the polymer solution obtained from step (a) and mixing them; and (c) coating the mixture of inorganic particles with binder polymer obtained from step (b) on a substrate, followed by drying, and then detaching the substrate.
  • the present invention is characterized in that it provides a novel organic/inorganic composite porous film, which serves sufficiently as separator to prevent electrical contact between a cathode and an anode of a battery and to pass ions therethrough and shows excellent thermal safety, lithium ion conductivity and degree of swelling with electrolyte.
  • the organic/inorganic composite porous film is obtained by using inorganic particles and a binder polymer.
  • the uniform and heat resistant micropore structure formed by the interstitial volumes among the inorganic particles permits the organic/inorganic composite porous film to be used as separator. Additionally, if a polymer capable of being gelled when swelled with a liquid electrolyte is used as the binder polymer component, the organic/inorganic composite porous film can serve also as electrolyte.
  • the organic/inorganic composite porous film according to the present invention shows improved thermal safety by virtue of the inorganic particles present therein.
  • the organic/inorganic composite porous film according to the present invention has uniform micropore structures formed by the interstitial volumes among the inorganic particles as shown in FIGS. 1 and 2 , and the micropore structures permit lithium ions to move smoothly therethrough. Therefore, it is possible to introduce a large amount of electrolyte through the micropore structures so that a high degree of swelling with electrolyte can be obtained, resulting in improvement in the quality of a battery.
  • the inorganic particles used in the organic/inorganic composite porous film have a high dielectric constant and/or lithium ion conductivity, the inorganic particles can improve lithium ion conductivity as well as heat resistance, thereby contributing to improvement of battery quality.
  • the organic/inorganic composite porous film according to the present invention can improve the quality of an electrochemical device compared to conventional organic/inorganic composite electrolytes. Additionally, the organic/inorganic composite porous film provides advantages in that wettablity with an electrolyte is improved compared to conventional hydrophobic polyolefin-based separators, and use of a polar electrolyte for battery is permitted.
  • the binder polymer is one capable of being gelled when swelled with electrolyte, the polymer reacts with the electrolyte injected subsequently and is gelled, thereby forming a gel type organic/inorganic composite electrolyte.
  • electrolytes are produced with ease compared to conventional gel-type electrolytes and show excellent ion conductivity and a high degree of swelling with electrolyte, thereby contributing to improve the quality of a battery.
  • One component present in the organic/inorganic composite porous film according to the present invention is inorganic particles currently used in the art.
  • the inorganic particles permit interstitial volumes to be formed among them, thereby serving to form micropores and to maintain the physical shape as spacer. Additionally, because the inorganic particles are characterized in that their physical properties are not changed even at a high temperature of 200 °C. or higher, the organic/inorganic composite porous film using the inorganic particles can have excellent heat resistance.
  • inorganic particles there is no particular limitation in selection of inorganic particles, as long as they are electrochemically stable.
  • inorganic particles that may be used in the present invention, as long as they are not subjected to oxidation and/or reduction at the range of drive voltages (for example, 0-5 V based on Li/Li + ) of a battery, to which they are applied.
  • drive voltages for example, 0-5 V based on Li/Li +
  • inorganic particles having a high density are used, they have a difficulty in dispersion during a coating step and may increase the weight of a battery to be manufactured.
  • inorganic particles having a density as low as possible. Further, when inorganic particles having a high dielectric constant are used, they can contribute to increase the dissociation degree of an electrolyte salt in a liquid electrolyte, such as a lithium salt, thereby improving the ion conductivity of the electrolyte.
  • inorganic particles having a dielectric constant of 5 or more include BaTiO 3 , Pb(Zr,Ti) O 3 (PZT) , Pb 1-x La x Zr 1-y Ti y O 3 (PLZT), PB(Mg 3 Nb 2/3 )O 3 —PbTiO 3 (PMN-PT), hafnia (HfO 2 ), SrTiO 3 , SnO 2 , CeO 2 , MgO, NiO, CaO, ZnO, ZrO 2 , Y 2 O 3 , Al 2 O 3 , TiO 2 , SiC or mixtures thereof.
  • inorganic particles having lithium ion conductivity are referred to as inorganic particles containing lithium elements and having a capability of conducting lithium ions without storing lithium. Inorganic particles having lithium ion conductivity can conduct and move lithium ions due to defects present in their structure, and thus can improve lithium ion conductivity and contribute to improve battery quality.
  • Non-limiting examples of such inorganic particles having lithium ion conductivity include: lithim phosphate (Li 3 PO 4 ), lithium titanium phosphate (Li x Ti y (PO 4 ) 3 , 0 ⁇ x ⁇ 2, 0 ⁇ y ⁇ 3), lithium aluminum titanium phosphate (Li x Al y Ti z (PO 4 ) 3 , 0 ⁇ x ⁇ 2, 0 ⁇ y ⁇ 1, 0 ⁇ z ⁇ 3), (LiAlTiP) x O y type glass (0 ⁇ x ⁇ 4, 0 ⁇ y ⁇ 13) such as 14Li 2 O-9Al 2 O 3 -38TiO 2 -39P 2 O 5 , lithium lanthanum titanate (Li x La y TiO 3 , 0 ⁇ y ⁇ 3), lithium germanium thiophosphate (Li x Ge y P z S w , 0 ⁇ x ⁇ 4, 0 ⁇ y ⁇ 1, 0 ⁇ z ⁇ 1, 0 ⁇ w ⁇ 5), such as Li 3.25 Ge 0.25 P 0.75
  • inorganic particles having a relatively high dielectric constant are used instead of inorganic particles having no reactivity or having relatively low dielectric constant. Further, the present invention also provides a novel use of inorganic particles as separators.
  • the above-described inorganic particles that have never been used as separators, for example Pb(Zr,Ti) O 3 (PZT), Pb 1-x La x Zr 1-y Ti y O 3 (PLZT), Pb(Mg 3 Nb 2/3 ) O 3 —PbTiO 3 (PMN-PT), hafnia (HfO 2 ), etc., have a high dielectric constant of 100 or more.
  • the inorganic particles also have piezoelectricity so that an electric potential can be generated between both surfaces by the charge formation, when they are drawn or compressed under the application of a certain pressure. Therefore, the inorganic particles can prevent internal short circuit between both electrodes, thereby contributing to improve the safety of a battery. Additionally, when such inorganic particles having a high dielectric constant are combined with inorganic particles having lithium ion conductivity, synergic effects can be obtained.
  • the organic/inorganic composite porous film according to the present invention can form pores having a size of several micrometers by controlling the size of inorganic particles, content of inorganic particles and the mixing ratio of inorganic particles and binder polymer. It is also possible to control the pore size and porosity.
  • inorganic particles preferably have a size of 0.001-10 ⁇ m for the purpose of forming a film having a uniform thickness and providing a suitable porosity.
  • size is less than 0.001 ⁇ m, inorganic particles have poor dispersibility so that physical properties of the organic/inorganic composite porous film cannot be controlled with ease.
  • size is greater than 10 ⁇ m, the resultant organic/inorganic composite porous film has an increased thickness under the same solid content, resulting in degradation in mechanical properties. Furthermore, such excessively large pores may increase a possibility of internal short circuit being generated during repeated charge/discharge cycles.
  • the inorganic particles are present in the mixture of the inorganic particles with binder polymer forming the organic/inorganic composite porous film, preferably in an amount of 50-99 wt. %, more particularly in an amount of 60-95 wt. % based on 100 wt. % of the total weight of the mixture.
  • the binder polymer is present in such a large amount as to decrease the interstitial volume formed among the inorganic particles and thus to decrease the pore size and porosity, resulting in degradation in the quality of a battery.
  • the content of the inorganic particles is greater than 99 wt. %, the polymer content is too low to provide sufficient adhesion among the inorganic particles, resulting in degradation in mechanical properties of a finally formed organic/inorganic composite porous film.
  • the binder polymer preferably has a glass transition temperature (T g ) as low as possible, more preferably T g of between ⁇ 200 °C. and 200 °C. Binder polymers having a low Tg as described above are preferable, because they can improve mechanical properties such as flexibility and elasticity of a finally formed film.
  • the polymer serves as binder that interconnects and stably fixes the inorganic particles among themselves, and thus prevents degradation in mechanical properties of a finally formed organic/inorganic composite porous film.
  • the binder polymer When the binder polymer has ion conductivity, it can further improve the quality of an electrochemical device. However, it is not essential to use a binder polymer having ion conductivity. Therefore, the binder polymer preferably has a dielectric constant as high as possible. Because the dissociation degree of a salt in an electrolyte depends on the dielectric constant of a solvent used in the electrolyte, the polymer having a higher dielectric constant can increase the dissociation degree of a salt in the electrolyte used in the present invention.
  • the dielectric constant of the polymer may range from 1.0 to 100 (as measured at a frequency of 1 kHz), and is preferably 10 or more.
  • the binder polymer used in the present invention may be further characterized in that it is gelled when swelled with a liquid electrolyte, and thus shows a high degree of swelling. Therefore, it is preferable to use a polymer having a solubility parameter of between 15 and 45 MPa 1/2 , more preferably of between 15 and 25 MPa 1/2 , and between 30 and 45 MPa 1/2 . Therefore, hydrophilic polymers having a lot of polar groups are more preferable than hydrophobic polymers such as polyolefins. When the binder polymer has a solubility parameter of less than 15 Mpa 1/2 or greater than 45 Mpa 1/2 , it has difficulty in swelling with a conventional liquid electrolyte for battery.
  • Non-limiting examples of the binder polymer that may be used in the present invention include polyvinylidene fluoride-co-hexafluoropropylene, polyvinylidene fluoride-co-trichloroethylene, polymethylmethacrylate, polyacrylonitrile, polyvinylpyrrolidone, polyvinyl acetate, polyethylene-co-vinyl acetate, polyethylene oxide, cellulose acetate, cellulose acetate butyrate, cellulose acetate propionate, cyanoethylpullulan, cyanoethyl polyvinylalcohol, cyanoethylcellulose, cyanoethylsucrose, pullulan, carboxymetyl cellulose, acrylonitrile-styrene-butadiene copolymer, polyimide or mixtures thereof.
  • Other materials may be used alone or in combination, as long as they satisfy the above characteristics.
  • the organic/inorganic composite porous film may further comprise additives other than the inorganic particles and binder polymer.
  • the film When the organic/inorganic composite porous film is manufactured by using inorganic particles and a binder polymer, the film may be realized by three types of embodiments, but is not limited thereto.
  • the first type is an organic/inorganic composite porous film formed by using a mixture of inorganic particles and binder polymer with no additional substrate.
  • the second type is an organic/inorganic composite porous film formed by coating the mixture on a porous substrate having pores, wherein the film coated on the porous substrate includes an active layer obtained by coating the mixture of inorganic particles and binder polymer on the surface of the porous substrate or on a part of the pores in the substrate.
  • the third type is an organic/inorganic composite porous film formed by coating the mixture on a cathode and/or an anode.
  • the third type is a monolithic electrode and film.
  • the substrate coated with the mixture of inorganic particles and binder polymer there is no particular limitation in the substrate coated with the mixture of inorganic particles and binder polymer, as long as it is a porous substrate having pores.
  • a heat resistant porous substrate having a melting point of 200 °C. or higher can improve the thermal safety of the organic/inorganic composite porous film under external and/or internal thermal impacts.
  • polyethylene terephthalate polybutylene terephthalate
  • polyester polyacetal
  • polyamide polycarbonate
  • polyimide polyetherether ketone
  • polyether sulfone polyphenylene oxide
  • polyphenylene sulfidro polyethylene naphthalene or mixtures thereof.
  • other heat resistant engineering plastics may be used with no particular limitation.
  • the porous substrate preferably has a thickness of between 1 ⁇ m and 100 ⁇ m, more preferably of between 5 ⁇ m and 50 ⁇ m.
  • the porous substrate has a thickness of less than 1 ⁇ m, it is difficult to maintain mechanical properties.
  • the porous substrate has a thickness of greater than 100 ⁇ m, it may function as resistance layer.
  • the porous substrate preferably has a porosity of between 5% and 95%.
  • the pore size (diameter) preferably ranges from 0.01 ⁇ m to 50 ⁇ m, more preferably from 0.1 ⁇ m to 20 ⁇ m.
  • the porous substrate may function as resistance layer.
  • the pore size and porosity are greater than 50 ⁇ m and 95%, respectively, it is difficult to maintain mechanical properties.
  • the porous substrate may take the form of a membrane or fiber.
  • the porous substrate may be a nonwoven web forming a porous web (preferably, spunbond type web comprising long fibers or melt blown type web).
  • a spunbond process is performed continuously through a series of steps and provides long fibers formed by heating and melting, which is stretched, in turn, by hot air to form a web.
  • a melt blown process performs spinning of a polymer capable of forming fibers through a spinneret having several hundreds of small orifices, and thus provides three-dimensional fibers having a spider-web structure resulting from interconnection of microfibers having a diameter of 10 ⁇ m or less.
  • the organic/inorganic composite porous film that may be formed in various types of embodiments according to the present invention is characterized in that the film comprises a micropore structure.
  • the organic/inorganic composite porous film formed by using the mixture of inorganic particles and polymer alone has a micropore structure formed by interstitial volumes among the inorganic particles serving as support as well as spacer.
  • the organic/inorganic composite porous film formed by coating the mixture on a porous substrate has pore structures present both in the substrate and in the active layer due to the pores present in the porous substrate itself and interstitial volumes among the inorganic particles in the active layer formed on the substrate.
  • the organic/inorganic composite porous film obtained by coating the mixture on the surface of an electrode has a uniform pore structure formed by interstitial volumes among the inorganic particles in the same manner as the pore structure formed by electrode active material particles in the electrode. Therefore, any embodiment of the organic/inorganic composite porous film according to the present invention has an increased volume of space, into which an electrolyte infiltrates, by virtue of such micropore structures. As a result, it is possible to increase dispersibility and conductivity of lithium ions, resulting in improvement in the quality of a battery.
  • the pore size and porosity of the organic/inorganic composite porous film mainly depend on the size of inorganic particles. For example, when inorganic particles having a particle diameter of 1 ⁇ m or less are used, pores formed thereby also have a size of 1 ⁇ m or less.
  • the pore structure is filled with an electrolyte injected subsequently and the electrolyte serves to conduct ions. Therefore, the size and porosity of the pores are important factors in controlling the ion conductivity of the organic/inorganic composite porous film.
  • the pores size and porosity of the organic/inorganic composite porous film according to the present invention range from 0.01 to 10 ⁇ m and from 5 to 95%, respectively.
  • the thickness of the organic/inorganic composite porous film according to the present invention may be controlled depending on the quality of a battery.
  • the film preferably has a thickness of between 1 and 100 ⁇ m, more preferably of between 2 and 30 ⁇ m. Control of the thickness of the film may contribute to improve the quality of a battery.
  • mixing ratio of inorganic particles to polymer in the organic/inorganic composite porous film according to the present invention can be controlled according to the thickness and structure of a film to be formed finally.
  • the organic/inorganic composite porous film may be applied to a battery together with a microporous separator (for example, a polyolefin-based separator), depending on the characteristics of a finally formed battery.
  • a microporous separator for example, a polyolefin-based separator
  • the organic/inorganic composite porous film may be manufactured by a conventional process known to one skilled in the art.
  • One embodiment of a method for manufacturing the organic/inorganic composite porous film according to the present invention includes the steps of: (a) dissolving a binder polymer into a solvent to form a polymer solution; (b) adding inorganic particles to the polymer solution obtained from step (a) and mixing them; and (c) coating the mixture obtained from step (b) on the surface of a substrate, followed by drying, and then detaching the substrate.
  • a binder polymer is dissolved in a suitable organic solvent to provide a polymer solution.
  • the solvent has a solubility parameter similar to that of the binder polymer to be used and a low boiling point.
  • solvents can be mixed uniformly with the polymer and can be removed easily after coating the polymer.
  • Non-limiting examples of the solvent that may be used include acetone, tetrahydrofuran, methylene chloride, chloroform, dimethylformamide, N-methyl-2-pyrrolidone (NMP), cyclohexane, water and mixtures thereof.
  • inorganic particles are added to and dispersed in the polymer solution obtained from the preceding step to provide a mixture of inorganic particles with binder polymer.
  • the time needed for pulverization is suitably 1-20 hours.
  • the particle size of the pulverized particles ranges preferably from 0.001 and 10 ⁇ m. Conventional pulverization methods, preferably a method using a ball mill may be used.
  • composition of the mixture containing inorganic particles and binder polymer can contribute to control the thickness, pore size and porosity of the organic/inorganic composite porous film to be formed finally.
  • the weight ratio (I/P) of the inorganic particles (I) to the polymer (P) increases. Therefore, the thickness of the organic/inorganic composite porous film increases under the same solid content (weight of the inorganic particles weight of the binder polymer). Additionally, the pore size increases in proportion to the pore formation among the inorganic particles. When the size (particle diameter) of inorganic particles increases, interstitial distance among the inorganic particles also increases, thereby increasing the pore size.
  • Particular examples of the substrate that may be used include Teflon sheets or the like generally used in the art, but are not limited thereto.
  • any methods known to one skilled in the art may be used. It is possible to use various processes including dip coating, die coating, roll coating, comma coating or combinations thereof.
  • the substrate is a porous substrate having pores or a preformed electrode
  • various types of organic/inorganic composite porous films can be obtained.
  • the mixture of inorganic particles and polymer may be coated on the surface of porous substrate, on the surface of electrode, and on a part of the pores present in the substrate.
  • the step of detaching a substrate may be omitted.
  • the organic/inorganic composite porous film according to the present invention obtained as described above, may be used as separator in an electrochemical device, preferably in a lithium secondary battery. Additionally, the organic/inorganic composite porous film may be coated with a conventional polymer (for example, a polymer capable of being swelled with an electrolyte) on one surface or both surfaces so as to be used as separator.
  • a conventional polymer for example, a polymer capable of being swelled with an electrolyte
  • the binder polymer used in the film is a polymer capable of being gelled when swelled with a liquid electrolyte
  • the polymer may react with the electrolyte injected after assembling a battery by using the separator, and thus be gelled to form a gel type organic/inorganic composite electrolyte.
  • the gel type organic/inorganic composite electrolyte according to the present invention is prepared with ease compared to gel type polymer electrolytes according to the prior art, and has a large space to be filled with a liquid electrolyte due to its microporous structure, thereby showing excellent ion conductivity and a high degree of swelling with electrolyte, resulting in improvement in the quality of a battery.
  • the present invention provides an electrochemical device comprising: (a) a cathode; (b) an anode; (c) the organic/inorganic composite porous film according to the present invention, interposed between the cathode and anode; and (d) an electrolyte.
  • Such electrochemical devices include any devices in which electrochemical reactions occur and particular examples thereof include all kinds of primary batteries, secondary batteries, fuel cells, solar cells or capacitors.
  • the electrochemical device is a lithium secondary battery including a lithium secondary metal battery, lithium secondary ion battery, lithium secondary polymer battery or lithium secondary ion polymer battery.
  • the organic/inorganic composite porous film contained in the electrochemical device serves as separator. If the polymer used in the film is a polymer capable of being gelled when swelled with electrolyte, the film may serve also as electrolyte.
  • a microporous separator may also be used.
  • the microporous separator includes currently used polyolefin-based separators or at least one porous substrate having a melting point of 200° C., selected from the group consisting of polyethylene terephthalate, polybutylene terephthalate, polyester, polyacetal, polyamide, polycarbonate, polyimide, polyetherether ketone, polyether sulfone, polyphenylene oxide, polyphenylene sulfidro and polyethylene naphthalene.
  • the electrochemical device may be manufactured by a conventional method known to one skilled in the art.
  • the electrochemical device is assembled by using the organic/inorganic composite porous film interposed between a cathode and an anode, and then an electrolyte is injected.
  • the electrode that may be applied together with the organic/inorganic composite porous film according to the present invention may be formed by applying an electrode active material on a current collector according to a method known to one skilled in the art.
  • cathode active materials may include any conventional cathode active materials currently used in a cathode of a conventional electrochemical device.
  • the cathode active material include lithium intercalation materials such as lithium manganese oxides, lithium cobalt oxides, lithium nickel oxides, lithium iron oxides or composite oxides thereof.
  • anode active materials may include any conventional anode active materials currently used in an anode of a conventional electrochemical device.
  • anode active material include lithium intercalation materials such as lithium metal, lithium alloys, carbon, petroleum coke, activated carbon, graphite or other carbonaceous materials.
  • Non-limiting examples of a cathode current collector include foil formed of aluminum, nickel or a combination thereof.
  • Non-limiting examples of an anode current collector include foil formed of copper, gold, nickel, copper alloys or a combination thereof.
  • the electrolyte that may be used in the present invention includes a salt represented by the formula of A + B ⁇ , wherein A + represents an alkali metal cation selected from the group consisting of Li + , Na + , K + and combinations thereof, and B ⁇ represents an anion selected from the group consisting of PF 6 ⁇ , BF 4 ⁇ , Cl ⁇ , Br ⁇ , I ⁇ , ClO 4 ⁇ , AsF 6 ⁇ , CH 3 CO 2 ⁇ , CF 3 SO 3 ⁇ , N (CF 3 SO 2 ) 2 ⁇ , C (CF 2 SO 2 ) 3 ⁇ and combinations thereof, the salt being dissolved or dissociated in an organic solvent selected from the group consisting of propylene carbonate (PC), ethylene carbonate (EC), diethyl carbonate (DEC), dimethyl carbonate (DMC), dipropyl carbonate (DPC), dimethyl sulfoxide, acetonitrile, dimethoxyethane, dieth
  • the electrolyte may be injected in a suitable step during the manufacturing process of an electrochemical device, according to the manufacturing process and desired properties of a final product.
  • electrolyte may be injected, before an electrochemical device is assembled or in a final step during the assemblage of an electrochemical device.
  • Processes that may be used for applying the organic/inorganic composite porous film to a battery include not only a conventional winding process but also a lamination (stacking) and folding process of a separator and electrode.
  • the organic/inorganic composite porous film according to the present invention When the organic/inorganic composite porous film according to the present invention is applied to a lamination process, it is possible to significantly improve the thermal safety of a battery, because a battery formed by a lamination and folding process generally shows more severe heat shrinking of a separator compared to a battery formed by a winding process. Additionally, when a lamination process is used, there is an advantage in that a battery can be assembled with ease by virtue of excellent adhesion of the polymer present in the organic/inorganic composite porous film according to the present invention. In this case, the adhesion can be controlled depending on the content of inorganic particles and polymer, and properties of the polymer. More particularly, as the polarity of the polymer increases and as the glass transition temperature (T g ) or melting point (T m ) of the polymer decreases, higher adhesion between the organic/inorganic composite porous film and electrode can be obtained.
  • T g glass transition temperature
  • T m melting
  • the organic/inorganic composite system according to the present invention was observed to determine variations in ion conductivity depending on the content of inorganic particles.
  • the film, into which the electrolyte is impregnated, was measured for ion conductivity by using Metrohm 712 instrument at a temperature of 25° C.
  • PVdF-HFP polymer polyvinylidene fluoride-hexafluoropropylene copolymer
  • THF tetrahydrofuran
  • the mixed solution obtained as described above was coated on a Teflon sheet by using a doctor blade coating method. After coating, THF was dried and the Teflon sheet was detached to obtain a final organic/inorganic composite porous film (see, FIG. 1 ).
  • the final film had a thickness of about 30 ⁇ m. After measuring with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.4 ⁇ m and a porosity of 60%.
  • NMP N-methyl-2-pyrrolidone
  • LiCoO 2 lithium cobalt composite oxide
  • carbon black carbon black
  • PVdF polyvinylidene fluoride
  • NMP N-methyl-2-pyrrolidone
  • carbon powder As anode active material
  • 1 wt. % of carbon black as conductive agent
  • the slurry was coated on Cu foil having a thickness of 10 ⁇ m as anode collector and dried to form an anode.
  • EC ethylene carbonate
  • PC propylene carbonate
  • DEC diethyl carbonate
  • Example 1 was repeated to provide a lithium secondary battery, except that PMNPT(lead magnesium niobate-lead titanate) powder was used instead of BaTiO 3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PMNPT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 30 ⁇ m, pore size of 0.3 ⁇ m and a porosity of 60%.
  • PMNPT lead magnesium niobate-lead titanate
  • Example 1 was repeated to provide a lithium secondary battery, except that PVdF-HFP was not used but about 2 wt. % of carboxymethyl cellulose (CMC) polymer was added to water and dissolved therein at 60° C. for about 12 hours or more to form a polymer solution, and the polymer solution was used to obtain an organic/inorganic composite porous film (CMC/BaTiO 3 ). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 ⁇ m, pore size of 0.4 ⁇ m and a porosity of 58%.
  • CMC carboxymethyl cellulose
  • Example 1 was repeated to provide a lithium secondary battery, except that PZT powder was used instead of BaTiO 3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PZT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 ⁇ m, pore size of 0.4 ⁇ m and a porosity of 62%.
  • Example 1 was repeated to provide a lithium secondary battery, except that PLZT powder was used instead of BaTiO 3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PLZT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 tin, pore size of 0.3 ⁇ m and a porosity of 58%.
  • Example 1 was repeated to provide a lithium secondary battery, except that HfO 2 powder was used instead of BaTiO 3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/HfO 2 ). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 28 ⁇ m, pore size of 0.4 ⁇ m and a porosity of 60%.
  • Example 1 was repeated to provide a lithium secondary battery, except that lithium titanium phosphate (LiTi 2 (PO 4 ) 3 ) powder having a particle diameter of about 400 nm was used in an amount of the total solid content of 20 wt. %, instead of BaTiO 3 powder, to obtain an organic/inorganic composite porous film (PVdF-HFP/LiTi 2 (PO 4 ) 3 ) having a thickness of about 20 ⁇ m. After measuring with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.5 ⁇ m and porosity of 62%.
  • lithium titanium phosphate (LiTi 2 (PO 4 ) 3 ) powder having a particle diameter of about 400 nm was used in an amount of the total solid content of 20 wt. %, instead of BaTiO 3 powder, to obtain an organic/inorganic composite porous film (PVdF-HFP/LiTi 2 (PO 4 ) 3 )
  • Example 1 was repeated to provide a lithium secondary battery, except that a conventional poly propylene/polyethylene/polypropylene (PP/PE/PP) separator (see, FIG. 3 ) was used.
  • PP/PE/PP poly propylene/polyethylene/polypropylene
  • Example 1 was repeated to provide an organic/inorganic composite porous film and lithium secondary battery comprising the same, except that BaTiO 3 and PVDF-HFP were used in a weight ratio of 20:80. After measuring the BaTiO 3 /PVdF-HFP with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.01 ⁇ m or less and a porosity of about 10%.
  • Example 1 was repeated to provide an organic/inorganic composite porous film and lithium secondary battery comprising the same, except that LiTi 2 (PO 4 ) 3 and PVDF-HFP were used in a weight ratio of 10:90.
  • the final organic/inorganic composite porous film had a pore size of 0.01 ⁇ m or less and a porosity of about 5%.
  • Dimethyl carbonate (DMC) was selected as plasticizer and used along with PVdF-HFP in a ratio of 30:70 (on the wt. % basis) and THF as solvent to form a porous film.
  • Dimetyl carbonate used in the film as plasticizer was extracted from the film by using methanol to provide a final porous film and a lithium secondary battery comprising the same.
  • the porous film After measuring the porous PVdF-HFP film with a porosimeter, the porous film had a pore size of 0.01 ⁇ m or less and a porosity of about 30% (see, FIG. 4 ).
  • the sample used in this test was PVdF-HFP/BaTiO 3 obtained according to Example 1.
  • a PP/PE/PP separator according to Comparative Example 1 and the porous film using a plasticizer according to Comparative Example 4 were used.
  • the PP/PE/PP separator according to Comparative Example 1 and the porous film according to Comparative Example 4 showed a conventional microporous structure (see, FIGS. 3 and 4 ). More particularly, the porous film according to Comparative Example 4 had a dense pore structure formed independently from the inorganic particles present on the surface of the film. It is thought that the dense pore structure is formed by artificial extraction of the plasticizer.
  • the organic/inorganic composite porous film according to the present invention showed a micropore structure formed by the inorganic particles as main component of the film (for example, inorganic particles with a high dielectric constant and/or lithium ion conductivity). Additionally, it could be seen that the polymer was coated on the surface of the inorganic particles (see, FIG. 2 ).
  • the organic/inorganic composite porous film (PVdF-CTFE/BaTiO 3 ) according to Example 1 was used as sample.
  • a conventional PP/PE/PP separator and PE separator were used as controls.
  • test samples were checked for its heat shrinkage after stored at a high temperature of 150° C. for hour.
  • the test samples provided different results after the lapse of 1 hour at 150° C.
  • the PP/PE/PP separator as control was shrunk due to high temperature to leave only the outer shape thereof.
  • the PE separator was shrunk to about 1/10 of its original size.
  • the organic/inorganic composite porous film according to the present invention showed good results with no heat shrinkage (see, FIG. 5 )
  • the organic/inorganic composite porous film according to the present invention has excellent thermal safety.
  • the lithium secondary battery comprising an organic/inorganic composite porous film according to the present invention has excellent thermal safety.
  • each lithium secondary battery comprising an organic/inorganic composite porous film according to the present invention showed excellent safety under overcharge conditions (see, Table 2 and FIG. 6 ).
  • Each battery having a capacity of 760 mAh was subjected to cycling at a discharge rate of 0.5C, 10 and 2C.
  • the following Table 3 shows the discharge capacity of each battery, the capacity being expressed on the basis of C-rate characteristics.
  • lithium secondary batteries comprising the organic/inorganic composite porous film according to the present invention showed C-rate characteristics comparable to those of the battery using a conventional polyolefin-based separator under a discharge rate of up to 2C (see, Table 3).
  • the organic/inorganic composite porous film according to the present invention comprises inorganic particles and a binder polymer, wherein the inorganic particles are interconnected among themselves and fixed by the binder polymer and interstitial volumes among the inorganic particles form a heat resistant micropore structure. Therefore, it is possible to increase the space to be filled with an electrolyte, and thus to improve a degree of swelling with electrolyte and lithium ion conductivity. As a result, the organic/inorganic composite porous film according to the present invention contributes to improve the thermal safety and quality of a lithium secondary battery using the same as separator.

Abstract

Disclosed is an organic/inorganic composite porous film comprising: (a) inorganic particles; and (b) a binder polymer coating layer formed partially or totally on surfaces of the inorganic particles, wherein the inorganic particles are interconnected among themselves and are fixed by the binder polymer, and interstitial volumes among the inorganic particles form a micropore structure. A method for manufacturing the same film and an electrochemical device including the same film are also disclosed. An electrochemical device comprising the organic/inorganic composite porous film shows improved safety and quality.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • This application is a Continuation Application of co-pending U.S. application Ser. No.: 13/785,260 filed on Mar. 5, 2013, which is a Continuation of U.S. application Ser. No. : 11/217,918 filed on Sep. 1, 2005 (now U.S. Pat. No.: 8,409,746 issued on Apr. 2, 2013), which claims priority under 35 U.S.C. 119 (a) to Patent Application Nos. 10-2004-70095, 10-2004-70096, and 10-2005-9999 filed in the Republic of Korea on Sep. 2, 2004, Sep. 2, 2004, and Feb. 3, 2005 respectively, all of which are hereby expressly incorporated by reference into the present application.
  • TECHNICAL FIELD
  • The present invention relates to a novel organic/inorganic composite porous film that can show excellent thermal safety and lithium ion conductivity and a high degree of swelling with electrolyte compared to conventional polyolefin-based separators, and an electrochemical device comprising the same, which ensures safety and has improved quality.
  • BACKGROUND ART
  • Recently, there is an increasing interest in energy storage technology. Batteries have been widely used as energy sources in portable phones, camcorders, notebook computers, PCs and electric cars, resulting in intensive research and development into them. In this regard, electrochemical devices are subjects of great interest. Particularly, development of rechargeable secondary batteries is the focus of attention.
  • Secondary batteries are chemical batteries capable of repeated charge and discharge cycles by means of reversible interconversion between chemical energy and electric energy, and may be classified into Ni-MH secondary batteries and lithium secondary batteries. Lithium secondary batteries include lithium secondary metal batteries, lithium secondary ion batteries, lithium secondary polymer batteries, lithium secondary ion polymer batteries, etc.
  • Because lithium secondary batteries have drive voltage and energy density higher than those of conventional batteries using aqueous electrolytes (such as Ni-MH batteries), they are produced commercially by many production companies. However, most lithium secondary batteries have different safety characteristics depending on several factors. Evaluation of and security in safety of batteries are very important matters to be considered. Therefore, safety of batteries is strictly restricted in terms of ignition and combustion in batteries by safety standards.
  • Currently available lithium ion batteries and lithium ion polymer batteries use polyolefin-based separators in order to prevent short circuit between a cathode and an anode. However, because such polyolefin-based separators have a melting point of 200 °C. or less, they have a disadvantage in that they can be shrunk or molten to cause a change in volume when the temperature of a battery is increased by internal and/or external factors. Therefore, there is a great possibility of short-circuit between a cathode and an anode caused by shrinking or melting of separators, resulting in accidents such as explosion of a battery caused by emission of electric energy. As a result, it is necessary to provide a separator that does not cause heat shrinking at high temperature.
  • To solve the above problems related with polyolefin-based separators, many attempts are made to develop an electrolyte using an inorganic material serving as a substitute for a conventional separator. Such electrolytes may be broadly classified into two types. The first type is a solid composite electrolyte obtained by using inorganic particles having lithium ion conductivity alone or by using inorganic particles having lithium ion conductivity mixed with a polymer matrix. See, Japanese Laid-Open Patent No. 2003-022707, [“Solid State Ionics”-vol. 158, n. 3 , p. 275, (2003)], [“Journal of Power Sources”-vol. 112, n. 1, p. 209, (2002)], [“Electrochimica Acta”-vol. 48, n. 14, p. 2003, (2003)], etc. However, it is known that such composite electrolytes are not advisable, because they have low ion conductivity compared to liquid electrolytes and the interfacial resistance between the inorganic materials and the polymer is high while they are mixed.
  • The second type is an electrolyte obtained by mixing inorganic particles having lithium ion conductivity or not with a gel polymer electrolyte formed of a polymer and liquid electrolyte. In this case, inorganic materials are introduced in a relatively small amount compared to the polymer and liquid electrolyte, and thus merely have a supplementary function to assist in lithium ion conduction made by the liquid electrolyte.
  • However, because electrolytes prepared as described above have no pores therein or, if any, have pores with a size of several angstroms and low porosity, formed by introduction of an artificial plasticizer, the electrolytes cannot serve sufficiently as separator, resulting in degradation in the battery quality.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The foregoing and other objects, features and advantages of the present invention will become more apparent from the following detailed description when taken in conjunction with the accompanying drwings in which:
  • FIG. 1 is a schematic view showing an organic/inorganic composite porous film according to the present invention;
  • FIG. 2 is a photograph taken by Scanning Electron Microscope (SEM) showing the organic/inorganic composite porous film (PVdF-HFP/BaTiO3) according to Example 1;
  • FIG. 3 is a photograph taken by SEM showing a polyolefin-based separator (PP/PE/PP) used in Comparative Example 1;
  • FIG. 4 is a photograph taken by SEM showing a porous film manufactured by using a plasticizer according to Comparative Example 4;
  • FIG. 5 is a photograph showing the organic/inorganic composite porous film (PVdF-HFP/BaTiO3) according to Example 1 compared to a currently used PP/PE/PP separator and PE separator, after each of the samples is maintained at 150 °C. for 1 hour;
  • FIG. 6 is a picture showing the results of an overcharge test for the lithium secondary battery including a currently used PP/PE/PP separator according to Comparative Example 1 and the battery including the organic/inorganic composite porous film (PVdF-HFP/BaTiO3) according to Example 1; and
  • FIG. 7 is a graph showing variations in ion conductivity depending on the content of inorganic particles, in the organic/inorganic composite porous film according to the present invention.
  • DISCLOSURE OF THE INVENTION
  • We have found that an organic/inorganic composite porous film, formed by using (1) inorganic particles and (2) a binder polymer, improves poor thermal safety of a conventional polyolefin-based separator. Additionally, we have found that because the organic/inorganic composite porous film has a micropore structure formed by the inorganic particles present in the film, it provides an increased volume of space into which a liquid electrolyte infiltrates, resulting in improvements in lithium ion conductivity and degree of swelling with electrolyte. Therefore, the organic/inorganic composite porous film can improve the quality and safety of an electrochemical device using the same as separator.
  • Therefore, it is an object of the present invention to provide an organic/inorganic composite porous film capable of improving the quality and safety of an electrochemical device, a method for manufacturing the same and an electrochemical device comprising the same.
  • According to an aspect of the present invention, there is provided an organic/inorganic composite porous film, which comprises (a) inorganic particles; and (b) a binder polymer coating layer formed partially or totally on the surface of the inorganic particles, wherein the inorganic particles are interconnected among themselves and are fixed by the binder polymer, and interstitial volumes among the inorganic particles form a micropore structure. There is also provided an electrochemical device (preferably, a lithium secondary battery) comprising the same.
  • According to another aspect of the present invention, there is provided a method for manufacturing an organic/inorganic composite porous film, which includes the steps of: (a) dissolving a binder polymer into a solvent to form a polymer solution; (b) adding inorganic particles to the polymer solution obtained from step (a) and mixing them; and (c) coating the mixture of inorganic particles with binder polymer obtained from step (b) on a substrate, followed by drying, and then detaching the substrate.
  • Hereinafter, the present invention will be explained in more detail.
  • The present invention is characterized in that it provides a novel organic/inorganic composite porous film, which serves sufficiently as separator to prevent electrical contact between a cathode and an anode of a battery and to pass ions therethrough and shows excellent thermal safety, lithium ion conductivity and degree of swelling with electrolyte.
  • The organic/inorganic composite porous film is obtained by using inorganic particles and a binder polymer. The uniform and heat resistant micropore structure formed by the interstitial volumes among the inorganic particles permits the organic/inorganic composite porous film to be used as separator. Additionally, if a polymer capable of being gelled when swelled with a liquid electrolyte is used as the binder polymer component, the organic/inorganic composite porous film can serve also as electrolyte.
  • Particular characteristics of the organic/inorganic composite porous film are as follows.
  • (1) The organic/inorganic composite porous film according to the present invention shows improved thermal safety by virtue of the inorganic particles present therein.
  • In other words, although conventional polyolefin-based separators cause heat shrinking at high temperature because they have a melting point of 120-140 °C., the organic/inorganic composite porous film comprising the inorganic particles and binder polymer does not cause heat shrinking due to the heat resistance of the inorganic particles. Therefore, an electrochemical device using the above organic/inorganic composite porous film as separator causes no degradation in safety resulting from an internal short circuit between a cathode and an anode even under extreme conditions such as high temperature, overcharge, etc. As a result, such electrochemical devices have excellent safety characteristics compared to conventional batteries.
  • (2) Conventional solid electrolytes formed by using inorganic particles and a binder polymer have no pore structure or, if any, have an irregular pore structure having a pore size of several angstroms. Therefore, they cannot serve sufficiently as spacer, through which lithium ions can pass, resulting in degradation in the quality of a battery. On the contrary, the organic/inorganic composite porous film according to the present invention has uniform micropore structures formed by the interstitial volumes among the inorganic particles as shown in FIGS. 1 and 2, and the micropore structures permit lithium ions to move smoothly therethrough. Therefore, it is possible to introduce a large amount of electrolyte through the micropore structures so that a high degree of swelling with electrolyte can be obtained, resulting in improvement in the quality of a battery.
  • (3) It is possible to control the pore size and porosity of the organic/inorganic composite porous film by varying the particle diameter of the inorganic particles and the mixing ratio of the inorganic particles with the polymer. The micropore structure is subsequently filled with a liquid electrolyte so that the interfacial resistance generating among the inorganic particles or between the inorganic particles and the binder polymer can be reduced significantly.
  • (4) When the inorganic particles used in the organic/inorganic composite porous film have a high dielectric constant and/or lithium ion conductivity, the inorganic particles can improve lithium ion conductivity as well as heat resistance, thereby contributing to improvement of battery quality.
  • (5) When the binder polymer used in the organic/inorganic composite porous film is one showing a high degree of swelling with electrolyte, the electrolyte injected after assemblage of a battery can infiltrate into the polymer and the resultant polymer containing the electrolyte infiltrated therein has a capability of conducting electrolyte ions. Therefore, the organic/inorganic composite porous film according to the present invention can improve the quality of an electrochemical device compared to conventional organic/inorganic composite electrolytes. Additionally, the organic/inorganic composite porous film provides advantages in that wettablity with an electrolyte is improved compared to conventional hydrophobic polyolefin-based separators, and use of a polar electrolyte for battery is permitted.
  • (6) Finally, if the binder polymer is one capable of being gelled when swelled with electrolyte, the polymer reacts with the electrolyte injected subsequently and is gelled, thereby forming a gel type organic/inorganic composite electrolyte. Such electrolytes are produced with ease compared to conventional gel-type electrolytes and show excellent ion conductivity and a high degree of swelling with electrolyte, thereby contributing to improve the quality of a battery.
  • One component present in the organic/inorganic composite porous film according to the present invention is inorganic particles currently used in the art. The inorganic particles permit interstitial volumes to be formed among them, thereby serving to form micropores and to maintain the physical shape as spacer. Additionally, because the inorganic particles are characterized in that their physical properties are not changed even at a high temperature of 200 °C. or higher, the organic/inorganic composite porous film using the inorganic particles can have excellent heat resistance.
  • There is no particular limitation in selection of inorganic particles, as long as they are electrochemically stable. In other words, there is no particular limitation in inorganic particles that may be used in the present invention, as long as they are not subjected to oxidation and/or reduction at the range of drive voltages (for example, 0-5 V based on Li/Li+) of a battery, to which they are applied. Particularly, it is preferable to use inorganic particles having ion conductivity as high as possible, because such inorganic particles can improve ion conductivity and quality in an electrochemical device. Additionally, when inorganic particles having a high density are used, they have a difficulty in dispersion during a coating step and may increase the weight of a battery to be manufactured. Therefore, it is preferable to use inorganic particles having a density as low as possible. Further, when inorganic particles having a high dielectric constant are used, they can contribute to increase the dissociation degree of an electrolyte salt in a liquid electrolyte, such as a lithium salt, thereby improving the ion conductivity of the electrolyte.
  • For these reasons, it is preferable to use inorganic particles having a high dielectric constant of 5 or more, preferably of 10 or more, inorganic particles having lithium conductivity or mixtures thereof.
  • Particular non-limiting examples of inorganic particles having a dielectric constant of 5 or more include BaTiO3, Pb(Zr,Ti) O3 (PZT) , Pb1-xLaxZr1-yTiyO3 (PLZT), PB(Mg3Nb2/3)O3—PbTiO3 (PMN-PT), hafnia (HfO2), SrTiO3, SnO2, CeO2, MgO, NiO, CaO, ZnO, ZrO2, Y2O3, Al2O3, TiO2, SiC or mixtures thereof.
  • As used herein, “inorganic particles having lithium ion conductivity” are referred to as inorganic particles containing lithium elements and having a capability of conducting lithium ions without storing lithium. Inorganic particles having lithium ion conductivity can conduct and move lithium ions due to defects present in their structure, and thus can improve lithium ion conductivity and contribute to improve battery quality. Non-limiting examples of such inorganic particles having lithium ion conductivity include: lithim phosphate (Li3PO4), lithium titanium phosphate (LixTiy(PO4)3, 0<x<2, 0<y<3), lithium aluminum titanium phosphate (LixAlyTiz(PO4)3, 0<x<2, 0<y<1, 0<z<3), (LiAlTiP)xOy type glass (0<x<4, 0<y<13) such as 14Li2O-9Al2O3-38TiO2-39P2O5, lithium lanthanum titanate (LixLayTiO3, 0<y<3), lithium germanium thiophosphate (LixGeyPzSw, 0<x<4, 0<y<1, 0<z<1, 0<w<5), such as Li3.25Ge0.25P0.75S4, lithium nitrides(LixNy, 0<x<4, 0<y<2) such as Li3N, SiS2 type glass (LixSiySz, 0<x<3, 0<y<2, 0<z<4) such as Li3PO4-Li2S-SiS2, P2S5 type glass (LixPySz, 0<x<3, 0<y<3, 0<z<7) such as LiI-Li2S-P2S5, or mixtures thereof.
  • According to the present invention, inorganic particles having a relatively high dielectric constant are used instead of inorganic particles having no reactivity or having relatively low dielectric constant. Further, the present invention also provides a novel use of inorganic particles as separators.
  • The above-described inorganic particles, that have never been used as separators, for example Pb(Zr,Ti) O3 (PZT), Pb1-xLaxZr1-yTiyO3 (PLZT), Pb(Mg3Nb2/3) O3—PbTiO3 (PMN-PT), hafnia (HfO2), etc., have a high dielectric constant of 100 or more. The inorganic particles also have piezoelectricity so that an electric potential can be generated between both surfaces by the charge formation, when they are drawn or compressed under the application of a certain pressure. Therefore, the inorganic particles can prevent internal short circuit between both electrodes, thereby contributing to improve the safety of a battery. Additionally, when such inorganic particles having a high dielectric constant are combined with inorganic particles having lithium ion conductivity, synergic effects can be obtained.
  • The organic/inorganic composite porous film according to the present invention can form pores having a size of several micrometers by controlling the size of inorganic particles, content of inorganic particles and the mixing ratio of inorganic particles and binder polymer. It is also possible to control the pore size and porosity.
  • Although there is no particular limitation in size of inorganic particles, inorganic particles preferably have a size of 0.001-10 μm for the purpose of forming a film having a uniform thickness and providing a suitable porosity. When the size is less than 0.001 μm, inorganic particles have poor dispersibility so that physical properties of the organic/inorganic composite porous film cannot be controlled with ease. When the size is greater than 10 μm, the resultant organic/inorganic composite porous film has an increased thickness under the same solid content, resulting in degradation in mechanical properties. Furthermore, such excessively large pores may increase a possibility of internal short circuit being generated during repeated charge/discharge cycles.
  • The inorganic particles are present in the mixture of the inorganic particles with binder polymer forming the organic/inorganic composite porous film, preferably in an amount of 50-99 wt. %, more particularly in an amount of 60-95 wt. % based on 100 wt. % of the total weight of the mixture. When the content of the inorganic particles is less than 50 wt. %, the binder polymer is present in such a large amount as to decrease the interstitial volume formed among the inorganic particles and thus to decrease the pore size and porosity, resulting in degradation in the quality of a battery. When the content of the inorganic particles is greater than 99 wt. %, the polymer content is too low to provide sufficient adhesion among the inorganic particles, resulting in degradation in mechanical properties of a finally formed organic/inorganic composite porous film.
  • Another component present in the organic/inorganic composite porous film according to the present invention is a binder polymer currently used in the art. The binder polymer preferably has a glass transition temperature (Tg) as low as possible, more preferably Tg of between −200 °C. and 200 °C. Binder polymers having a low Tg as described above are preferable, because they can improve mechanical properties such as flexibility and elasticity of a finally formed film. The polymer serves as binder that interconnects and stably fixes the inorganic particles among themselves, and thus prevents degradation in mechanical properties of a finally formed organic/inorganic composite porous film.
  • When the binder polymer has ion conductivity, it can further improve the quality of an electrochemical device. However, it is not essential to use a binder polymer having ion conductivity. Therefore, the binder polymer preferably has a dielectric constant as high as possible. Because the dissociation degree of a salt in an electrolyte depends on the dielectric constant of a solvent used in the electrolyte, the polymer having a higher dielectric constant can increase the dissociation degree of a salt in the electrolyte used in the present invention. The dielectric constant of the polymer may range from 1.0 to 100 (as measured at a frequency of 1 kHz), and is preferably 10 or more.
  • In addition to the above-described functions, the binder polymer used in the present invention may be further characterized in that it is gelled when swelled with a liquid electrolyte, and thus shows a high degree of swelling. Therefore, it is preferable to use a polymer having a solubility parameter of between 15 and 45 MPa1/2, more preferably of between 15 and 25 MPa1/2, and between 30 and 45 MPa1/2. Therefore, hydrophilic polymers having a lot of polar groups are more preferable than hydrophobic polymers such as polyolefins. When the binder polymer has a solubility parameter of less than 15 Mpa1/2 or greater than 45 Mpa1/2, it has difficulty in swelling with a conventional liquid electrolyte for battery.
  • Non-limiting examples of the binder polymer that may be used in the present invention include polyvinylidene fluoride-co-hexafluoropropylene, polyvinylidene fluoride-co-trichloroethylene, polymethylmethacrylate, polyacrylonitrile, polyvinylpyrrolidone, polyvinyl acetate, polyethylene-co-vinyl acetate, polyethylene oxide, cellulose acetate, cellulose acetate butyrate, cellulose acetate propionate, cyanoethylpullulan, cyanoethyl polyvinylalcohol, cyanoethylcellulose, cyanoethylsucrose, pullulan, carboxymetyl cellulose, acrylonitrile-styrene-butadiene copolymer, polyimide or mixtures thereof. Other materials may be used alone or in combination, as long as they satisfy the above characteristics.
  • The organic/inorganic composite porous film may further comprise additives other than the inorganic particles and binder polymer.
  • When the organic/inorganic composite porous film is manufactured by using inorganic particles and a binder polymer, the film may be realized by three types of embodiments, but is not limited thereto.
  • The first type is an organic/inorganic composite porous film formed by using a mixture of inorganic particles and binder polymer with no additional substrate. The second type is an organic/inorganic composite porous film formed by coating the mixture on a porous substrate having pores, wherein the film coated on the porous substrate includes an active layer obtained by coating the mixture of inorganic particles and binder polymer on the surface of the porous substrate or on a part of the pores in the substrate. The third type is an organic/inorganic composite porous film formed by coating the mixture on a cathode and/or an anode. The third type is a monolithic electrode and film.
  • In the second embodiment of the organic/inorganic composite porous film according to the present invention, there is no particular limitation in the substrate coated with the mixture of inorganic particles and binder polymer, as long as it is a porous substrate having pores. However, it is preferable to use a heat resistant porous substrate having a melting point of 200 °C. or higher. Such heat resistant porous substrates can improve the thermal safety of the organic/inorganic composite porous film under external and/or internal thermal impacts. Non-limiting examples of the porous substrate having a melting point of 200 °C. or higher that may be used include polyethylene terephthalate, polybutylene terephthalate, polyester, polyacetal, polyamide, polycarbonate, polyimide, polyetherether ketone, polyether sulfone, polyphenylene oxide, polyphenylene sulfidro, polyethylene naphthalene or mixtures thereof. However, other heat resistant engineering plastics may be used with no particular limitation.
  • Although there is no particular limitation in thickness of the porous substrate, the porous substrate preferably has a thickness of between 1 μm and 100 μm, more preferably of between 5 μm and 50 μm. When the porous substrate has a thickness of less than 1 μm, it is difficult to maintain mechanical properties. When the porous substrate has a thickness of greater than 100 μm, it may function as resistance layer.
  • Although there is no particular limitation in pore size and porosity of the porous substrate, the porous substrate preferably has a porosity of between 5% and 95%. The pore size (diameter) preferably ranges from 0.01 μm to 50 μm, more preferably from 0.1 μm to 20 μm. When the pore size and porosity are less than 0.01 μm and 5%, respectively, the porous substrate may function as resistance layer. When the pore size and porosity are greater than 50 μm and 95%, respectively, it is difficult to maintain mechanical properties.
  • The porous substrate may take the form of a membrane or fiber. When the porous substrate is fibrous, it may be a nonwoven web forming a porous web (preferably, spunbond type web comprising long fibers or melt blown type web).
  • A spunbond process is performed continuously through a series of steps and provides long fibers formed by heating and melting, which is stretched, in turn, by hot air to form a web. A melt blown process performs spinning of a polymer capable of forming fibers through a spinneret having several hundreds of small orifices, and thus provides three-dimensional fibers having a spider-web structure resulting from interconnection of microfibers having a diameter of 10 μm or less.
  • The organic/inorganic composite porous film that may be formed in various types of embodiments according to the present invention is characterized in that the film comprises a micropore structure. First, the organic/inorganic composite porous film formed by using the mixture of inorganic particles and polymer alone has a micropore structure formed by interstitial volumes among the inorganic particles serving as support as well as spacer. Next, the organic/inorganic composite porous film formed by coating the mixture on a porous substrate has pore structures present both in the substrate and in the active layer due to the pores present in the porous substrate itself and interstitial volumes among the inorganic particles in the active layer formed on the substrate. Finally, the organic/inorganic composite porous film obtained by coating the mixture on the surface of an electrode has a uniform pore structure formed by interstitial volumes among the inorganic particles in the same manner as the pore structure formed by electrode active material particles in the electrode. Therefore, any embodiment of the organic/inorganic composite porous film according to the present invention has an increased volume of space, into which an electrolyte infiltrates, by virtue of such micropore structures. As a result, it is possible to increase dispersibility and conductivity of lithium ions, resulting in improvement in the quality of a battery.
  • The pore size and porosity of the organic/inorganic composite porous film mainly depend on the size of inorganic particles. For example, when inorganic particles having a particle diameter of 1 μm or less are used, pores formed thereby also have a size of 1 μm or less. The pore structure is filled with an electrolyte injected subsequently and the electrolyte serves to conduct ions. Therefore, the size and porosity of the pores are important factors in controlling the ion conductivity of the organic/inorganic composite porous film. Preferably, the pores size and porosity of the organic/inorganic composite porous film according to the present invention range from 0.01 to 10 μm and from 5 to 95%, respectively. There is no particular limitation in thickness of the organic/inorganic composite porous film according to the present invention. The thickness may be controlled depending on the quality of a battery. According to the present invention, the film preferably has a thickness of between 1 and 100 μm, more preferably of between 2 and 30 μm. Control of the thickness of the film may contribute to improve the quality of a battery.
  • There is no particular limitation in mixing ratio of inorganic particles to polymer in the organic/inorganic composite porous film according to the present invention. The mixing ratio can be controlled according to the thickness and structure of a film to be formed finally.
  • The organic/inorganic composite porous film may be applied to a battery together with a microporous separator (for example, a polyolefin-based separator), depending on the characteristics of a finally formed battery.
  • The organic/inorganic composite porous film may be manufactured by a conventional process known to one skilled in the art. One embodiment of a method for manufacturing the organic/inorganic composite porous film according to the present invention, includes the steps of: (a) dissolving a binder polymer into a solvent to form a polymer solution; (b) adding inorganic particles to the polymer solution obtained from step (a) and mixing them; and (c) coating the mixture obtained from step (b) on the surface of a substrate, followed by drying, and then detaching the substrate.
  • Hereinafter, the method for manufacturing the organic/inorganic composite porous film according to the present invention will be explained in detail.
  • (1) First, a binder polymer is dissolved in a suitable organic solvent to provide a polymer solution.
  • It is preferable that the solvent has a solubility parameter similar to that of the binder polymer to be used and a low boiling point. Such solvents can be mixed uniformly with the polymer and can be removed easily after coating the polymer. Non-limiting examples of the solvent that may be used include acetone, tetrahydrofuran, methylene chloride, chloroform, dimethylformamide, N-methyl-2-pyrrolidone (NMP), cyclohexane, water and mixtures thereof.
  • (2) Next, inorganic particles are added to and dispersed in the polymer solution obtained from the preceding step to provide a mixture of inorganic particles with binder polymer.
  • It is preferable to perform a step of pulverizing inorganic particles after adding the inorganic particles to the binder polymer solution. The time needed for pulverization is suitably 1-20 hours. The particle size of the pulverized particles ranges preferably from 0.001 and 10 μm. Conventional pulverization methods, preferably a method using a ball mill may be used.
  • Although there is no particular limitation in composition of the mixture containing inorganic particles and binder polymer, such composition can contribute to control the thickness, pore size and porosity of the organic/inorganic composite porous film to be formed finally.
  • In other words, as the weight ratio (I/P) of the inorganic particles (I) to the polymer (P) increases, porosity of the organic/inorganic composite porous film according to the present invention increases. Therefore, the thickness of the organic/inorganic composite porous film increases under the same solid content (weight of the inorganic particles weight of the binder polymer). Additionally, the pore size increases in proportion to the pore formation among the inorganic particles. When the size (particle diameter) of inorganic particles increases, interstitial distance among the inorganic particles also increases, thereby increasing the pore size.
  • (3) The mixture of inorganic particles with binder polymer is coated on a substrate, followed by drying, and then the substrate is detached to provide the organic/inorganic composite porous film.
  • Particular examples of the substrate that may be used include Teflon sheets or the like generally used in the art, but are not limited thereto.
  • In order to coat the porous substrate with the mixture of inorganic particles and binder polymer, any methods known to one skilled in the art may be used. It is possible to use various processes including dip coating, die coating, roll coating, comma coating or combinations thereof.
  • In this step, when the substrate is a porous substrate having pores or a preformed electrode, various types of organic/inorganic composite porous films can be obtained. The mixture of inorganic particles and polymer may be coated on the surface of porous substrate, on the surface of electrode, and on a part of the pores present in the substrate. In this step, the step of detaching a substrate may be omitted.
  • The organic/inorganic composite porous film according to the present invention, obtained as described above, may be used as separator in an electrochemical device, preferably in a lithium secondary battery. Additionally, the organic/inorganic composite porous film may be coated with a conventional polymer (for example, a polymer capable of being swelled with an electrolyte) on one surface or both surfaces so as to be used as separator.
  • If the binder polymer used in the film is a polymer capable of being gelled when swelled with a liquid electrolyte, the polymer may react with the electrolyte injected after assembling a battery by using the separator, and thus be gelled to form a gel type organic/inorganic composite electrolyte.
  • The gel type organic/inorganic composite electrolyte according to the present invention is prepared with ease compared to gel type polymer electrolytes according to the prior art, and has a large space to be filled with a liquid electrolyte due to its microporous structure, thereby showing excellent ion conductivity and a high degree of swelling with electrolyte, resulting in improvement in the quality of a battery.
  • Further, the present invention provides an electrochemical device comprising: (a) a cathode; (b) an anode; (c) the organic/inorganic composite porous film according to the present invention, interposed between the cathode and anode; and (d) an electrolyte.
  • Such electrochemical devices include any devices in which electrochemical reactions occur and particular examples thereof include all kinds of primary batteries, secondary batteries, fuel cells, solar cells or capacitors. Particularly, the electrochemical device is a lithium secondary battery including a lithium secondary metal battery, lithium secondary ion battery, lithium secondary polymer battery or lithium secondary ion polymer battery.
  • According to the present invention, the organic/inorganic composite porous film contained in the electrochemical device serves as separator. If the polymer used in the film is a polymer capable of being gelled when swelled with electrolyte, the film may serve also as electrolyte.
  • In addition to the above organic/inorganic composite porous film, a microporous separator may also be used. Particular examples of the microporous separator that may be used includes currently used polyolefin-based separators or at least one porous substrate having a melting point of 200° C., selected from the group consisting of polyethylene terephthalate, polybutylene terephthalate, polyester, polyacetal, polyamide, polycarbonate, polyimide, polyetherether ketone, polyether sulfone, polyphenylene oxide, polyphenylene sulfidro and polyethylene naphthalene.
  • The electrochemical device may be manufactured by a conventional method known to one skilled in the art. In one embodiment of the method for manufacturing the electrochemical device, the electrochemical device is assembled by using the organic/inorganic composite porous film interposed between a cathode and an anode, and then an electrolyte is injected.
  • The electrode that may be applied together with the organic/inorganic composite porous film according to the present invention may be formed by applying an electrode active material on a current collector according to a method known to one skilled in the art. Particularly, cathode active materials may include any conventional cathode active materials currently used in a cathode of a conventional electrochemical device. Particular non-limiting examples of the cathode active material include lithium intercalation materials such as lithium manganese oxides, lithium cobalt oxides, lithium nickel oxides, lithium iron oxides or composite oxides thereof. Additionally, anode active materials may include any conventional anode active materials currently used in an anode of a conventional electrochemical device. Particular non-limiting examples of the anode active material include lithium intercalation materials such as lithium metal, lithium alloys, carbon, petroleum coke, activated carbon, graphite or other carbonaceous materials. Non-limiting examples of a cathode current collector include foil formed of aluminum, nickel or a combination thereof. Non-limiting examples of an anode current collector include foil formed of copper, gold, nickel, copper alloys or a combination thereof.
  • The electrolyte that may be used in the present invention includes a salt represented by the formula of A+B, wherein A+ represents an alkali metal cation selected from the group consisting of Li+, Na+, K+ and combinations thereof, and B represents an anion selected from the group consisting of PF6 , BF4 , Cl, Br, I, ClO4 , AsF6 , CH3CO2 , CF3SO3 , N (CF3SO2) 2 , C (CF2SO2) 3 and combinations thereof, the salt being dissolved or dissociated in an organic solvent selected from the group consisting of propylene carbonate (PC), ethylene carbonate (EC), diethyl carbonate (DEC), dimethyl carbonate (DMC), dipropyl carbonate (DPC), dimethyl sulfoxide, acetonitrile, dimethoxyethane, diethoxyethane, tetrahydrofuran, N-methyl-2-pyrrolidone (NMP), ethylmethyl carbonate (EMC), gamma-butyrolactone (GBL) and mixtures thereof. However, the electrolyte that may be used in the present invention is not limited to the above examples.
  • More particularly, the electrolyte may be injected in a suitable step during the manufacturing process of an electrochemical device, according to the manufacturing process and desired properties of a final product. In other words, electrolyte may be injected, before an electrochemical device is assembled or in a final step during the assemblage of an electrochemical device.
  • Processes that may be used for applying the organic/inorganic composite porous film to a battery include not only a conventional winding process but also a lamination (stacking) and folding process of a separator and electrode.
  • When the organic/inorganic composite porous film according to the present invention is applied to a lamination process, it is possible to significantly improve the thermal safety of a battery, because a battery formed by a lamination and folding process generally shows more severe heat shrinking of a separator compared to a battery formed by a winding process. Additionally, when a lamination process is used, there is an advantage in that a battery can be assembled with ease by virtue of excellent adhesion of the polymer present in the organic/inorganic composite porous film according to the present invention. In this case, the adhesion can be controlled depending on the content of inorganic particles and polymer, and properties of the polymer. More particularly, as the polarity of the polymer increases and as the glass transition temperature (Tg) or melting point (Tm) of the polymer decreases, higher adhesion between the organic/inorganic composite porous film and electrode can be obtained.
  • BEST MODE FOR CARRYING OUT THE INVENTION
  • Reference will now be made in detail to the preferred embodiments of the present invention. It is to be understood that the following examples are illustrative only and the present invention is not limited thereto.
  • Reference Example. Variations in Ion Conductivity Depending on Content of Inorganic Particles
  • The organic/inorganic composite system according to the present invention was observed to determine variations in ion conductivity depending on the content of inorganic particles.
  • The organic/inorganic composite film according to the present invention was dipped into the electrolyte formed of ethylene carbonate/propylene carbonate/diethyl carbonate (EC/PC/DEC=30:20:50 on the basis of wt. %) containing 1M lithium hexafluorophosphate (LiPF6) dissolved therein. The film, into which the electrolyte is impregnated, was measured for ion conductivity by using Metrohm 712 instrument at a temperature of 25° C.
  • As shown in FIG. 7, as the content of inorganic particles increases, ion conductivity also increases.
  • Particularly, when 50 wt. % or more of inorganic particles are used, ion conductivity increases significantly.
  • EXAMPLE 1-9
  • Preparation of Organic/Inorganic Composite Porous Film and Manufacture of Lithium Secondary Battery using the Same
  • Example 1 1-1. Preparation of Organic/Inorganic Composite Porous Film (PVdF-HFP/BaTiO3)
  • PVdF-HFP polymer (polyvinylidene fluoride-hexafluoropropylene copolymer) was added to tetrahydrofuran (THF) in the amount of about 5 wt. % and dissolved therein at 50° C. for about 12 hours or more to form a polymer solution. To the polymer solution obtained as described above, BaTiO3 powder having a particle diameter of about 400 nm was added with the concentration of 20 wt. % on the total solid content basis, and then dispersed to form a mixed solution (BaTiO3/PVDF-HFP=80:20 (weight ratio)). Then, the mixed solution obtained as described above was coated on a Teflon sheet by using a doctor blade coating method. After coating, THF was dried and the Teflon sheet was detached to obtain a final organic/inorganic composite porous film (see, FIG. 1). The final film had a thickness of about 30 μm. After measuring with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.4 μm and a porosity of 60%.
  • 1-2. Manufacture of Lithium Secondary Battery
  • (Manufacture of Cathode)
  • To N-methyl-2-pyrrolidone (NMP) as a solvent, 94 wt. % of lithium cobalt composite oxide (LiCoO2) as cathode active material, 3 wt. % of carbon black as conductive agent and 3 wt. % of PVdF (polyvinylidene fluoride) as binder were added to form slurry for a cathode. The slurry was coated on A1 foil having a thickness of 20 μm as cathode collector and dried to form a cathode.
  • (Manufacture of Anode)
  • To N-methyl-2-pyrrolidone (NMP) as solvent, 96 wt. % of carbon powder as anode active material, 3 wt. % of PVdF (polyvinylidene fluoride) as binder and 1 wt. % of carbon black as conductive agent were added to form mixed slurry for an anode. The slurry was coated on Cu foil having a thickness of 10 μm as anode collector and dried to form an anode.
  • (Manufacture of Battery)
  • The cathode and anode obtained as described above were stacked with the organic/inorganic composite porous film obtained as described in Example 1-1 to form an assembly. Then, an electrolyte (ethylene carbonate (EC)/propylene carbonate (PC)/diethyl carbonate (DEC)=30:20:50 (wt. %) containing 1M of lithium hexafluorophosphate (LiPF6)) was injected thereto to provide a lithium secondary battery.
  • Example 2
  • Example 1 was repeated to provide a lithium secondary battery, except that mixed powder of BaTiO3 and Al2O3 (weight ratio=20:80) was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/BaTiO3—Al2O3). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 μm, pore size of 0.3 μm and a porosity of 57%.
  • Example 3
  • Example 1 was repeated to provide a lithium secondary battery, except that PMNPT(lead magnesium niobate-lead titanate) powder was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PMNPT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 30 μm, pore size of 0.3 μm and a porosity of 60%.
  • Example 4
  • Example 1 was repeated to provide a lithium secondary battery, except that PVdF-HFP was not used but about 2 wt. % of carboxymethyl cellulose (CMC) polymer was added to water and dissolved therein at 60° C. for about 12 hours or more to form a polymer solution, and the polymer solution was used to obtain an organic/inorganic composite porous film (CMC/BaTiO3). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 μm, pore size of 0.4 μm and a porosity of 58%.
  • Example 5
  • Example 1 was repeated to provide a lithium secondary battery, except that PZT powder was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PZT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 μm, pore size of 0.4 μm and a porosity of 62%.
  • Example 6
  • Example 1 was repeated to provide a lithium secondary battery, except that PLZT powder was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/PLZT). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 tin, pore size of 0.3 μm and a porosity of 58%.
  • Example 7
  • Example 1 was repeated to provide a lithium secondary battery, except that HfO2 powder was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/HfO2). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 28 μm, pore size of 0.4 μm and a porosity of 60%.
  • Example 8
  • Example 1 was repeated to provide a lithium secondary battery, except that lithium titanium phosphate (LiTi2(PO4)3) powder having a particle diameter of about 400 nm was used in an amount of the total solid content of 20 wt. %, instead of BaTiO3 powder, to obtain an organic/inorganic composite porous film (PVdF-HFP/LiTi2(PO4)3) having a thickness of about 20 μm. After measuring with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.5 μm and porosity of 62%.
  • Example 9
  • Example 1 was repeated to provide a lithium secondary battery, except that mixed powder of BaTiO3 and LiTi2(PO4)3 (weight ratio=50:50) was used instead of BaTiO3 powder to obtain an organic/inorganic composite porous film (PVdF-HFP/LiTi2(PO4)3-BaTiO3). After measuring with a porosimeter, the final organic/inorganic composite porous film had a thickness of 25 μm, pore size of 0.3 μm and a porosity of 60%.
  • COMPARATIVE EXAMPLES 1-4 Comparative Example 1
  • Example 1 was repeated to provide a lithium secondary battery, except that a conventional poly propylene/polyethylene/polypropylene (PP/PE/PP) separator (see, FIG. 3) was used.
  • Comparative Example 2
  • Example 1 was repeated to provide an organic/inorganic composite porous film and lithium secondary battery comprising the same, except that BaTiO3 and PVDF-HFP were used in a weight ratio of 20:80. After measuring the BaTiO3/PVdF-HFP with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.01 μm or less and a porosity of about 10%.
  • Comparative Example 3
  • Example 1 was repeated to provide an organic/inorganic composite porous film and lithium secondary battery comprising the same, except that LiTi2(PO4)3 and PVDF-HFP were used in a weight ratio of 10:90. After measuring the LiTi2(PO4)3/PVdF-HFP with a porosimeter, the final organic/inorganic composite porous film had a pore size of 0.01 μm or less and a porosity of about 5%.
  • Comparative Example 4 Manufacture of Porous Film using Plasticizer
  • Dimethyl carbonate (DMC) was selected as plasticizer and used along with PVdF-HFP in a ratio of 30:70 (on the wt. % basis) and THF as solvent to form a porous film. Dimetyl carbonate used in the film as plasticizer was extracted from the film by using methanol to provide a final porous film and a lithium secondary battery comprising the same. After measuring the porous PVdF-HFP film with a porosimeter, the porous film had a pore size of 0.01 μm or less and a porosity of about 30% (see, FIG. 4).
  • Experimental Example 1 Surface Analysis of Organic/Inorganic Composite Porous Film
  • The following test was performed to analyze the surface of an organic/inorganic composite porous film according to the present invention.
  • The sample used in this test was PVdF-HFP/BaTiO3 obtained according to Example 1. As controls, a PP/PE/PP separator according to Comparative Example 1 and the porous film using a plasticizer according to Comparative Example 4 were used.
  • When analyzed by using Scanning Electron Microscope (SEM), the PP/PE/PP separator according to Comparative Example 1 and the porous film according to Comparative Example 4 showed a conventional microporous structure (see, FIGS. 3 and 4). More particularly, the porous film according to Comparative Example 4 had a dense pore structure formed independently from the inorganic particles present on the surface of the film. It is thought that the dense pore structure is formed by artificial extraction of the plasticizer.
  • On the contrary, the organic/inorganic composite porous film according to the present invention showed a micropore structure formed by the inorganic particles as main component of the film (for example, inorganic particles with a high dielectric constant and/or lithium ion conductivity). Additionally, it could be seen that the polymer was coated on the surface of the inorganic particles (see, FIG. 2).
  • Experimental Example 2 Evaluation of Heat Shrinkage of Organic/Inorganic Composite Porous Film
  • The following experiment was performed to compare the organic/inorganic composite porous film with a conventional separator.
  • The organic/inorganic composite porous film (PVdF-CTFE/BaTiO3) according to Example 1 was used as sample. A conventional PP/PE/PP separator and PE separator were used as controls.
  • Each of the test samples was checked for its heat shrinkage after stored at a high temperature of 150° C. for hour. The test samples provided different results after the lapse of 1 hour at 150° C. The PP/PE/PP separator as control was shrunk due to high temperature to leave only the outer shape thereof. Similarly, the PE separator was shrunk to about 1/10 of its original size. On the contrary, the organic/inorganic composite porous film according to the present invention showed good results with no heat shrinkage (see, FIG. 5)
  • As can be seen from the foregoing, the organic/inorganic composite porous film according to the present invention has excellent thermal safety.
  • Experimental Example 3 Evaluation for Safety of Lithium Secondary Battery
  • The following test was performed to evaluate the safety of each lithium secondary battery comprising the organic/inorganic composite porous film according to the present invention.
  • Lithium secondary batteries according to Examples 1-9 were used as samples. As controls, used were the battery using a currently used PP/PE/PP separator according to Comparative Example 1, the battery using the BaTiO3/PVdF-HFP film (weight ratio=20:80 on the wt. % basis) as separator according to Comparative Example 2, and the battery using the LiTi2(PO4) 3/PVdF-HFP film (weight ratio=10:90 on the wt. % basis) as separator according to Comparative Example 3.
  • 3-1. Hot Box Test
  • Each battery was stored at high temperatures of 150° C. and 160° C. for 1 hour and then checked. The results are shown in the following Table 1.
  • After storing at high temperatures, the battery using a currently used PP/PE/PP separator according to Comparative Example 1 caused explosion when stored at 160° C. for 1 hour. This indicates that polyolefin-based separators cause extreme heat shrinking, melting and breakage when stored at high temperature, resulting in internal short circuit between both electrodes (i.e., a cathode and an anode) of a battery. On the contrary, lithium secondary batteries comprising an organic/inorganic composite porous film according to the present invention showed such a safe state as to prevent firing and burning even at a high temperature of 160° C. (see, Table 1).
  • Therefore, it can be seen that the lithium secondary battery comprising an organic/inorganic composite porous film according to the present invention has excellent thermal safety.
  • TABLE 1
    Hot Box Test Conditions
    150° C./1 hr 160° C./1 hr
    Ex. 1
    Ex. 2
    Ex. 3
    Ex. 4
    Ex. 5
    Ex. 6
    Ex. 7
    Ex. 8
    Ex. 9
    Comp. Ex. 1 X
    Comp. Ex. 2
    Comp. Ex. 3
  • 3-2. Overcharge Test
  • Each battery was charged under the conditions of 6V/1A and 10V/1A and then checked. The results are shown in the following Table 2.
  • After checking, the battery using a currently used PP/PE/PP separator according to Comparative Example 1 exploded (see, FIG. 6). This indicates that the polyolefin-based separator is shrunk by overcharge of the battery to cause short circuit between electrodes, resulting in degradation in safety of the battery. On the contrary, each lithium secondary battery comprising an organic/inorganic composite porous film according to the present invention showed excellent safety under overcharge conditions (see, Table 2 and FIG. 6).
  • TABLE 2
    Overcharge
    Test Conditions
    6 V/1 A 10 V/1 A
    Ex. 1
    Ex. 2
    Ex. 3
    Ex. 4
    Ex. 5
    Ex. 6
    Ex. 7
    Ex. 8
    Ex. 9
    Comp. Ex. 1 X
    Comp. Ex. 2
    Comp. Ex. 3
  • Experimental Example 4 Evaluation for Quality of Lithium Secondary Battery
  • The following tests were performed in order to determine the charge/discharge capacity of each lithium secondary battery comprising an organic/inorganic composite porous film according to the present invention.
  • Lithium secondary batteries according to Examples 1-9 were used as samples. As controls, used were the battery using a currently used PP/PE/PP separator according to Comparative Example 1, the battery using the BaTiO3/PVdF-HFP film (weight ratio=20:80 on the wt. % basis) as separator according to Comparative Example 2, the battery using the LiTi2(PO4)3/PVdF-HFP film (weight ratio=10:90 on the wt. % basis) as separator according to Comparative Example 3, and the battery using the porous PVdF-HFP film obtained by using a plasticizer as separator according to Comparative Example 4.
  • Each battery having a capacity of 760 mAh was subjected to cycling at a discharge rate of 0.5C, 10 and 2C. The following Table 3 shows the discharge capacity of each battery, the capacity being expressed on the basis of C-rate characteristics.
  • After performing the test, the battery according to Comparative Examples 2 using, as separator, an organic/inorganic composite porous film that includes a mixture containing inorganic particles with a high dielectric constant and a binder polymer in a ratio of 20:80 (on the wt. % basis) and the battery according to Comparative Examples 3 using, as separator, an organic/inorganic composite porous film that includes a mixture containing inorganic particles with lithium ion conductivity and a binder polymer in a ratio of 10:90 (on the wt. % basis), showed a significant drop in capacity depending on discharge rates, as compared to the batteries using, as separators, the organic/inorganic composite porous film obtained from the above Examples according to the present invention and a conventional polyolefin-based separator (see, Table 3). This indicates that such relatively low amount of inorganic particles compared to the polymer may decrease the pore size and porosity in the pore structure formed by interstitial volume among the inorganic particles, resulting in degradation in the quality of a battery. Additionally, the battery using the porous film having a pore structure artificially formed by using a plasticizer as separator according to Comparative Example 4 also showed a significant drop in capacity depending on discharge rates in the same manner as the batteries according to Comparative Examples 2 and 3.
  • On the contrary, lithium secondary batteries comprising the organic/inorganic composite porous film according to the present invention showed C-rate characteristics comparable to those of the battery using a conventional polyolefin-based separator under a discharge rate of up to 2C (see, Table 3).
  • TABLE 3
    Discharge Rate (mAh)
    0.5 C 1 C 2 C
    Ex. 1 757 746 694
    Ex. 2 756 748 693
    Ex. 3 756 744 691
    Ex. 4 758 747 694
    Ex. 5 759 750 698
    Ex. 6 755 742 690
    Ex. 7 758 747 694
    Ex. 8 756 745 793
    Ex. 9 757 746 792
    Comp. Ex. 1 758 746 693
    Comp. Ex. 2 695 562 397
    Comp. Ex. 3 642 555 385
    Comp. Ex. 4 698 585 426
  • INDUSTRIAL APPLICABILITY
  • As can be seen from the foregoing, the organic/inorganic composite porous film according to the present invention comprises inorganic particles and a binder polymer, wherein the inorganic particles are interconnected among themselves and fixed by the binder polymer and interstitial volumes among the inorganic particles form a heat resistant micropore structure. Therefore, it is possible to increase the space to be filled with an electrolyte, and thus to improve a degree of swelling with electrolyte and lithium ion conductivity. As a result, the organic/inorganic composite porous film according to the present invention contributes to improve the thermal safety and quality of a lithium secondary battery using the same as separator.
  • While this invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not limited to the disclosed embodiment and the drawings. On the contrary, it is intended to cover various modifications and variations within the spirit and scope of the appended claims.

Claims (19)

1. An organic/inorganic composite porous film, which comprises:
(a) inorganic particles; and
(b) a binder polymer coating layer formed partially or totally on surfaces of the inorganic particles, wherein the inorganic particles are interconnected among themselves and are fixed by the binder polymer, and interstitial volumes among the inorganic particles form a micropore structure.
2. The film according to claim 1, wherein the inorganic particles are at least one selected from the group consisting of: (a) inorganic particles having a dielectric constant of 5 or more; and (b) inorganic particles having lithium ion conductivity.
3. The film according to claim 2, wherein the inorganic particles having a dielectric constant of 5 or more are BaTiO3, Pb(Zr,Ti) O3 (PZT), Pb1-xLaxZr1-yTiyO3 (PLZT) , Pb(Mg3Nb2/3) O3—PbTiO3 (PMN-PT), hafnia (HfO2), SrTiO3, SnO2, CeO2, MgO, NiO, CaO, ZnO, ZrO2, Y2O3, Al2O3, TiO2 or SiC.
4. The film according to claim 2, wherein the inorganic particles having lithium ion conductivity are at least one selected from the group consisting of: lithim phosphate (Li3PO4), lithium titanium phosphate (LixTiy(PO4)3, 0<x<2, 0<y<3), lithium aluminum titanium phosphate (LixAlyTiz(PO4)3, 0<x<2, 0<y<1, 0<z<3), (LiAlTiP)xOy type glass (0<x<4, 0<y<13), lithium lanthanum titanate (LixLayTiO3, 0<x<2, 0<y<3), lithium germanium thiophosphate (LixGeyPzSw, 0<x<4, 0<y<1, 0<z<1, 0<w<5), lithium nitrides (LixNy, 0<x<4, 0<y<2), SiS2 type glass (LixSiySz, 0<x<3, 0<y<2, 0<z<4) and P2S5 type glass (LixPySz, 0<x<3, 0<y<3, 0<z<7).
5. The film according to claim 1, wherein the inorganic particles have a size of between 0.001 μm and 10 μm.
6. The film according to claim 1, wherein the inorganic particles are present in the mixture of inorganic particles with the binder polymer in an amount of 50-99 wt. % based on 100 wt. % of the mixture.
7. The film according to claim 1, wherein the binder polymer has a glass transition temperature (Tg) of between −200° C. and 200° C.
8. The film according to claim 1, wherein the binder polymer has a solubility parameter of between 15 and 45 MPa1/2.
9. The film according to claim 1, wherein the binder polymer is at least one selected from the group consisting of polyvinylidene fluoride-co-hexafluoropropylene, polyvinylidene fluoride-co-trichloroethylene, polymethylmethacrylate, polyacrylonitrile, polyvinylpyrrolidone, polyvinyl acetate, polyethylene-co-vinyl acetate, polyethylene oxide, cellulose acetate, cellulose acetate butyrate, cellulose acetate propionate, cyanoethylpullulan, cyanoethyl polyvinylalcohol, cyanoethylcellulose, cyanoethylsucrose, pullulan, carboxymetyl cellulose, acrylonitrile-styrene-butadiene copolymer and polyimide.
10. The film according to claim 1, which has a pore size of between 0.001 and 10 μm.
11. The film according to claim 1, which has a porosity of between 5% and 95%.
12. The film according to claim 1, which has a thickness of between 1 and 100 μm.
13. An electrochemical device comprising:
(a) a cathode;
(b) an anode;
(c) an organic/inorganic composite porous film, which comprises: (i) inorganic particles; and (ii) a binder polymer coating layer formed partially or totally on surfaces of the inorganic particles, wherein the inorganic particles are interconnected among themselves and are fixed by the binder polymer, and interstitial volumes among the inorganic particles form a micropore structure; and
(d) an electrolyte.
14. The electrochemical device according to claim 13, wherein the inorganic particles are at least one selected from the group consisting of: (a) inorganic particles having a dielectric constant of 5 or more; and
(b) inorganic particles having lithium ion conductivity.
15. The electrochemical device according to claim 13, wherein the binder polymer has a solubility parameter of between 15 and 45 MPa1/2.
16. The electrochemical device according to claim 13, which is a lithium secondary battery.
17. The electrochemical device according to claim 13, which further comprises a microporous separator.
18. The electrochemical device according to claim 17, wherein the microporous separator is a polyolefin-based separator, or at least one porous substrate having a melting point of 200° C. or higher, selected from the group consisting of polyethylene terephthalate, polybutylene terephthalate, polyester, polyacetal, polyamide, polycarbonate, polyimide, polyetherether ketone, polyether sulfone, polyphenylene oxide, polyphenylene sulfidro and polyethylene naphthalene.
19. A method for manufacturing an organic/inorganic composite porous film according to claim 1, which comprises the steps of:
(a) dissolving a binder polymer into a solvent to form a polymer solution;
(b) adding inorganic particles to the polymer solution obtained from step (a) and mixing them; and
(c) coating the mixture of inorganic particles with binder polymer obtained from step (b) on a substrate, followed by drying, and then detaching the substrate.
US15/266,838 2004-09-02 2016-09-15 Organic/inorganic composite porous film and electrochemical device prepared thereby Abandoned US20170005309A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US15/266,838 US20170005309A1 (en) 2004-09-02 2016-09-15 Organic/inorganic composite porous film and electrochemical device prepared thereby
US15/890,229 US20180166671A1 (en) 2004-09-02 2018-02-06 Organic/inorganic composite porous film and electrochemical device prepared thereby
US16/374,483 US20190229316A1 (en) 2004-09-02 2019-04-03 Organic/inorganic composite porous film and electrochemical device prepared thereby
US17/358,433 US20210320380A1 (en) 2004-09-02 2021-06-25 Organic/inorganic composite porous film and electrochemical device prepared thereby

Applications Claiming Priority (9)

Application Number Priority Date Filing Date Title
KR20040070095 2004-09-02
KR1020040070096A KR100895196B1 (en) 2004-09-02 2004-09-02 Organic/inorganic composite porous film and electrochemical device prepared thereby
KR10-2004-70096 2004-09-02
KR10-2004-70095 2004-09-02
KR10-2005-9999 2005-02-03
KR1020050009999A KR20060041650A (en) 2004-09-02 2005-02-03 Organic/inorganic composite porous film and electrochemical device prepared thereby
US11/217,918 US8409746B2 (en) 2004-09-02 2005-09-01 Organic/inorganic composite porous film and electrochemical device prepared thereby
US13/785,260 US9490463B2 (en) 2004-09-02 2013-03-05 Organic/inorganic composite porous film and electrochemical device prepared thereby
US15/266,838 US20170005309A1 (en) 2004-09-02 2016-09-15 Organic/inorganic composite porous film and electrochemical device prepared thereby

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US13/785,260 Continuation US9490463B2 (en) 2004-09-02 2013-03-05 Organic/inorganic composite porous film and electrochemical device prepared thereby

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US15/890,229 Continuation US20180166671A1 (en) 2004-09-02 2018-02-06 Organic/inorganic composite porous film and electrochemical device prepared thereby

Publications (1)

Publication Number Publication Date
US20170005309A1 true US20170005309A1 (en) 2017-01-05

Family

ID=35943666

Family Applications (7)

Application Number Title Priority Date Filing Date
US11/217,918 Active 2027-12-11 US8409746B2 (en) 2004-02-09 2005-09-01 Organic/inorganic composite porous film and electrochemical device prepared thereby
US13/184,288 Abandoned US20110281172A1 (en) 2004-02-09 2011-07-15 Organic/inorganic composite porous film and electrochemical device prepared thereby
US13/785,260 Active US9490463B2 (en) 2004-09-02 2013-03-05 Organic/inorganic composite porous film and electrochemical device prepared thereby
US15/266,838 Abandoned US20170005309A1 (en) 2004-09-02 2016-09-15 Organic/inorganic composite porous film and electrochemical device prepared thereby
US15/890,229 Abandoned US20180166671A1 (en) 2004-09-02 2018-02-06 Organic/inorganic composite porous film and electrochemical device prepared thereby
US16/374,483 Abandoned US20190229316A1 (en) 2004-09-02 2019-04-03 Organic/inorganic composite porous film and electrochemical device prepared thereby
US17/358,433 Pending US20210320380A1 (en) 2004-09-02 2021-06-25 Organic/inorganic composite porous film and electrochemical device prepared thereby

Family Applications Before (3)

Application Number Title Priority Date Filing Date
US11/217,918 Active 2027-12-11 US8409746B2 (en) 2004-02-09 2005-09-01 Organic/inorganic composite porous film and electrochemical device prepared thereby
US13/184,288 Abandoned US20110281172A1 (en) 2004-02-09 2011-07-15 Organic/inorganic composite porous film and electrochemical device prepared thereby
US13/785,260 Active US9490463B2 (en) 2004-09-02 2013-03-05 Organic/inorganic composite porous film and electrochemical device prepared thereby

Family Applications After (3)

Application Number Title Priority Date Filing Date
US15/890,229 Abandoned US20180166671A1 (en) 2004-09-02 2018-02-06 Organic/inorganic composite porous film and electrochemical device prepared thereby
US16/374,483 Abandoned US20190229316A1 (en) 2004-09-02 2019-04-03 Organic/inorganic composite porous film and electrochemical device prepared thereby
US17/358,433 Pending US20210320380A1 (en) 2004-09-02 2021-06-25 Organic/inorganic composite porous film and electrochemical device prepared thereby

Country Status (3)

Country Link
US (7) US8409746B2 (en)
EP (3) EP1784876B1 (en)
WO (1) WO2006025662A1 (en)

Families Citing this family (138)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080057386A1 (en) 2002-10-15 2008-03-06 Polyplus Battery Company Ionically conductive membranes for protection of active metal anodes and battery cells
US7645543B2 (en) 2002-10-15 2010-01-12 Polyplus Battery Company Active metal/aqueous electrochemical cells and systems
US7491458B2 (en) 2003-11-10 2009-02-17 Polyplus Battery Company Active metal fuel cells
US9368775B2 (en) 2004-02-06 2016-06-14 Polyplus Battery Company Protected lithium electrodes having porous ceramic separators, including an integrated structure of porous and dense Li ion conducting garnet solid electrolyte layers
US7282295B2 (en) * 2004-02-06 2007-10-16 Polyplus Battery Company Protected active metal electrode and battery cell structures with non-aqueous interlayer architecture
EP1784876B1 (en) * 2004-09-02 2018-01-24 LG Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US7641992B2 (en) * 2004-10-29 2010-01-05 Medtronic, Inc. Medical device having lithium-ion battery
CN101048898B (en) 2004-10-29 2012-02-01 麦德托尼克公司 Lithium-ion battery and medical device
US9065145B2 (en) * 2004-10-29 2015-06-23 Medtronic, Inc. Lithium-ion battery
US8105714B2 (en) * 2004-10-29 2012-01-31 Medtronic, Inc. Lithium-ion battery
US7642013B2 (en) * 2004-10-29 2010-01-05 Medtronic, Inc. Medical device having lithium-ion battery
US9077022B2 (en) 2004-10-29 2015-07-07 Medtronic, Inc. Lithium-ion battery
US7807299B2 (en) * 2004-10-29 2010-10-05 Medtronic, Inc. Lithium-ion battery
US7563541B2 (en) * 2004-10-29 2009-07-21 Medtronic, Inc. Lithium-ion battery
US7662509B2 (en) * 2004-10-29 2010-02-16 Medtronic, Inc. Lithium-ion battery
US8980453B2 (en) 2008-04-30 2015-03-17 Medtronic, Inc. Formation process for lithium-ion batteries
US7927742B2 (en) 2004-10-29 2011-04-19 Medtronic, Inc. Negative-limited lithium-ion battery
US7682745B2 (en) * 2004-10-29 2010-03-23 Medtronic, Inc. Medical device having lithium-ion battery
WO2007062220A2 (en) * 2005-11-23 2007-05-31 Polyplus Battery Company Li/air non-aqueous batteries
US8182943B2 (en) * 2005-12-19 2012-05-22 Polyplus Battery Company Composite solid electrolyte for protection of active metal anodes
TWI346406B (en) * 2006-02-16 2011-08-01 Lg Chemical Ltd Lithium secondary battery with enhanced heat-resistance
JP5611505B2 (en) * 2006-03-29 2014-10-22 日立マクセル株式会社 Battery separator and lithium secondary battery
US9269937B2 (en) 2006-04-28 2016-02-23 Lg Chem, Ltd. Method for preparing separator for battery with gel polymer layer
WO2007126242A1 (en) * 2006-04-28 2007-11-08 Lg Chem, Ltd. Separator for battery with gel polymer layer
WO2007129839A1 (en) * 2006-05-04 2007-11-15 Lg Chem, Ltd. Lithium secondary battery and method for producing the same
US7990679B2 (en) * 2006-07-14 2011-08-02 Dais Analytic Corporation Nanoparticle ultracapacitor
JP4876765B2 (en) * 2006-08-10 2012-02-15 パナソニック株式会社 Method for producing non-aqueous electrolyte secondary battery
US20120196189A1 (en) 2007-06-29 2012-08-02 Johnson Ip Holding, Llc Amorphous ionically conductive metal oxides and sol gel method of preparation
US8211496B2 (en) * 2007-06-29 2012-07-03 Johnson Ip Holding, Llc Amorphous lithium lanthanum titanate thin films manufacturing method
US9034525B2 (en) * 2008-06-27 2015-05-19 Johnson Ip Holding, Llc Ionically-conductive amorphous lithium lanthanum zirconium oxide
JP5795475B2 (en) 2007-07-25 2015-10-14 エルジー・ケム・リミテッド Electrochemical element and manufacturing method thereof
US8735766B2 (en) * 2007-08-06 2014-05-27 Plasma Surgical Investments Limited Cathode assembly and method for pulsed plasma generation
JP5426551B2 (en) * 2007-08-21 2014-02-26 エー123 システムズ, インコーポレイテッド Electrochemical cell separator and method for producing the same
US20090092903A1 (en) * 2007-08-29 2009-04-09 Johnson Lonnie G Low Cost Solid State Rechargeable Battery and Method of Manufacturing Same
CN101809801B (en) 2007-09-28 2014-03-26 A123系统公司 Batteries having inorganic/organic porous films
CA2719223C (en) 2008-03-27 2017-07-04 Zpower, Inc. Electrode separator
WO2010024559A2 (en) 2008-08-25 2010-03-04 주식회사 엘지화학 Separator furnished with porous coating layer, method of manufacturing same, and electrochemical device furnished therewith
CN102197516B (en) * 2008-08-29 2014-03-12 日本瑞翁株式会社 Porous membrane, secondary battery electrode and lithium ion secondary battery
JP5689800B2 (en) * 2008-09-03 2015-03-25 エルジー・ケム・リミテッド Separator provided with porous coating layer and electrochemical device provided with the same
KR101089135B1 (en) * 2008-12-19 2011-12-02 주식회사 엘지화학 Lithium secondary battery having high power
DE112010000853T5 (en) * 2009-01-12 2012-12-06 A123 Systems, Inc. Laminated battery cell and method for its production
DE102009002680A1 (en) 2009-04-28 2010-11-04 Evonik Litarion Gmbh Production and use of ceramic composite materials based on polymer carrier film
DE202009013522U1 (en) 2009-10-07 2009-12-24 Hummel Ag Cable gland for a shielded cable
US20130183568A1 (en) * 2009-11-18 2013-07-18 Susan J. Babinec Composite separator for electrochemical cell and method for its manufacture
KR101408844B1 (en) 2010-06-10 2014-06-20 에스케이이노베이션 주식회사 Micro-porous polyolefin film with thermally stable hybrid-composite layers
EP2617084B1 (en) * 2010-09-16 2020-05-13 ZPower, LLC Electrode separator
US20130244003A1 (en) * 2010-11-26 2013-09-19 Research & Business Foundation Sungkyunkwan University Organic/inorganic hybrid hierarchical structure and method for manufacturing superhydrophobic or superhydrophilic surface using same
EP2677590B1 (en) * 2011-02-15 2019-04-03 LG Chem, Ltd. Separator, preparation method thereof, and electrochemical device comprising same
KR101254693B1 (en) 2011-02-15 2013-04-15 주식회사 엘지화학 A separator, the manufacturing method thereof, and electrochemical device containing the same
US9287580B2 (en) 2011-07-27 2016-03-15 Medtronic, Inc. Battery with auxiliary electrode
US9065156B2 (en) 2011-08-08 2015-06-23 Wisconsin Alumni Research Foundation Photovoltaic capacitor for direct solar energy conversion and storage
CN103765661B (en) 2011-09-02 2016-06-22 西奥公司 Microsphere composite electrolyte
WO2013047875A1 (en) * 2011-09-30 2013-04-04 富士フイルム株式会社 Electroacoustic converter film, flexible display, vocal cord microphone, and musical instrument sensor
CN103181000B (en) * 2011-10-20 2019-04-19 株式会社Lg化学 The manufacturing method of diaphragm, the diaphragm manufactured by this method and the electrochemical apparatus for having the diaphragm
KR20130048843A (en) 2011-11-03 2013-05-13 에스케이이노베이션 주식회사 Multi-layered micro-porous polyolefin film having excellent thermal property and method for preparing the same
US8828573B2 (en) 2011-11-15 2014-09-09 Polyplus Battery Company Electrode structures for aqueous electrolyte lithium sulfur batteries
US8828574B2 (en) 2011-11-15 2014-09-09 Polyplus Battery Company Electrolyte compositions for aqueous electrolyte lithium sulfur batteries
US9660265B2 (en) 2011-11-15 2017-05-23 Polyplus Battery Company Lithium sulfur batteries and electrolytes and sulfur cathodes thereof
US8828575B2 (en) 2011-11-15 2014-09-09 PolyPlus Batter Company Aqueous electrolyte lithium sulfur batteries
US20130149560A1 (en) 2011-12-09 2013-06-13 Medtronic, Inc. Auxiliary electrode for lithium-ion battery
DE102012000910A1 (en) * 2012-01-19 2013-07-25 Sihl Gmbh Separator comprising a porous layer and process for its preparation
CN102544576A (en) * 2012-02-21 2012-07-04 东莞新能源科技有限公司 Lithium ion battery
KR20150016210A (en) 2012-03-01 2015-02-11 엑셀라트론 솔리드 스테이트 엘엘씨 High Capacity Solid State Composite Cathode, Solid State Composite Separator, Solid-State Rechargeable Lithium Battery and Methods of Making Same
EP3252854B1 (en) 2012-04-13 2018-09-26 LG Chem, Ltd. Battery system for secondary battery comprising blended cathode material, and apparatus and method for managing the same
PL2808933T3 (en) 2012-05-23 2019-09-30 Lg Chem, Ltd. Fabricating method of electrode assembly and electrochemical cell containing the same
KR101454829B1 (en) 2012-06-13 2014-10-28 주식회사 엘지화학 Apparatus for estimating state of charge of secondary battery including blended cathode material and Method thereof
EP3339870B1 (en) 2012-06-13 2021-08-04 LG Chem, Ltd. Apparatus and method for estimating soc of secondary battery including blended cathode material
EP2835658B1 (en) 2012-06-13 2016-10-19 LG Chem, Ltd. Apparatus and method for estimating voltage of secondary cell including mixed cathode material
CN102737850A (en) * 2012-06-25 2012-10-17 侯栋 Diaphragm
US9123970B2 (en) * 2012-07-03 2015-09-01 Electronics And Telecommunications Research Institute Lithium battery binder composition, method for preparing the same and lithium battery including the same
US20140011095A1 (en) * 2012-07-03 2014-01-09 Electronics And Telecommunications Research Institute Organic/inorganic hybrid electrolyte, methods for preparing the same, and lithium battery including the same
US9793525B2 (en) 2012-10-09 2017-10-17 Johnson Battery Technologies, Inc. Solid-state battery electrodes
KR101936924B1 (en) 2012-12-06 2019-01-09 삼성전자주식회사 Separation membrane, and water treatment device using said separation membrane
TWI520402B (en) 2013-02-15 2016-02-01 Lg化學股份有限公司 Electrode assembly and manufacturing method thereof
PL2863466T3 (en) * 2013-02-15 2020-09-07 Lg Chem, Ltd. Electrode assembly and method for producing electrode assembly
EP2958179B1 (en) 2013-02-15 2017-06-21 LG Chem, Ltd. Electrode assembly having improved safety and production method therefor
WO2014126431A1 (en) * 2013-02-15 2014-08-21 주식회사 엘지화학 Electrode assembly and polymer secondary battery cell comprising same
WO2014126430A1 (en) * 2013-02-15 2014-08-21 주식회사 엘지화학 Electrode assembly and polymer secondary battery cell comprising same
PL2876721T3 (en) 2013-02-15 2023-01-09 Lg Energy Solution, Ltd. Electrode assembly
MY153875A (en) * 2013-03-05 2015-04-07 Univ Malaya A method of producing a polytetrafluoroethylene adhesive polymer membrane
KR101816763B1 (en) 2013-05-08 2018-01-09 주식회사 엘지화학 Electrode structure of electrochemical device including insulating layer and manufacturing thereof
EP2894698B1 (en) * 2013-05-08 2017-03-01 LG Chem, Ltd. Electrode structure including insulation layer, method for manufacturing same, and electrochemical element including same
CN103311486B (en) * 2013-05-14 2016-06-08 中南大学 A kind of organic-inorganic composite diaphragm and Synthesis and applications thereof
CN104662724A (en) * 2013-05-23 2015-05-27 株式会社Lg化学 Method for manufacturing electrode assembly
KR101549337B1 (en) 2013-11-22 2015-09-01 주식회사 엘지화학 Method for electrode assembly
EP2882028B1 (en) * 2013-05-23 2020-01-15 LG Chem, Ltd. Method for manufacturing electrode assembly
EP2882027B1 (en) 2013-05-23 2020-03-18 LG Chem, Ltd. Electrode assembly and radical unit for the same
US9905860B2 (en) 2013-06-28 2018-02-27 Polyplus Battery Company Water activated battery system having enhanced start-up behavior
KR101620173B1 (en) 2013-07-10 2016-05-13 주식회사 엘지화학 A stepwise electrode assembly with good stability and the method thereof
US10497915B2 (en) 2013-08-29 2019-12-03 Htc Corporation Battery structure, electronic device and manufacturing method of battery structure
WO2015056963A1 (en) 2013-10-14 2015-04-23 주식회사 엘지화학 Apparatus for estimating state of secondary battery including blended positive electrode material, and method therefor
KR101708885B1 (en) 2013-10-14 2017-02-21 주식회사 엘지화학 Apparatus for estimating state of secondary battery including blended cathode material and Method thereof
KR101703957B1 (en) * 2013-10-31 2017-02-08 주식회사 엘지화학 An organic-inoranic composite porous layer, a seperator and an electrode structure comprising the same
WO2015069008A1 (en) * 2013-11-05 2015-05-14 주식회사 엘지화학 Separation membrane for electrochemical element
DE102013226064A1 (en) * 2013-12-16 2015-06-18 Robert Bosch Gmbh Method for producing a functional layer for a lithium cell
DE102013226743A1 (en) * 2013-12-19 2015-06-25 Robert Bosch Gmbh Thermally conductive polymer separator
KR102059720B1 (en) 2014-03-14 2019-12-26 도오꾜오까고오교 가부시끼가이샤 Porous separator for secondary batteries and secondary battery using same
CN106132519B (en) 2014-04-11 2020-05-15 3M创新有限公司 Microporous article with acid-sintered interconnected silica nanoparticle three-dimensional porous network and method of making same
KR101729815B1 (en) 2014-07-29 2017-04-24 주식회사 엘지화학 Electrode assembly and radical cell for the same
KR101661024B1 (en) * 2014-07-31 2016-09-28 주식회사 엘지화학 Electrodes Assembly and Manufacturing Method thereof
KR101710060B1 (en) * 2014-08-13 2017-02-24 주식회사 엘지화학 Stack and folding-type electrode assembly and method for fabricating the same
KR101823192B1 (en) 2014-09-04 2018-01-29 주식회사 엘지화학 Apparatus for manufcaturing radical unit and method for manufacturing electrode assembly
US9773966B2 (en) * 2014-09-08 2017-09-26 Shimano Inc. Piezoelectric sensor for bicycle component
KR101729818B1 (en) 2014-09-17 2017-05-11 주식회사 엘지화학 Electrode assembly and radical unit for the same
KR102432559B1 (en) * 2014-09-22 2022-08-17 도쿄 오카 고교 가부시키가이샤 Separator for metal secondary batteries
KR101618218B1 (en) * 2014-09-26 2016-05-09 대한민국 An Electrochemical Device Comprising The Nano-Fiber Membrane Cellulose And Preparation Method Thereof
KR101806594B1 (en) 2014-09-26 2017-12-07 주식회사 엘지화학 Method for manufacturing electrode assembly
JP6580680B2 (en) 2014-12-08 2019-09-25 エルジー・ケム・リミテッド Secondary battery with improved output characteristics
US10050246B2 (en) 2014-12-26 2018-08-14 Samsug SDI Co., Ltd. Binder for rechargeable battery, separator for rechargeable battery including same, and rechargeable battery including same
DE102015202972A1 (en) 2015-02-19 2016-08-25 Robert Bosch Gmbh Flexible inorganic-polymer composite separator for a lithium-oxygen cell
CN105161762A (en) * 2015-08-05 2015-12-16 山东鸿正电池材料科技有限公司 Preparation method of polymer electrolyte membrane and lithium-ion battery
EP3394918A1 (en) 2015-12-21 2018-10-31 Johnson IP Holding, LLC Solid-state batteries, separators, electrodes, and methods of fabrication
US10218044B2 (en) 2016-01-22 2019-02-26 Johnson Ip Holding, Llc Johnson lithium oxygen electrochemical engine
WO2017161160A1 (en) 2016-03-16 2017-09-21 University Of Utah Research Foundation Composite solid electrolytes for lithium batteries
WO2017171524A1 (en) 2016-04-01 2017-10-05 주식회사 엘지화학 Electrochemical device separator comprising adhesive layer, and electrode assembly comprising separator
CN106784548A (en) * 2016-12-19 2017-05-31 西南石油大学 Lithium ion battery green, Efficient lignocellulose matrix barrier film and preparation method thereof
KR102266508B1 (en) 2017-09-26 2021-06-16 주식회사 엘지에너지솔루션 Battery Rapid Charging System
CN110622338B (en) 2017-12-06 2022-10-25 株式会社Lg新能源 Separator for lithium ion secondary battery and lithium metal battery including the same
JP7062462B2 (en) 2018-02-19 2022-05-06 株式会社東芝 Inorganic compound particles, composite electrolyte membranes, composite electrodes, secondary batteries, battery packs and vehicles
WO2019204244A1 (en) * 2018-04-16 2019-10-24 Board Of Regents, The University Of Texas System Electrochemical devices and methods of making and use thereof
KR102351623B1 (en) * 2018-05-14 2022-01-14 주식회사 엘지에너지솔루션 Separator without separator base member
KR102308942B1 (en) * 2018-07-26 2021-10-05 주식회사 엘지에너지솔루션 Separator and electrochemical device containing the same
CN109411675B (en) * 2018-10-30 2021-08-24 安徽金力新能源有限公司 Nickel-cobalt-manganese/nickel-cobalt-aluminum acid lithium battery, functional diaphragm for same and production process of diaphragm
CN113574729B (en) * 2019-03-20 2023-06-02 帝人株式会社 Separator for nonaqueous secondary battery and nonaqueous secondary battery
CN110212141A (en) * 2019-06-18 2019-09-06 林雨露 It is a kind of based on the lithium battery of polyethene microporous membrane new types of diaphragm material
KR102196914B1 (en) * 2019-08-22 2020-12-31 지머터리얼즈 주식회사 Composite separator for lithium secondary battery and method of manufacturing the same
CN112563664B (en) * 2019-09-26 2022-03-18 比亚迪股份有限公司 Diaphragm and lithium ion battery
CN112952295B (en) * 2019-11-26 2023-03-10 北京卫蓝新能源科技有限公司 Polyolefin-cellulose composite diaphragm and preparation method thereof
KR20210079234A (en) * 2019-12-19 2021-06-29 주식회사 엘지에너지솔루션 A separator for an electrochemical device and an electrochemical device comprising the separator and a method for manufacturing the electrochemical device
CN111192999A (en) * 2020-03-14 2020-05-22 东莞东阳光科研发有限公司 Lithium ion battery diaphragm and preparation method thereof
CN114079124B (en) * 2020-08-14 2022-12-13 中国科学院上海硅酸盐研究所 Organic-inorganic composite lithium ion battery diaphragm and preparation method thereof
CN112002939B (en) * 2020-08-31 2021-10-15 成都新柯力化工科技有限公司 Clean preparation method of lithium battery solid electrolyte
US20220267886A1 (en) * 2021-02-19 2022-08-25 GM Global Technology Operations LLC Melt spinning methods for forming lithium-metal foils and electrodes of electrochemical devices
CN113235300B (en) * 2021-05-06 2022-07-26 甘肃省民翔新能源科技有限公司 Preparation method of high-temperature-resistant lithium ion battery composite diaphragm
RU2762828C1 (en) * 2021-05-31 2021-12-23 федеральное государственное бюджетное образовательное учреждение высшего образования "Национальный исследовательский университет "МЭИ" (ФГБОУ ВО "НИУ "МЭИ") Gelpolymer electrolyte
CN113871794B (en) * 2021-09-14 2023-07-11 中国科学院上海硅酸盐研究所 Lithium-containing cyanamide compound/organic polymer composite electrochemical energy storage device diaphragm, and preparation method and application thereof
CN114395094B (en) * 2021-12-24 2023-12-19 乳源东阳光氟树脂有限公司 Organic-inorganic composite PVDF resin emulsion, coating liquid and preparation method thereof
CN114824273B (en) * 2022-04-15 2023-04-11 广东马车动力科技有限公司 Sulfide composite solid electrolyte membrane, preparation method thereof and solid battery

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5695873A (en) * 1995-06-05 1997-12-09 The University Of Dayton Polymer-ceramic composite electrolytes
US5858264A (en) * 1996-03-26 1999-01-12 Japan Gore-Tex, Inc. Composite polymer electrolyte membrane
US5882721A (en) * 1997-05-01 1999-03-16 Imra America Inc Process of manufacturing porous separator for electrochemical power supply
JPH1180395A (en) * 1997-09-09 1999-03-26 Nitto Denko Corp Porous film and separator for nonaqueous electrolyte cell or battery
US5965299A (en) * 1997-06-23 1999-10-12 North Carolina State University Composite electrolyte containing surface modified fumed silica
WO2000038263A1 (en) * 1998-12-22 2000-06-29 Finecell Co., Ltd. Microporous solid electrolytes and methods for preparing them
US6387564B1 (en) * 1997-02-28 2002-05-14 Asahi Kasei Kabushiki Kaisha Non-aqueous secondary battery having an aggregation layer
US6447958B1 (en) * 1998-04-27 2002-09-10 Sumitomo Chemical Co., Ltd. Non-aqueous electrolyte battery separator
US6632561B1 (en) * 1998-11-04 2003-10-14 Basf Aktiengesellschaft Composites bodies used as separators in electrochemical cells
US20080241566A1 (en) * 2007-03-30 2008-10-02 Frank Hoefflin Damping composition with improved bakability
US7662517B2 (en) * 2004-12-22 2010-02-16 Lg Chem, Ltd. Organic/inorganic composite microporous membrane and electrochemical device prepared thereby
US7682740B2 (en) * 2004-02-07 2010-03-23 Lg Chem, Ltd. Organic/inorganic composite porous layer-coated electrode and electrochemical device comprising the same
US7704641B2 (en) * 2004-07-07 2010-04-27 Lg Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US8409746B2 (en) * 2004-09-02 2013-04-02 Lg Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US20130101885A1 (en) * 2011-10-20 2013-04-25 Joo Sung Lee Method for manufacturing separator, separator manufactured by the method and method for manufacturing electrochemical device including the separator
US8715856B2 (en) * 2009-03-03 2014-05-06 Lg Chem, Ltd. Lithium secondary battery containing cathode materials having high energy density and organic/inorganic composite porous membrane
US8841031B2 (en) * 2004-12-07 2014-09-23 Lg Chem, Ltd. Surface-treated microporous membrane and electrochemical device prepared thereby

Family Cites Families (114)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4637990A (en) * 1978-08-28 1987-01-20 Torobin Leonard B Hollow porous microspheres as substrates and containers for catalysts and method of making same
JPS55165572A (en) 1979-06-12 1980-12-24 Toshiba Corp Zinc-alkaline secondary cell
JPS5632674A (en) 1979-08-23 1981-04-02 Toshiba Corp Cylindrical zinc alkaline secondary battery
JPS56132674A (en) 1980-03-19 1981-10-17 Fujitsu Ltd Photoelectric conversion device
US4540640A (en) * 1983-04-29 1985-09-10 The United States Of America As Represented By The United States Department Of Energy Coated powder for electrolyte matrix for carbonate fuel cell
US4615913A (en) 1984-03-13 1986-10-07 Kaman Sciences Corporation Multilayered chromium oxide bonded, hardened and densified coatings and method of making same
DK106788A (en) 1987-03-04 1988-09-05 New Brunswick Telephone Co LITHIUM-lithium nitride-ANODE
JPH0574466A (en) * 1991-09-17 1993-03-26 Kanegafuchi Chem Ind Co Ltd Solid electrolyte film
JPH05314995A (en) 1992-05-07 1993-11-26 Japan Energy Corp Electrolyte composite body
US5580834A (en) * 1993-02-10 1996-12-03 The Morgan Crucible Company Plc Self-sintered silicon carbide/carbon graphite composite material having interconnected pores which may be impregnated and raw batch and process for producing same
WO1994020995A2 (en) * 1993-03-01 1994-09-15 W.R. Grace & Co.-Conn. Battery separators
US5378551A (en) * 1993-07-19 1995-01-03 Motorola, Inc. Rechargeable battery cell having integral vibrating means
US5336573A (en) 1993-07-20 1994-08-09 W. R. Grace & Co.-Conn. Battery separator
JP3371301B2 (en) 1994-01-31 2003-01-27 ソニー株式会社 Non-aqueous electrolyte secondary battery
JPH07263028A (en) * 1994-03-25 1995-10-13 Fuji Photo Film Co Ltd Nonaqueous secondary battery
EP0848435B1 (en) 1995-08-28 2007-05-16 Asahi Kasei EMD Corporation Lithium battery and production method thereof
JPH0995700A (en) 1995-09-29 1997-04-08 Koronbusu:Kk Production of soft leather product and treating agent for soft leather
DE19612769A1 (en) 1996-03-29 1997-10-02 Basf Ag Mixtures suitable as carrier material for solid electrolytes or separators for electrochemical cells
JP3539570B2 (en) 1996-06-13 2004-07-07 旭化成エレクトロニクス株式会社 Hybrid electrolyte, method for producing the electrolyte, and method for producing an electrochemical device using the electrolyte
US5948464A (en) 1996-06-19 1999-09-07 Imra America, Inc. Process of manufacturing porous separator for electrochemical power supply
KR980011946A (en) 1996-07-18 1998-04-30 김광호 Method for manufacturing semiconductor memory device for ROM coding
KR19980011946U (en) 1996-08-23 1998-05-25 김종진 Support for turning workpieces on lathes
US6447951B1 (en) 1996-09-23 2002-09-10 Valence Technology, Inc. Lithium based phosphates, method of preparation, and uses thereof
JPH10241656A (en) 1997-02-28 1998-09-11 Asahi Chem Ind Co Ltd Battery
FR2766295B1 (en) * 1997-07-17 1999-09-24 Alsthom Cge Alcatel POLYMERIC SEPARATOR, MANUFACTURING PROCESS AND ELECTROCHEMICAL GENERATOR INCLUDING IT
CN1155129C (en) 1997-08-08 2004-06-23 日本电池株式会社 Method for producing electrode for non-water electrolyte battery
US6656641B1 (en) * 1997-08-21 2003-12-02 University Of Dayton Methods of enhancing conductivity of a polymer-ceramic composite electrolyte
US6153337A (en) 1997-12-19 2000-11-28 Moltech Corporation Separators for electrochemical cells
CN1125498C (en) 1998-01-19 2003-10-22 三菱电机株式会社 Battery
FR2777698B1 (en) 1998-04-16 2000-05-12 Alsthom Cge Alcatel SEPARATOR COMPRISING A MACROPOROUS MATRIX AND A POROUS POLYMER, ITS MANUFACTURING METHOD, ELECTROCHEMICAL GENERATOR COMPRISING SAME AND THE MANUFACTURING METHOD THEREOF
US6281257B1 (en) * 1998-04-27 2001-08-28 The Regents Of The University Of Michigan Porous composite materials
KR20000019372A (en) * 1998-09-10 2000-04-06 박호군 Solid polymer alloy electrolyte of homogeneous phase, complex electrode using the electrolyte, lithium polymer battery, lithium ion polymer battery and manufacturing method thereof
US6194098B1 (en) 1998-12-17 2001-02-27 Moltech Corporation Protective coating for separators for electrochemical cells
US6277514B1 (en) * 1998-12-17 2001-08-21 Moltech Corporation Protective coating for separators for electrochemical cells
JP2000228223A (en) 1999-02-05 2000-08-15 Tokuyama Corp Non-aqueous electrolyte secondary cell
KR100326457B1 (en) 1999-03-10 2002-02-28 김순택 A positive active material for a lithium secondary battery and a method of preparing the same
KR100326455B1 (en) 1999-03-30 2002-02-28 김순택 Positive active material for lithium secondary battery and method of preparing the same
WO2000060683A1 (en) 1999-03-31 2000-10-12 Koninklijke Philips Electronics N.V. Microporous electrode or separator for use in a non-aqueous battery, and method of manufacturing
JP3643289B2 (en) 1999-04-30 2005-04-27 株式会社オハラ Glass ceramic composite electrolyte and lithium secondary battery
EP1115166A4 (en) * 1999-06-22 2004-09-15 Mitsubishi Electric Corp Separator for cell, cell, and method for producing separator
CN1157817C (en) 1999-08-14 2004-07-14 惠州Tcl金能电池有限公司 Compound polymer dielectric membrane and lithium batttery made by using said membrane
US20020102456A1 (en) 1999-09-20 2002-08-01 Mitsubishi Denki Kabushiki Kaisha Battery
US20030170536A1 (en) * 1999-09-22 2003-09-11 Mitsubishi Denki Kabushiki Kaisha Bttery with adhesion resin layer including filler
US6328770B1 (en) 1999-11-23 2001-12-11 Valence Technology (Nevada), Inc. Method of making multi-layer electrochemical cell devices
KR20020086858A (en) 1999-12-09 2002-11-20 엔티케이 파워덱스 인코포레이티드 Battery separator for li-ion and/or li-ion polymer battery
JP4563537B2 (en) 1999-12-22 2010-10-13 日本板硝子株式会社 Sealed lead-acid battery separator
US6623886B2 (en) 1999-12-29 2003-09-23 Kimberly-Clark Worldwide, Inc. Nickel-rich quaternary metal oxide materials as cathodes for lithium-ion and lithium-ion polymer batteries
US6830849B2 (en) * 2000-01-10 2004-12-14 Lg Chemical Co., Ltd. High crystalline polypropylene microporous membrane, multi-component microporous membrane and methods for preparing the same
JP2001273898A (en) * 2000-01-20 2001-10-05 Japan Storage Battery Co Ltd Positive active material for nonaqueous electrolyte secondary battery, method of manufacturing same, and nonaqueous electrolyte secondary battery using the active material
KR100497147B1 (en) 2000-02-08 2005-06-29 주식회사 엘지화학 Multiply stacked electrochemical cell and method for preparing the same
US6503432B1 (en) * 2000-03-02 2003-01-07 E. I. Du Pont De Nemours And Company Process for forming multilayer articles by melt extrusion
US7094497B2 (en) 2000-03-07 2006-08-22 Teijin Limited Separator for lithium ion secondary battery
TW499766B (en) * 2000-03-29 2002-08-21 Elite Ionergy Co Ltd Battery manufacturing method
US6432586B1 (en) * 2000-04-10 2002-08-13 Celgard Inc. Separator for a high energy rechargeable lithium battery
KR100362280B1 (en) * 2000-04-11 2002-11-23 삼성에스디아이 주식회사 Separator for lithium secondary battery and the method thereof
JP2002008724A (en) 2000-06-23 2002-01-11 Ryoji Mishima Nano-particle composite polymer electrolyte and lithium secondary battery using this
KR100374010B1 (en) 2000-07-12 2003-02-26 한국과학기술연구원 Powders for Metallic Oxide Electrodes and Method for Preparing the Same
US6730439B2 (en) 2000-08-01 2004-05-04 Tonen Tapyrus Co., Ltd. Heat-resistant separator
JP3885100B2 (en) 2000-08-12 2007-02-21 エルジー・ケミカル・カンパニー・リミテッド Multi-component composite film and method for producing the same
JP4799776B2 (en) * 2000-08-22 2011-10-26 富士フイルム株式会社 Electrolyte composition and electrochemical cell using the same
JP4487457B2 (en) 2000-08-30 2010-06-23 住友化学株式会社 Nonaqueous electrolyte secondary battery separator and nonaqueous electrolyte secondary battery
US20020160256A1 (en) * 2000-09-21 2002-10-31 Kenichiro Kami Non-aqueous electrolyte secondary battery
JP4020296B2 (en) * 2000-12-21 2007-12-12 キヤノン株式会社 Ionic conduction structure, secondary battery and method for producing them
WO2002061874A1 (en) 2001-01-31 2002-08-08 Korea Institute Of Science And Technology A multi-layered, uv-cured polymer electrolyte and lithium secondary battery comprising the same
JP2002256093A (en) 2001-02-28 2002-09-11 Nitto Denko Corp Porous film, production method thereof and usage thereof
KR100406690B1 (en) 2001-03-05 2003-11-21 주식회사 엘지화학 Electrochemical device using multicomponent composite membrane film
KR100399785B1 (en) 2001-04-07 2003-09-29 삼성에스디아이 주식회사 Separators for winding-type lithium secondary batteries comprising gel-type polymer electrolytes and manufacturing method for the same
CN1137192C (en) 2001-05-11 2004-02-04 崔蔚 Organic compound material containing inorganic nano material, its preparation method and use
US20020185627A1 (en) * 2001-05-29 2002-12-12 Chung Yuan Christian University Solid composite polymer electrolyte
JP4981220B2 (en) 2001-06-21 2012-07-18 帝人株式会社 Non-aqueous secondary battery separator and non-aqueous secondary battery
JP2003022707A (en) 2001-07-06 2003-01-24 National Institute For Materials Science Lithium ion conductive solid electrolyte molding and lithium battery using the same
JP5082177B2 (en) * 2001-08-16 2012-11-28 株式会社Gsユアサ Battery separator and battery using the same
KR100424194B1 (en) 2001-11-01 2004-03-24 한국과학기술연구원 Electrode part having microstructure of extended triple phase boundary by porous ion conductive ceria film coating and Method to manufacture the said electrode
KR20030065074A (en) 2002-01-29 2003-08-06 주식회사 뉴턴에너지 Electrochemical Cell And Method Of Manufacturing The Same
US20030157409A1 (en) * 2002-02-21 2003-08-21 Sui-Yang Huang Polymer lithium battery with ionic electrolyte
RU2218634C2 (en) 2002-02-26 2003-12-10 ООО Инженерная фирма "Орион ХИТ" Lithium cell
KR100454716B1 (en) * 2002-04-03 2004-11-05 한국과학기술연구원 Aqueous ceramic slurry using acrylic emulsion as a binding agent and method for producing a ceramic tape using the same
KR100449761B1 (en) 2002-05-18 2004-09-22 삼성에스디아이 주식회사 Lithium secondary battery inhibiting decomposition of electrolytic solution and manufacturing method thereof
KR100477885B1 (en) 2002-07-08 2005-03-18 베스 주식회사 Method of making lithium ion polymer battery and porous polymeric electrolte
JP2004063394A (en) * 2002-07-31 2004-02-26 Sanyo Electric Co Ltd Nonaqueous electrolyte battery
KR100495567B1 (en) 2002-08-14 2005-06-16 한국과학기술원 Lithium/Sulfur Rechargeable Battery Comprising Electrode Composition Based on Vinylidene Fluoride Polymer as A Binder, and Preparation Method thereof
DE10240032A1 (en) 2002-08-27 2004-03-11 Creavis Gesellschaft Für Technologie Und Innovation Mbh Ion-conducting battery separator for lithium batteries, process for their production and their use
KR100467696B1 (en) * 2002-08-31 2005-01-24 삼성에스디아이 주식회사 Organic electrolytic solution and lithium battery employing the same
JP4344121B2 (en) * 2002-09-06 2009-10-14 パナソニック株式会社 Anode material for non-aqueous electrolyte secondary battery and non-aqueous electrolyte secondary battery
KR100467705B1 (en) * 2002-11-02 2005-01-24 삼성에스디아이 주식회사 Seperator having inorganic protective film and lithium battery using the same
KR20030007659A (en) 2002-11-20 2003-01-23 주식회사 파인셀 Microporous Inorganic Solid Electrolytes and Methods for Preparing Them
DE10255121B4 (en) * 2002-11-26 2017-09-14 Evonik Degussa Gmbh Separator with asymmetric pore structure for an electrochemical cell
JP4792688B2 (en) 2003-01-24 2011-10-12 住友化学株式会社 Method for producing separator for non-aqueous electrolyte secondary battery
JP4563039B2 (en) 2003-02-21 2010-10-13 パナソニック株式会社 Lithium ion secondary battery
US7115339B2 (en) * 2003-02-21 2006-10-03 Matsushita Electric Industrial Co., Ltd. Lithium ion secondary battery
KR100496642B1 (en) 2003-04-25 2005-06-20 한국전자통신연구원 Composite polymer electrolytes including single-ion conductor for lithium rechargeable battery and method for preparing the same
DE10347569A1 (en) * 2003-10-14 2005-06-02 Degussa Ag Ceramic, flexible membrane with improved adhesion of the ceramic on the carrier fleece
KR100551005B1 (en) 2003-10-21 2006-02-13 삼성에스디아이 주식회사 Positive electrode for lithium-sulfur battery and lithium-sulfur battery comprising same
JP2005146243A (en) 2003-11-17 2005-06-09 Iwao Jiki Kogyo Kk Resin composite porous material
KR100610261B1 (en) 2003-12-26 2006-08-09 주식회사 엘지화학 Lithium secondary battery with a different kind of separators
WO2005067080A1 (en) 2004-01-09 2005-07-21 Matsushita Electric Industrial Co., Ltd. Lithium ion secondary cell
DE602005011264D1 (en) * 2004-02-18 2009-01-08 Panasonic Corp SECONDARY BATTERY
JP2005276503A (en) 2004-03-23 2005-10-06 Mitsubishi Electric Corp Separator for battery and battery using the same
US7604895B2 (en) 2004-03-29 2009-10-20 Lg Chem, Ltd. Electrochemical cell with two types of separators
JP4794824B2 (en) 2004-04-05 2011-10-19 パナソニック株式会社 Lithium ion secondary battery and manufacturing method thereof
JP4763253B2 (en) 2004-05-17 2011-08-31 パナソニック株式会社 Lithium ion secondary battery
CN100452487C (en) 2004-06-22 2009-01-14 松下电器产业株式会社 Secondary battery and method for producing the same
KR100739337B1 (en) 2004-09-02 2007-07-12 주식회사 엘지화학 Organic/inorganic composite porous film and electrochemical device prepared thereby
WO2006112243A1 (en) 2005-04-15 2006-10-26 Matsushita Electric Industrial Co., Ltd. Rectangular lithium secondary battery
KR100858214B1 (en) 2005-06-27 2008-09-10 주식회사 엘지화학 Bi-layered organic/inorganic composite microporous separator with heterogeneous surface and electrochemical device using the same
KR100933427B1 (en) 2005-08-16 2009-12-23 주식회사 엘지화학 Electrochemical device consisting of cross separator
JP5211695B2 (en) 2006-02-01 2013-06-12 ダイキン工業株式会社 High dielectric film
TWI346406B (en) * 2006-02-16 2011-08-01 Lg Chemical Ltd Lithium secondary battery with enhanced heat-resistance
US20090273119A1 (en) * 2006-03-10 2009-11-05 Tetsuya Imai Imprint Method and Imprint Apparatus
KR100791791B1 (en) * 2006-03-10 2008-01-04 주식회사 엘지화학 Electrode having porous active coating layer, and manufacturing method thereof and electrochemical device containing the same
KR100727248B1 (en) 2007-02-05 2007-06-11 주식회사 엘지화학 Organic/inorganic composite separator having porous active coating layer and electrochemical device containing the same
JP5339305B2 (en) * 2008-11-26 2013-11-13 パナソニック株式会社 Nitrogen oxide detection element
WO2011019187A2 (en) * 2009-08-10 2011-02-17 주식회사 엘지화학 Lithium secondary battery
WO2013168313A1 (en) 2012-05-11 2013-11-14 ポリプラスチックス株式会社 Resin composition for light-reflective component

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5695873A (en) * 1995-06-05 1997-12-09 The University Of Dayton Polymer-ceramic composite electrolytes
US5858264A (en) * 1996-03-26 1999-01-12 Japan Gore-Tex, Inc. Composite polymer electrolyte membrane
US6387564B1 (en) * 1997-02-28 2002-05-14 Asahi Kasei Kabushiki Kaisha Non-aqueous secondary battery having an aggregation layer
US5882721A (en) * 1997-05-01 1999-03-16 Imra America Inc Process of manufacturing porous separator for electrochemical power supply
US5965299A (en) * 1997-06-23 1999-10-12 North Carolina State University Composite electrolyte containing surface modified fumed silica
JPH1180395A (en) * 1997-09-09 1999-03-26 Nitto Denko Corp Porous film and separator for nonaqueous electrolyte cell or battery
US6447958B1 (en) * 1998-04-27 2002-09-10 Sumitomo Chemical Co., Ltd. Non-aqueous electrolyte battery separator
US6632561B1 (en) * 1998-11-04 2003-10-14 Basf Aktiengesellschaft Composites bodies used as separators in electrochemical cells
WO2000038263A1 (en) * 1998-12-22 2000-06-29 Finecell Co., Ltd. Microporous solid electrolytes and methods for preparing them
US7682740B2 (en) * 2004-02-07 2010-03-23 Lg Chem, Ltd. Organic/inorganic composite porous layer-coated electrode and electrochemical device comprising the same
US7704641B2 (en) * 2004-07-07 2010-04-27 Lg Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US8409746B2 (en) * 2004-09-02 2013-04-02 Lg Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US9490463B2 (en) * 2004-09-02 2016-11-08 Lg Chem, Ltd. Organic/inorganic composite porous film and electrochemical device prepared thereby
US8841031B2 (en) * 2004-12-07 2014-09-23 Lg Chem, Ltd. Surface-treated microporous membrane and electrochemical device prepared thereby
US7662517B2 (en) * 2004-12-22 2010-02-16 Lg Chem, Ltd. Organic/inorganic composite microporous membrane and electrochemical device prepared thereby
US20080241566A1 (en) * 2007-03-30 2008-10-02 Frank Hoefflin Damping composition with improved bakability
US8715856B2 (en) * 2009-03-03 2014-05-06 Lg Chem, Ltd. Lithium secondary battery containing cathode materials having high energy density and organic/inorganic composite porous membrane
US20130101885A1 (en) * 2011-10-20 2013-04-25 Joo Sung Lee Method for manufacturing separator, separator manufactured by the method and method for manufacturing electrochemical device including the separator

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Declaration Under 37 CFR 1.132 filed on 7/15/2011 in the US family member application 11/217,918 *

Also Published As

Publication number Publication date
US20180166671A1 (en) 2018-06-14
US20190229316A1 (en) 2019-07-25
US9490463B2 (en) 2016-11-08
US20210320380A1 (en) 2021-10-14
US20110281172A1 (en) 2011-11-17
US8409746B2 (en) 2013-04-02
EP1784876B1 (en) 2018-01-24
EP1784876A1 (en) 2007-05-16
EP3745494A1 (en) 2020-12-02
EP1784876A4 (en) 2011-05-11
US20060046149A1 (en) 2006-03-02
WO2006025662A1 (en) 2006-03-09
EP3322000A1 (en) 2018-05-16
US20130183570A1 (en) 2013-07-18

Similar Documents

Publication Publication Date Title
US20210320380A1 (en) Organic/inorganic composite porous film and electrochemical device prepared thereby
US7704641B2 (en) Organic/inorganic composite porous film and electrochemical device prepared thereby
US20110281171A1 (en) Organic/inorganic composite porous film and electrochemical device prepared thereby
KR100895196B1 (en) Organic/inorganic composite porous film and electrochemical device prepared thereby
US7662517B2 (en) Organic/inorganic composite microporous membrane and electrochemical device prepared thereby
US7638241B2 (en) Organic/inorganic composite separator having morphology gradient, manufacturing method thereof and electrochemical device containing the same
KR100749301B1 (en) New organic/inorganic composite porous film and electrochemical device prepared thereby
KR100742959B1 (en) Organic/inorganic composite porous film and electrochemical device using the same
KR100739337B1 (en) Organic/inorganic composite porous film and electrochemical device prepared thereby
US20110318141A1 (en) Substrate transfer equipment and high speed substrate processing system using the same
KR20060041650A (en) Organic/inorganic composite porous film and electrochemical device prepared thereby

Legal Events

Date Code Title Description
STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION