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WO2017033993A1 - Séparateur de piles et son procédé de fabrication - Google Patents

Séparateur de piles et son procédé de fabrication Download PDF

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Publication number
WO2017033993A1
WO2017033993A1 PCT/JP2016/074774 JP2016074774W WO2017033993A1 WO 2017033993 A1 WO2017033993 A1 WO 2017033993A1 JP 2016074774 W JP2016074774 W JP 2016074774W WO 2017033993 A1 WO2017033993 A1 WO 2017033993A1
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Prior art keywords
plate
battery separator
substantially spherical
spherical organic
organic particles
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PCT/JP2016/074774
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English (en)
Japanese (ja)
Inventor
水野　直樹
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東レバッテリーセパレータフィルム株式会社
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Priority to CN201680043565.5A priority Critical patent/CN107925034B/zh
Priority to KR1020187004801A priority patent/KR102187519B1/ko
Priority to JP2017536475A priority patent/JP6669174B2/ja
Publication of WO2017033993A1 publication Critical patent/WO2017033993A1/fr

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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403—Manufacturing processes of separators, membranes or diaphragms
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/446—Composite material consisting of a mixture of organic and inorganic materials
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403—Manufacturing processes of separators, membranes or diaphragms
    • H01M50/406—Moulding; Embossing; Cutting
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417—Polyolefins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/42—Acrylic resins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/426—Fluorocarbon polymers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/431—Inorganic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/443—Particulate material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/451—Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/491—Porosity
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention is a battery separator suitable for a lithium ion secondary battery having a high volumetric energy density, comprising a porous layer having adhesion to an electrode material and a polyolefin microporous film.
  • Polyolefin microporous membranes typified by polyethylene microporous membranes have excellent electrical insulation properties, ion permeability, electrolyte resistance, and oxidation resistance due to electrolyte impregnation, and an abnormal battery temperature rise of about 120 to 150 ° C.
  • the microporous membrane has a shutdown characteristic that closes the pores of the microporous membrane and cuts off the current to suppress excessive temperature rise, and is suitably used as a separator for non-aqueous electrolyte secondary batteries.
  • the viscosity of the polyolefin decreases and the microporous membrane contracts, which may cause membrane breakage of the microporous membrane.
  • lithium-ion battery separators are deeply involved in battery characteristics, battery productivity, and battery safety, and require permeability, mechanical characteristics, heat resistance, shutdown characteristics, melt-breaking characteristics (meltdown characteristics), etc.
  • improvements in adhesion to electrode materials from the viewpoint of battery cycle characteristics, and improvements in electrolyte permeability from the viewpoint of productivity have been required. Improvements in functionality are being considered.
  • the electrode body in which the negative electrode, the separator, and the positive electrode are superimposed can be filled in the container at a high density. Rather, it is predicted that a high density winding property is required.
  • Patent Document 1 in order to improve adhesion to an electrode material, a coating solution containing inorganic particles such as aluminum hydroxide oxide having an average particle diameter of 1 to 1.8 ⁇ m and an acrylic latex is used.
  • An inorganic filler layer having a thickness of 2 to 7 ⁇ m is laminated on one side of a polyolefin resin porous membrane having a thickness of 9 to 18 ⁇ m, and two types of acrylic resins having an average particle diameter of 60 to 161 nm and different glass transition temperatures (Tg) are contained on both sides.
  • Tg glass transition temperatures
  • Patent Document 2 discloses a coating solution in which a fine particle containing a vinylidene fluoride-acrylic copolymer resin having an average particle diameter of 250 nm, inorganic particles or organic particles having an average particle diameter of 200 to 1800 nm, and an aqueous emulsion is mixed with a film thickness of 9
  • the present invention assumes that the capacity of the battery will increase further in the future, and even when the battery separator is thinned, it has adhesiveness with the electrode material and unnecessary space between the electrode material and the separator. Aiming to provide a battery separator particularly suitable for lithium ion secondary battery separators, which can increase the number of windings and the number of layers of the electrode body by minimizing the number of electrodes and obtain an electrode body with a high volume energy density. It is a thing.
  • the battery separator of the present invention has the following configuration. That is, (1) It has a polyolefin microporous film, and a substantially spherical organic particle made of an acrylic resin or a fluorine resin and a porous layer containing a plate-like inorganic particle on at least one surface, and the substantially spherical organic particle is in the film thickness direction.
  • the ratio (r / t) between the average particle diameter r ( ⁇ m) of the substantially spherical organic particles and the average thickness t ( ⁇ m) of the plate-like inorganic particles is Satisfactory battery separator. 0.1 ⁇ m ⁇ r ⁇ 0.8 ⁇ m ...
  • the plate-like inorganic particles are preferably alumina or boehmite.
  • the volume of the substantially spherical organic particles is preferably 10 to 30% by volume with respect to the total volume of the substantially spherical organic particles and the plate-like inorganic particles.
  • the battery separator of the present invention is preferably a lithium ion secondary battery separator.
  • the battery separator manufacturing method of the present invention has the following configuration. That is, (5) A battery separator manufacturing method including the following steps (a) and (b) in sequence.
  • the viscosity of the coating liquid A is preferably 10 to 30 mPa ⁇ s.
  • the viscosity of the coating liquid B is preferably 1 to 10 mPa ⁇ s.
  • the present invention assumes that the capacity of the battery will increase further in the future, and even when the battery separator is thinned, it has adhesiveness with the electrode material and unnecessary space between the electrode material and the separator. It is a battery separator particularly suitable for a lithium ion secondary battery separator, which can increase the number of windings and the number of laminated layers of the electrode body by minimizing the amount of electrode and obtain an electrode body having a high volume energy density.
  • the polyolefin microporous membrane preferably contains a polyolefin resin having a melting point (softening point) of 70 to 150 ° C. from the viewpoint of the function of blocking the pores when the charge / discharge reaction is abnormal.
  • the polyolefin resin may be a single substance such as polyethylene or polypropylene, a mixture thereof, a mixture of two or more different polyolefin resins, or a copolymer of different olefins.
  • polyethylene resin is preferable from the viewpoint of the function of blocking the pores.
  • the polyolefin microporous film may be a single layer or a multilayer film composed of two or more layers having different molecular weights or average pore diameters.
  • a method for producing a multilayer film composed of two or more layers for example, the polyolefin resin constituting the A1 layer or the A2 layer is melt-kneaded with a film-forming solvent, and the resulting molten mixture is sent from each extruder to one die. It is possible to produce either a method in which gel sheets constituting each component are integrated and co-extruded or a method in which gel sheets constituting each layer are superposed and heat-sealed.
  • the coextrusion method is more preferable because it is easy to obtain a high interlayer adhesive strength, and it is easy to form communication holes between layers, so that high permeability is easily maintained and productivity is excellent.
  • the film thickness of the polyolefin microporous membrane is preferably 3 ⁇ m or more and less than 10 ⁇ m, more preferably 5 ⁇ m or more and less than 9.0 ⁇ m, and even more preferably 6 ⁇ m or more and 8 ⁇ m, from the viewpoint of increasing the volume energy of the battery that will be advanced in the future. Is less than.
  • the average pore diameter of the polyolefin microporous membrane is 0.01 to 1.0 ⁇ m, preferably 0.05 to 0.5 ⁇ m, more preferably 0.1 to 0.3 ⁇ m, from the viewpoint of the pore closing speed and the pore closing temperature. .
  • the average pore diameter of the polyolefin microporous membrane is within the above-mentioned preferable range, the anchoring effect by the resin of the porous layer can be obtained without significantly deteriorating the air resistance when the porous layer is laminated.
  • the air permeability resistance of the polyolefin microporous membrane is preferably 50 to 500 sec / 100 cc Air.
  • the porosity of the polyolefin microporous membrane is preferably 30 to 70%.
  • the porous layer includes plate-like inorganic particles and substantially spherical organic particles.
  • the plate-like inorganic particles play a role of reinforcing the polyolefin microporous membrane by its heat resistance and improving the melt-breaking properties.
  • the substantially spherical organic particles play a role of improving the adhesion with the electrode material and improving the cycle characteristics when incorporated in a battery.
  • the porous layer is formed by sequentially applying a coating liquid A containing plate-like inorganic particles and a coating liquid B containing substantially spherical organic particles to a polyolefin microporous film.
  • the coating liquid A contains plate-like inorganic particles and a dispersion medium, and may contain a binder as necessary.
  • the material of the plate-like inorganic particles is not particularly limited, but alumina, boehmite, and mica are relatively easily available and suitable.
  • boehmite is preferable from the viewpoint that the hardness is low and wear of a coating roll or the like can be suppressed.
  • plate-like inorganic particles refers to particles having an aspect ratio (major axis / thickness) of 1.5 or more and a major axis / minor axis ratio of 1 to 10.
  • the lower limit of the aspect ratio of the plate-like inorganic particles is preferably 2, more preferably 3, and still more preferably 5.
  • the upper limit is preferably 50, more preferably 20, and even more preferably 10.
  • the average particle size (average major axis) of the plate-like inorganic particles is preferably 0.5 ⁇ m to 2.0 ⁇ m, and the average thickness is preferably 0.1 ⁇ m or more and less than 0.5 ⁇ m.
  • the plate-like inorganic particles can be easily arranged in a direction substantially parallel to the plane direction of the polyolefin microporous membrane.
  • the porous layer can be filled with a relatively high density, and generation of coarse voids and surface protrusions exceeding 1 ⁇ m in size can be suppressed in the porous layer.
  • the average value of the ratio of the long axis direction length to the short axis direction length (major axis / minor axis) of the plate-like inorganic particles is preferably 3 or less, more preferably 2 or less and a value close to 1. .
  • the binder is not particularly limited as long as it provides the adhesion between the polyolefin microporous membrane and the porous layer and adheres the plate-like inorganic particles.
  • a water-soluble resin or a water-dispersible resin is preferable.
  • the water-soluble resin or water-dispersible resin include acrylic resins such as polyvinyl alcohol, polyacrylic acid, polyacrylamide, and polymethacrylic acid.
  • polyvinyl alcohol and acrylic resin are preferable.
  • acrylic resin commercially available acrylic emulsions can be used. For example, “Acryset” (registered trademark) TF-300 manufactured by Nippon Shokubai Co., Ltd., “Polysol” (registered trademark) AP manufactured by Showa Denko K.K. -4735.
  • the dispersion medium of the coating liquid A contains water as a main component, and ethyl alcohol, butyl alcohol, or the like may be added to improve the coating property. Furthermore, you may add a binder, a dispersing agent, and a thickener as needed.
  • the viscosity of the coating liquid A is preferably 10 to 30 mPa ⁇ s, more preferably 12 to 25 mPa ⁇ s, and still more preferably 15 to 25 mPa ⁇ s.
  • the content of the plate-like inorganic particles in the coating liquid A is preferably 40 to 60% by mass. When the viscosity of the coating liquid A and the content of the plate-like inorganic particles are within the above preferable ranges, the plate-like inorganic particles can be made substantially parallel to the plane direction of the polyolefin microporous membrane.
  • the coating amount is preferably 1 g / m 2 or more and 3 g / m 2 or less in consideration of the volume energy density when the wound body is used as a film breaking strength or an electrode body.
  • the coating liquid B contains substantially spherical organic particles and a dispersion medium, and may contain a binder as necessary.
  • the circularity of the substantially spherical organic particles is 0.97 or more, preferably 0.98 or more, and most preferably 0.99 to 1.00.
  • L0 in the above equation is the perimeter of an ideal circle (perfect circle) having the same area as the area calculated from the projection image (particle image) of the target particle actually measured, and L1 is the measurement. This is the actual perimeter measured from the particle projection image (particle image) of the target particle.
  • the lower limit of the average particle diameter (r) of the substantially spherical organic particles is preferably 0.1 ⁇ m, more preferably 0.2 ⁇ m, and still more preferably 0.3 ⁇ m.
  • the upper limit is preferably 0.8 ⁇ m, more preferably 0.7 ⁇ m, and even more preferably 0.6 ⁇ m. If the average particle size (r) is less than 0.1 ⁇ m, it may penetrate into the gaps between the plate-like inorganic particles as far as possible, and may not sufficiently contribute to the improvement in adhesion to the electrode material. If it exceeds 0.8 ⁇ m, it tends to fall off, which is not preferable.
  • the substantially spherical organic particles preferably contain a fluorine resin, an acrylic resin, or both.
  • the fluororesin is at least one selected from the group consisting of vinylidene fluoride homopolymers, vinylidene fluoride / fluorinated olefin copolymers, vinyl fluoride homopolymers, and vinyl fluoride / fluorinated olefin copolymers. Can be used.
  • a vinylidene fluoride / hexafluoropropylene copolymer is preferable from the viewpoint of adhesion to an electrode material.
  • the mol% of hexafluoropropylene is more preferably 1 to 3 mol%.
  • This polymer has excellent adhesion to electrode materials, moderate swelling with non-aqueous electrolytes, and high chemical and physical stability against non-aqueous electrolytes. Affinity with the electrolytic solution can be sufficiently maintained even when used in
  • fluororesin a commercially available fluororesin can be used after being refined into a spherical shape if necessary.
  • examples of commercially available fluororesins include KYNAR FREX (registered trademark) 2851-00, 2801-00, 2821-00, 2501-20 and the like manufactured by ARKEMA.
  • the acrylic resin is not particularly limited as long as it has adhesiveness with the electrode material, but a resin obtained by polymerizing an acrylate monomer is preferable.
  • the acrylate monomer include methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl meth (acrylate), isopyl pill (meth) acrylate, n-butyl (meth) acrylate, and t-butyl (meth) acrylate.
  • De port carboxymethyl group-containing (meth) acrylate De port carboxymethyl group-containing (meth) acrylate.
  • a coating liquid in which commercially available acrylic resin particles are dispersed may be used.
  • examples of the coating liquid in which commercially available acrylic resin particles are dispersed include ASR latex product name: TRD202A manufactured by JSR Corporation.
  • Non-crosslinked organic particles are preferred from the viewpoint of adhesion to the electrode material.
  • the dispersion medium of the coating liquid B contains water as a main component, and ethyl alcohol, butyl alcohol, or the like may be added as necessary in order to improve coating properties. Furthermore, you may add a binder, a dispersing agent, and a thickener as needed.
  • the binder is not particularly limited as long as it imparts adhesion between the polyolefin microporous membrane and the porous layer and adheres substantially spherical organic particles.
  • the same binder as the first layer can be used.
  • the viscosity of the coating liquid B is preferably 1 to 10 mPa ⁇ s, more preferably 2 to 8 mPa ⁇ s, and further preferably 3 to 6 mPa ⁇ s.
  • the content of the substantially spherical organic particles in the coating liquid B is preferably 3 to 10% by mass.
  • the substantially spherical organic particles roll on the plate-like inorganic particles, and the surface recesses between the plate-like inorganic particles are likely to enter. As shown in 1 and 2, it becomes easy to obtain a sea-island structure state of aggregates of substantially spherical organic particles and plate-like inorganic particles.
  • the volume of the substantially spherical organic particles is preferably 10 to 30% by volume with respect to the total volume of the substantially spherical organic particles and the plate-like inorganic particles. If it is 10 volume% or more, the function which provides or improves the adhesiveness with an electrode material will be easy to be obtained. If it is 30% by volume or less, a relatively large content of the plate-like inorganic particles can be maintained, and sufficient film breaking strength can be easily obtained.
  • the ratio (r / t) of the average particle diameter r ( ⁇ m) of the substantially spherical organic particles to the average thickness t ( ⁇ m) of the plate-like inorganic particles is set within the range of 0.3 ⁇ r / t ⁇ 1.0. is important. Within the above preferable range, when the coating liquid B is applied to the plate-like inorganic particle layer, the substantially spherical organic particles roll on the surface of the plate-like inorganic particle layer and easily enter the recesses of the plate-like inorganic particle layer.
  • the cross section of the porous layer has a form in which the substantially spherical organic particles enter the recesses on the surface of the plate-like inorganic particle layer so as to have adhesiveness with the electrode (see FIG. 1).
  • the surface of the porous layer is magnified, almost spherical organic particles are present so as to fill the recesses on the surface of the plate-like inorganic particle layer, and an aggregate of plate-like inorganic particles and spherical organic particles is observed. It has a form (see FIG. 2).
  • FIG. 2 shows an example in which the plate-like inorganic particles are islands and the aggregate of spherical organic particles is the sea.
  • the porous layer has a sea-island structure, the adhesion with the electrode material can be improved while suppressing an increase in the thickness of the porous layer. If it is strong, it leads to the improvement of the volume energy density of the battery obtained.
  • the thickness of the porous layer varies depending on the intended use of the obtained battery, but is preferably 0.5 to 2.5 ⁇ m, more preferably 0.8 to 2.2 ⁇ m, and still more preferably 1.0 to 2.0 ⁇ m. is there. Adhesiveness with an electrode material can be provided or improved as the film thickness of the porous layer is within the above preferred range.
  • the membrane breaking strength when the polyolefin microporous membrane is melted / shrinked at a temperature equal to or higher than the melting point of the polyolefin can be maintained, and insulation can be secured. Further, a high volume energy density can be obtained when a wound body is used as the electrode body.
  • the porosity of the porous layer is preferably 30 to 90% from the viewpoint of the electric resistance and film strength of the film.
  • the air resistance of the porous layer is preferably 1 to 600 sec / 100 cc Air measured by a method based on JIS P 8117 from the viewpoint of film strength and cycle characteristics.
  • the battery separator of the present invention is obtained by applying a coating liquid A containing plate-like inorganic particles and a coating liquid B containing substantially spherical organic particles to a polyolefin microporous film.
  • the coating liquid A is applied to the polyolefin microporous membrane so that the plate-like inorganic particles are substantially parallel to the polyolefin microporous membrane, and dried to form a plate-like inorganic particle layer.
  • the direction of the plate-like inorganic particles becomes irregular, and voids exceeding 1 ⁇ m in size are easily formed in the porous layer, and plate-like inorganic particles that are not substantially parallel are easily generated as protrusions on the surface, and the electrode body. As a result, voids are likely to occur.
  • the coating liquid B may be applied only on the plate-like inorganic particle layer, or may be applied to the other surface of the polyolefin microporous film not provided with the plate-like inorganic particle layer. In order to obtain adhesiveness with the electrode material, it is sufficient that the substantially spherical organic particles of the coating liquid B can be applied so as to be unevenly distributed on the surface.
  • a well-known method can be adopted as the wet coating method.
  • examples thereof include a roll coating method, a gravure coating method, a kiss coating method, a dip coating method, a spray coating method, an air knife coating method, a Meyer bar coating method, a pipe doctor method, a blade coating method, and a die coating method.
  • a method of applying a relatively strong shearing force to the coating solution on the polyolefin microporous film is preferable, and among the roll coating method and the gravure coating method, the reverse roll coating method and the reverse gravure coating method are preferable.
  • the rotation direction of the coating roll relative to the traveling direction of the polyolefin microporous membrane is opposite, so that a strong shearing force can be applied to the coating liquid, and the plate-like inorganic particles are applied to the polyolefin microporous membrane. It can be made to be substantially parallel to it.
  • the ratio between the conveying speed (F) of the polyolefin microporous membrane and the peripheral speed (S) of the coating roll rotating in reverse (hereinafter abbreviated as S / F ratio) is preferably 1.02 or more.
  • a more preferred lower limit is 1.05, and even more preferably 1.07. If it is 1.02 or more, a sufficient shearing force can be applied to the coating solution.
  • the upper limit is not particularly defined but can be 1.20.
  • the total thickness of the battery separator is preferably 6 to 13 ⁇ m, more preferably 7 to 12 ⁇ m, from the viewpoint of mechanical strength and insulation. Also, a high volume energy density can be obtained when a wound body is used as the electrode body.
  • the measured value in an Example is a value measured with the following method.
  • the obtained sample was observed by SEM at a magnification of 20,000 times.
  • Arbitrary 20 particles were selected on the image obtained by SEM measurement, and the average value of the particle diameters of the 20 particles was defined as the average particle diameter of the substantially spherical organic particles.
  • Average particle size of the plate-like inorganic particles From among the images obtained by the SEM measurement used in the above 3, arbitrary 20 particles whose planar shape is observed on the image are selected with respect to the double-sided tape. The average value of the length of the major axis was taken as the average particle size of the plate-like inorganic particles.
  • Film thickness Measured using a contact-type film thickness meter Digital Micrometer M-30 manufactured by Sony Manufacturing Systems Co., Ltd..
  • the layer coat electrode A100 (1.6mAh / cm ⁇ 2 >) by the Piotrec company company was used as a negative electrode.
  • ⁇ Active material of negative electrode adheres to modified porous layer of battery separator in an area ratio of less than 30%
  • meltdown characteristics While the separators obtained in the examples and comparative examples were heated at a rate of temperature increase of 5 ° C./min, the air resistance was measured with an Oken type air resistance meter (Asahi Seiko Co., Ltd., EGO-1T). Then, after the air resistance reached the detection limit of 1 ⁇ 10 5 sec / 100 cc, the temperature at which the air resistance began to drop again to 1 ⁇ 10 5 sec / 100 cc or less was obtained and was defined as the meltdown temperature (° C.). When the judgment meltdown temperature (° C) exceeds 200 ° C When the meltdown temperature (° C) is 200 ° C or lower ⁇ ⁇
  • Viscosity of coating liquid The viscosity of the coating liquid at 25 ° C. was measured using a viscometer (DV-I PRIME manufactured by BROOKFIELD).
  • Example 1 (Preparation of coating solution A) 40 parts by weight of a mixture of 58 parts by weight of ion-exchanged water and 1 part by weight of butanol (plate boehmite having an average particle diameter of 1.0 ⁇ m and an average thickness of 0.4 ⁇ m, major axis / minor axis ratio of 2) and Ken as a binder 1 part by mass of 95% of polyvinyl alcohol was added and dispersed well. Subsequently, carboxymethylcellulose (CMC) was added as a thickener, and the liquid viscosity was adjusted to 20 mPa ⁇ s to obtain a coating liquid A1.
  • CMC carboxymethylcellulose
  • Example 2 The same procedure as in Example 1 was conducted except that coating liquid A2 in the form of plate-like boehmite particles (average particle size 2.0 ⁇ m, average thickness 0.4 ⁇ m, major axis / minor axis ratio 3) was used instead of plate-like boehmite. A battery separator was obtained.
  • Example 3 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A3 having a liquid viscosity adjusted to 10 mPa ⁇ s was used.
  • Example 4 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A4 having a liquid viscosity adjusted to 30 mPa ⁇ s was used.
  • Example 5 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A5 having an average particle size of 1.0 ⁇ m, an average thickness of 0.2 ⁇ m, and a major axis / minor axis ratio of 3 was used. .
  • Example 6 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A6 having an average particle size of 2.0 ⁇ m, an average thickness of 0.6 ⁇ m, and a major axis / minor axis ratio of 3 was used for the plate-like boehmite particles.
  • Example 7 The same procedure as in Example 1 was performed except that the coating amount of the coating liquid B was adjusted so that the volume of the substantially spherical organic particles was 25% by volume with respect to the total volume of the substantially spherical organic particles and the plate-like inorganic particles. Thus, a battery separator was obtained.
  • Example 8 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A was applied under conditions of an S / F ratio of 1.18.
  • Example 9 In the preparation of the coating liquid B, a battery separator was obtained in the same manner as in Example 1 except that the coating liquid B2 having a liquid viscosity adjusted to 10 mPa ⁇ s was used.
  • Example 10 In the preparation of the coating liquid B, a battery separator was obtained in the same manner as in Example 1 except that the coating liquid B3 having a liquid viscosity adjusted to 2 mPa ⁇ s was used.
  • Comparative Example 1 (Preparation of coating solution) 40 parts by mass of plate boehmite having an average particle diameter of 1.0 ⁇ m and an average thickness of 0.4 ⁇ m in a mixed solution composed of 58 parts by mass of ion-exchanged water and 1 part by mass of butanol, and 1 mass of polyvinyl alcohol having a saponification degree of 95% as a binder And a substantially spherical organic particle dispersion liquid (TRD202A manufactured by JSR Corporation, solid content concentration 40% by mass) made of an acrylic resin having an average particle size of 0.2 ⁇ m with respect to the total volume of the substantially spherical organic particles and the plate-like inorganic particles Then, it was added so that the volume of the substantially spherical organic particles was 15% by volume and well dispersed.
  • TRD202A manufactured by JSR Corporation, solid content concentration 40% by mass
  • Carboxymethylcellulose (CMC) was added as a thickener to this dispersion, and the liquid viscosity was adjusted to 20 mPa ⁇ s to obtain a coating liquid C.
  • a coating device reverse gravure coating method shown in FIG. 3 on a polyethylene microporous membrane (thickness 7 ⁇ m, porosity 21%, air permeability 120 seconds / 100 cc)
  • a conveyance speed of 30 m / min S / F Coating and drying were performed under the condition of a ratio of 1.05, and a porous layer was laminated to obtain a battery separator.
  • the basis weight when the porous layer was dried was 2.7 g / m 2 .
  • Comparative Example 2 In the preparation of the coating liquid A, a battery separator was obtained in the same manner as in Example 1 except that the coating liquid A7 in which alumina particles having an average particle diameter of 0.4 ⁇ m were used instead of the plate boehmite was used.
  • Comparative Example 3 In the preparation of the coating liquid A, a battery separator was obtained in the same manner as in Example 1 except that the coating liquid A8 having a liquid viscosity adjusted to 8 mPa ⁇ s was used.
  • Comparative Example 4 In the preparation of the coating liquid B, a battery separator was obtained in the same manner as in Example 1 except that the coating liquid B4 having a liquid viscosity adjusted to 20 mPa ⁇ s was used.
  • Comparative Example 5 In the preparation of the coating liquid B, a coating liquid B5 obtained by replacing the substantially spherical organic particle dispersion with an aqueous dispersion (solid content concentration 15% by mass) of melamine / formaldehyde condensate spherical particles (average particle size 0.4 ⁇ m) is used. A battery separator was obtained in the same manner as in Example 1 except that it was used.
  • Comparative Example 6 The same procedure as in Example 1 was conducted except that the coating amount of the coating liquid B was adjusted so that the volume of the substantially spherical organic particles was 5% by volume with respect to the total volume of the substantially spherical organic particles and the plate-like inorganic particles. Thus, a battery separator was obtained.
  • Comparative Example 7 A battery separator was obtained in the same manner as in Example 1 except that the coating liquid A was applied under conditions of an S / F ratio of 0.50.
  • Comparative Example 8 Similar to Example 1 except that the rotation direction of the gravure roll is the same as the transport direction of the polyethylene microporous membrane when the coating liquid A1 is applied, and the coating liquid A1 is applied under the condition of S / F ratio of 1.25. Thus, a battery separator was obtained.
  • Comparative Example 9 A polyethylene microporous membrane (porosity 23%, air permeability 110 seconds / 100 cc) having the same thickness as the battery separator of Comparative Example 1 was used as the battery separator.
  • Table 1 shows the characteristics of the battery separators obtained in Examples 1 to 10 and Comparative Examples 1 to 9.
  • Table 1 shows the characteristics of the battery separators obtained in Examples 1 to 10 and Comparative Examples 1 to 9.
  • Example 1 to 10 and Comparative Examples 3 and 5 to 7 substantially spherical organic particles are unevenly distributed on the surface of the porous layer, and the plate-like inorganic particles are islands. It was a sea-island structure with substantially spherical organic particles as the sea.
  • Comparative Examples 1 and 4 plate-like inorganic particles and substantially spherical organic particles were mixed, and the sea-island structure was not obtained.

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Abstract

La présente invention, supposant que des séparateurs de piles continueront de s'amincir et d'accroître leur capacité, concerne un séparateur de piles présentant une adhésion à un matériau d'électrode et pouvant minimiser l'espace gaspillé entre un matériau d'électrode et un séparateur, et concerne un séparateur de piles dans lequel une haute densité d'énergie volumique peut être obtenue lorsque le matériau d'électrode et le séparateur sont superposés et formés en un corps enroulé, et qui est particulièrement avantageux pour un séparateur de piles lithium-ion. Un séparateur de piles dans lequel une couche poreuse contenant une pellicule microporeuse polyoléfine, et des particules inorganiques en forme de plaque et des particules organiques sensiblement sphériques composées d'une résine acrylique ou de fluororésine sont stratifiées sur la surface de la pellicule, les particules organiques sensiblement sphériques sont distribuées non uniformément sur la surface de la couche poreuse, et le ratio du diamètre de particule moyen r (µm) des particules organiques sensiblement sphériques et l'épaisseur moyenne t (µm) des particules inorganiques en forme de plaque satisfait les formules 1 et 2. 0,1 µm ≦ r ≦ 0,8 µm... Formule 1 0,3 ≦ r/t ≦ 1,0... Formule 2
PCT/JP2016/074774 2015-08-27 2016-08-25 Séparateur de piles et son procédé de fabrication WO2017033993A1 (fr)

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JP2019160408A (ja) * 2018-03-07 2019-09-19 トヨタ自動車株式会社 電池およびその製造方法
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JP2019160408A (ja) * 2018-03-07 2019-09-19 トヨタ自動車株式会社 電池およびその製造方法
JP7032180B2 (ja) 2018-03-07 2022-03-08 トヨタ自動車株式会社 電池およびその製造方法
US12002990B2 (en) 2018-10-12 2024-06-04 Lg Energy Solution, Ltd. Porous separator and lithium secondary battery comprising same
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