Classifications

• • 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
  • 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
  • H01M50/429—Natural polymers
  • H01M50/4295—Natural cotton, cellulose or wood
• • 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
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
  • B32B5/18—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/20—Manufacture of shaped structures of ion-exchange resins
  • C08J5/22—Films, membranes or diaphragms
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
• • 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
  • H01M50/411—Organic material
  • H01M50/429—Natural 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
  • H01M50/44—Fibrous 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
  • H01M50/489—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 relates to a laminated porous film that can be used for a separator for an electricity storage device having excellent electrical characteristics and safety. Specifically, by providing a porous layer on the porous film, it has excellent safety, has excellent film physical properties and high battery performance, and is suitable for use as an electrical storage device separator because of its high quality.
• the present invention relates to a porous film.
• a porous film made of polyolefin or the like is excellent in mechanical properties in addition to electrical insulation and ion permeability, and is therefore widely used especially for separator applications of lithium ion secondary batteries.
• the porous film produced by such a method has problems such as insufficient heat resistance and dimensional stability, and cannot prevent penetration of foreign matter mixed in the battery.
• the object of the present invention is to solve the above-mentioned problems. That is, the object of the present invention is to achieve excellent battery performance, heat resistance and cost reduction by reducing the water content and improving coating properties by containing at least two water-soluble polymers in the porous layer, and An object of the present invention is to provide a laminated porous film that is suitable for use as a separator for an electricity storage device by having high quality.
• the present invention provides a porous layer on at least one surface of a substrate, and the porous layer contains inorganic particles (A), at least two types of water-soluble polymers (B) and a resin (C).
• A inorganic particles
• B water-soluble polymers
• C resin
• the laminated porous film of the present invention is excellent in that it can achieve low moisture content and can impart excellent coating properties by containing at least two types of water-soluble polymer (B) in the porous layer. It is possible to provide a laminated porous film that achieves battery performance, heat resistance, and cost reduction, is high-quality, and is suitable for use as a separator for an electricity storage device.
• the laminated porous film refers to a laminated film in which a porous layer is provided on at least one side of a substrate.
• This porous layer contains inorganic particles (A), at least two types of water-soluble polymers (B), and a resin (C).
• the base material used for the laminated porous film is a porous sheet having air permeability for laminating a porous layer.
• Specific examples include nonwoven fabrics, various woven fabrics, and porous films.
• the substrate used in the present invention is preferably a porous film made of a resin because it is excellent in productivity and processability.
• the porous film is a microporous membrane having a large number of fine through holes penetrating both surfaces of the film and having air permeability.
• the main component of the porous film is preferably resin (D).
• the main component of the porous film means that it accounts for 80% by mass or more of the raw material constituting the porous film.
• an olefin resin As the resin (D), an olefin resin, a fluorine resin, an imide resin, a urethane resin, an acrylic resin, or the like can be used, but the olefin resin is excellent in terms of ease of processing and low cost. From the viewpoint of achieving both a high point and high ionic conductivity.
• olefin resins examples include single polyolefin resins such as polyethylene, polypropylene, polybutene-1, and poly-4-methylpentene-1, mixtures of these resins, and random copolymerization and block copolymerization of monomers. Resin can be used.
• the porous film used as the substrate of the laminated porous film of the present invention preferably has a melting point of 110 ° C. or higher from the viewpoint of heat resistance.
• the porous film may change in dimensions when the porous layer is laminated on the porous film.
• the melting point of the porous film refers to the melting point as a matter of course when it exhibits a single melting point.
• the porous film has a plurality of melting points such as a mixture of olefinic resins
• the melting point appearing on the highest temperature side is defined as the melting point of the porous film.
• the melting point of the porous film is more preferably 130 ° C. or higher, and further preferably 150 ° C.
• the porous film exhibits a plurality of melting points, it is preferable that all of them are within the above range.
• the porous film used for the substrate preferably has ⁇ -crystal forming ability.
• the porous film can be produced by making the film porous by the ⁇ -crystal method described later.
• the porous film obtained by the ⁇ crystal method has excellent productivity and has a surface pore diameter (surface pore diameter) suitable for expressing high adhesion due to the anchor effect when the porous layer is laminated. It can be suitably used as a substrate for a porous film.
• the ⁇ crystal method refers to a method of forming a through hole in a film by stretching after forming a resin having ⁇ crystal forming ability into a sheet.
• the resin used for the porous film can be formed by adding a nucleating agent ( ⁇ crystal nucleating agent) capable of selectively forming ⁇ crystals out of the resin crystal seeds.
• ⁇ crystal nucleating agent for the polypropylene resin
• examples of the ⁇ crystal nucleating agent for the polypropylene resin include various pigment compounds and amide compounds. Particularly, amide compounds disclosed in JP-A-5-310665 can be preferably used.
• the content of the ⁇ crystal nucleating agent is preferably 0.05 to 0.5 parts by mass, more preferably 0.1 to 0.3 parts by mass when the entire polypropylene resin is 100 parts by mass. .
• the ⁇ crystal-forming ability indicates the abundance ratio of ⁇ -crystals in a polypropylene resin measured under the following conditions, and is a value indicating how much ⁇ -crystals are formed. It is.
• the ⁇ crystal-forming ability was measured after 5 mg of polypropylene resin or polypropylene film was heated from room temperature to 240 ° C. at a rate of 10 ° C./min (first run) using a differential scanning calorimeter and held for 10 minutes. Cool to 30 ° C. at 10 ° C./min. The melting peak observed when the temperature is raised (second run) again at 10 ° C./minute after holding for 5 minutes is the melting peak of the ⁇ crystal at 145 ° C.
• the melting at which the peak is observed is the melting peak of the ⁇ crystal, and the heat of fusion is determined.
• the heat of fusion of the ⁇ crystal is ⁇ H ⁇ and the heat of fusion of the ⁇ crystal is ⁇ H ⁇ .
• Crystal formation ability. ⁇ crystal forming ability (%) [ ⁇ H ⁇ / ( ⁇ H ⁇ + ⁇ H ⁇ )] ⁇ 100
• the ⁇ -crystal forming ability of the polypropylene resin constituting (included) the porous film used for the substrate has a high porosity and suitable air resistance, and the porous layer is laminated when the porous layer is laminated. From the viewpoint of forming a surface pore size suitable for adhesion between the porous film and the porous film, it is preferably 40 to 90%. If the ⁇ -crystal forming ability is less than 40%, the amount of ⁇ -crystal is small at the time of film production, so the number of voids formed in the film is reduced by utilizing the transition to ⁇ -crystal, and as a result, only a film with low permeability is obtained. It may not be possible.
• the ⁇ -crystal forming ability exceeds 90%, coarse pores are formed, and the function as a power storage device separator may not be provided.
• the ⁇ crystal forming ability is more preferably 45 to 80%.
• the polypropylene resin constituting the porous film is an isotactic polypropylene resin having a melt flow rate (hereinafter referred to as MFR, measurement conditions are 230 ° C., 2.16 kg) in the range of 2 to 30 g / 10 min. It is preferable that If the MFR is out of the above preferred range, it may be difficult to obtain a stretched film. More preferably, the MFR is 3 to 20 g / 10 minutes.
• the isotactic index of the isotactic polypropylene resin is preferably 90 to 99.9%. If the isotactic index is less than 90%, the crystallinity of the resin is low, and it may be difficult to achieve high air permeability.
• a commercially available resin can be used as the isotactic polypropylene resin.
• homopolypropylene resin can be used for the porous film, as well as ethylene component, butene, hexene, octene, etc. in polypropylene from the viewpoint of stability in the film-forming process, film-forming property, and uniformity of physical properties.
• a copolymer obtained by copolymerizing the ⁇ -olefin component in an amount of 5% by mass or less may be used.
• the form of the comonomer introduced into the polypropylene may be either random copolymerization or block copolymerization.
• the above polypropylene resin preferably contains a high melt tension polypropylene in the range of 0.5 to 5% by mass from the viewpoint of improving the film forming property.
• High melt tension polypropylene is a polypropylene resin whose tension in the molten state is increased by mixing a high molecular weight component or a component having a branched structure into the polypropylene resin, or by copolymerizing a long-chain branched component with polypropylene.
• This high melt tension polypropylene is commercially available, and for example, polypropylene resins PF814, PF633, and PF611 manufactured by Basel, polypropylene resin WB130HMS manufactured by Borealis, and polypropylene resins D114 and D206 manufactured by Dow can be used.
• the air-permeability is improved by increasing the void formation efficiency at the time of stretching and by increasing the pore diameter. Therefore, 1 to 10 ethylene / ⁇ -olefin copolymer is added to the homopolypropylene resin. A mixture containing mass% is preferable.
• examples of the ethylene / ⁇ -olefin copolymer include linear low-density polyethylene and ultra-low-density polyethylene. Among them, an ethylene / octene-1 copolymer obtained by copolymerizing octene-1 is preferable. Can be used.
• this ethylene-octene-1 copolymer a commercially available resin, for example, “Engage (registered trademark)” (type names: 8411, 8452, 8100, etc.) manufactured by Dow Chemical can be used.
• the porous film used for the substrate is preferably stretched at least in the uniaxial direction.
• the porosity and mechanical strength of the film may be insufficient.
• a method of stretching the porous film in at least a uniaxial direction it is preferable to stretch the porous film at a predetermined ratio after heating by a tenter method, a roll method, an inflation method, or a combination thereof.
• the stretching may be uniaxial stretching or biaxial stretching.
• any of simultaneous biaxial stretching, sequential stretching, and multistage stretching for example, a combination of simultaneous biaxial stretching and sequential stretching may be used, but sequential biaxial stretching is preferable from the viewpoint of productivity.
• an antioxidant such as an antioxidant, a heat stabilizer, an antistatic agent, a lubricant composed of inorganic or organic particles, an antiblocking agent, a filler, an incompatible polymer, etc.
• An agent may be included.
• an antioxidant is added in an amount of 0.01 to 0 to 100 parts by mass of the olefin resin for the purpose of suppressing oxidative degradation due to the thermal history of the olefin resin. It is preferable to contain 0.5 parts by mass.
• the air resistance of the porous film used as the substrate of the laminated porous film is preferably 50 to 500 seconds / 100 ml. If the air permeability resistance is less than 50 seconds / 100 ml, it may be difficult to maintain insulation when the separator is used. Moreover, when it exceeds 500 seconds / 100 ml, when it uses as a base material of a lamination
• the air resistance of the porous film is more preferably 80 to 400 seconds / 100 ml, still more preferably 100 to 300 seconds / 100 ml.
• the porous film used in the present invention preferably has a porosity of 50% or more and less than 85%, and more preferably 65% or more and less than 80%. If it is less than 50%, the number of pores on the surface will be small, so that the adhesion to the porous film may be insufficient when the porous layer is laminated. If it is 85% or more, it may be insufficient from the viewpoint of separator characteristics and strength.
• the ratio of (N A ) / (N B ) is preferably 0.1 to 4, more preferably 0.4 to 3.
• a method for controlling the surface pore diameter within such a preferable range can be achieved by stretching and making the polypropylene resin to which the above-mentioned ⁇ crystal nucleating agent is added.
• the surface pore diameter of the porous film can be confirmed by taking a surface image using a scanning electron microscope and performing image analysis.
• the laminated porous film of the present invention forms a porous layer on at least one side of the porous film obtained as described above.
• surface treatment for easy adhesion such as corona discharge treatment
• Examples of the surface treatment include corona discharge treatment in air, an oxygen atmosphere, a nitrogen atmosphere, plasma treatment, and the like, but simple corona discharge treatment is preferable.
• the laminated porous film of the present invention is provided with a porous layer containing inorganic particles (A).
• the inorganic particles (A) are preferably the main component in the porous layer.
• being a main component of the porous layer means that 50% by mass or more of the composition constituting the porous layer is inorganic particles (A).
• the inorganic particles (A) used for the porous layer are preferably particles whose shape is maintained at least up to 200 ° C. That the shape is maintained means that the aspect ratio and average particle diameter of the inorganic particles (A) at normal temperature do not change even at 200 ° C. More preferably, the shape is maintained up to 300 ° C, and still more preferably the shape is maintained up to 330 ° C. That is, it is preferable that the phase transition accompanying the melting point, softening point, thermal decomposition temperature, or volume change of the inorganic particles (A) does not occur up to the above temperature.
• inorganic particles (A) that do not exhibit a melting point and are maintained in shape until at least 330 ° C. alumina, boehmite, silica, titania, zirconia, magnesia, ceria, yttria, zinc oxide, iron oxide, and the like
• Oxide ceramics, nitride ceramics such as silicon nitride, titanium nitride, boron nitride, silicon carbide, calcium carbonate, aluminum sulfate, potassium titanate, talc, kaolin clay, kaolinite, halloysite, pyrophyllite, montmorillonite, Sericite, mica, amicite, bentonite, asbestos, zeolite, calcium silicate, magnesium silicate and the like can be mentioned.
• the inorganic particles (A) are preferably calcium carbonate, alumina, boehmite, and silica from the viewpoint of electrochemical stability, and more preferably calcium carbonate from the viewpoint of dispersibility and adhesiveness to the resin (C).
• the average particle size of the inorganic particles (A) used in the porous layer is preferably 0.05 to 15 ⁇ m, more preferably 0.1 to 10 ⁇ m, from the viewpoint of achieving both the air permeability and the mechanical properties of the porous layer. .
• the average particle diameter is less than 0.05 ⁇ m, the inorganic particles (A) enter the porous film from the open surface of the porous film, and the air resistance of the porous film increases or the surface area of the particles increases. Aggregation tends to occur, and when the porous layer is provided on the surface of the porous film, coarse protrusions are formed, which may deteriorate the quality of the laminated porous film.
• the average particle diameter of an inorganic particle (A) says the value obtained by measuring the inorganic particle in a laminated porous film.
• the aspect ratio of the inorganic particles (A) in the porous layer is preferably 1.5 or more and 10 or less, more preferably 2 or more and 8 or less. More preferably, it is 6 or less.
• the aspect ratio is less than 1.5, the filling rate of particles increases, and thus the air resistance may be easily lowered.
• the aspect ratio is greater than 10, the flexibility of the porous layer is impaired, and cracking may easily occur when the laminated porous film is bent.
• the aspect ratio of the inorganic particles (A) can be evaluated by a method described later by observing the laminated porous film with a scanning electron microscope.
• the proportion of the inorganic particles (A) contained in the porous layer is preferably 50% by mass or more and less than 95% by mass in the composition forming the porous layer, and 60% by mass. More preferably, it is less than 90% by mass.
• the ratio of the inorganic particles (A) is 95% by mass or more, the amount of the resin (C) described later with respect to the inorganic particles (A) decreases, and the inorganic particles (A) cannot be sufficiently bonded to each other. May decrease.
• the proportion of the inorganic particles (A) is lower than 50% by mass, the heat resistance of the porous layer is not sufficiently exhibited, and when the laminated porous film is formed, the shrinkage becomes remarkable, or the resin (C) is a porous layer. It may block the air holes inside and induce a decrease in air resistance.
• the ratio of the inorganic particles (A) contained in the porous layer of the laminated porous film of the present invention is that the porous layer is peeled and collected from the laminated porous film, and this is subjected to powder X-ray analysis to identify the inorganic particle species. It can obtain
• the thickness of the porous layer of the laminated porous film of the present invention is 1 to 30 ⁇ m from the viewpoint of heat resistance and mechanical properties. It is preferably 1 to 20 ⁇ m, more preferably 1 to 10 ⁇ m, and particularly preferably 1 to 6 ⁇ m. If the thickness is less than 1 ⁇ m, sufficient heat resistance cannot be obtained, or the stiffness of the laminated porous film is weak, and wrinkles and necking occur when transported as a separator with tension applied in the battery assembly process. There is a case.
• the thickness exceeds 30 ⁇ m, since the wet thickness (thickness in a wet state before drying) becomes thick in the coating when forming the porous layer on the porous film, the drying efficiency is lowered.
• the water content increases when the porous film is formed, or when the laminated porous film is bent, cracks and peeling easily occur.
• As a method for controlling the thickness to such a preferable range it can be achieved by controlling the discharge amount of the coating liquid, the conveying speed, and the like when the coating method described later is used. The thickness of the porous layer can be confirmed by a method described later.
• the porous layer of the laminated porous film of the present invention contains at least two water-soluble polymers (B).
• B water-soluble polymers
• the drying efficiency in the drying process at the time of coating can be effectively improved, so that a low water content can be expressed without using a special process.
• the stability of the coating liquid for forming the porous layer can be improved by including two or more types of water-soluble polymer (B), in coating when the porous layer is laminated on the porous film, Suppression is possible. From the above effects, it is possible to produce a laminated porous film that has excellent electrochemical stability and can be manufactured at high quality and at low cost.
• the water-soluble polymer (B) used for the porous layer of the laminated porous film of the present invention has the effect of adjusting the viscosity of the coating liquid for forming the porous layer on the surface of the porous film, and making it within a coatable range. It is preferable that the material has
• the water-soluble polymer (B) used for the porous layer is a vinyl alcohol polymer (for example, ethylene vinyl alcohol (EVA), polyvinyl alcohol (PVA), polyvinyl butyral (PVB), etc.). ), Polyalkyl vinyl ether, carboxy vinyl polymer, water-soluble acrylic resin, water-soluble styrene resin, vinyl pyrrolidone resin (for example, polyvinyl pyrrolidone (PVP)), cellulosic compounds and derivatives thereof (for example, carboxymethyl cellulose (CMC) ), Hydroxyethyl cellulose (HEC), etc.), and preferably contains at least two water-soluble polymers selected from these.
• a vinyl alcohol polymer for example, ethylene vinyl alcohol (EVA), polyvinyl alcohol (PVA), polyvinyl butyral (PVB), etc.
• EVA ethylene vinyl alcohol
• PVA polyvinyl alcohol
• PVB polyvinyl butyral
• Polyalkyl vinyl ether Polyalky
• At least two kinds are preferably selected from vinyl alcohol polymers, water-soluble acrylic resins, and cellulose compounds.
• at least two cellulose compounds are selected. It is preferable that the species is selected.
• One of the water-soluble polymers (B) used for the porous layer of the laminated porous film of the present invention can obtain the effect of dispersing the inorganic particles (A) (the effect of promoting dispersion and maintaining dispersion stability). Therefore, a water-soluble polymer containing at least one functional group selected from the group consisting of an amino group, a carbonyl group, a carboxyl group, a sulfonyl group and a phosphate group as a functional group at the end of the side chain of the polymer skeleton ( B1) is preferred.
• the side chain of the polymer skeleton means a molecular chain having one or more carbons branched from the repeating unit (main chain) of the polymer constituting the water-soluble polymer.
• the functional group at the end of the side chain of the polymer skeleton preferably contains an amino group or a carboxyl group from the viewpoint of high adsorptivity to the surface of the inorganic particles (A).
• water-soluble polymer (B1) includes the above-described functional group
• functional groups such as a hydroxyl group, an alkyl group, and a halogen group exemplified in the description of the water-soluble polymer (B2) described later are provided. May be included.
• Examples of the water-soluble polymer (B1) used in the porous layer of the laminated porous film of the present invention include acrylic acid / sulfonic acid monomer copolymer salt, polyacrylamide, polyethyleneimine, polystyrene sulfonate, polyamidine, carboxymethylcellulose ( CMC), carboxymethyl ethyl cellulose, carboxymethyl hydroxyethyl cellulose, and the like.
• carboxymethyl cellulose (CMC), carboxymethyl ethyl cellulose, and carboxymethyl hydroxyethyl cellulose are preferable from the viewpoint of heat resistance, and carboxymethyl cellulose (CMC) from the viewpoint of electrochemical stability. CMC) is preferred.
• the other one of the water-soluble polymers (B) used for the porous layer of the laminated porous film of the present invention is selected from the group consisting of a hydroxyl group, an alkyl group and a halogen group at the end of the side chain of the polymer skeleton.
• a water-soluble polymer (B2) containing only at least one selected functional group is preferable. By including only these functional groups, adsorption / dehydration of the end of the side chain and water can be facilitated, and the water content of the porous layer can be reduced. Among these, the solubility in the coating liquid that forms the porous layer is good, and it is difficult to form an undissolved substance that becomes a foreign substance. B2) is preferred.
• Examples of the water-soluble polymer (B2) used for the porous layer of the laminated porous film of the present invention include polyvinyl alcohol, ethylene vinyl alcohol, polyvinyl butyral, polyalkyl vinyl ether, hydroxyethyl cellulose (HEC), butyl methyl cellulose, hydroxypropyl cellulose. Hydroxypropylmethylcellulose, hydroxyethylmethylcellulose, alkylhydroxyethylcellulose and the like are preferable, and hydroxyethylcellulose (HEC) is preferable from the viewpoint of electrochemical stability and heat resistance.
• the water-soluble polymer (B1) and the water-soluble polymer (B2) contained in the porous layer are preferably selected from cellulosic compounds. Since the cellulosic compound has no or high crystal melting point, if the water-soluble polymer (B1) and the water-soluble polymer (B2) to be used are cellulose compounds, the laminated porous film has sufficient heat resistance. It becomes possible to grant. If the water-soluble polymer (B1) or water-soluble polymer (B2) to be used is other than a cellulose compound, heat resistance may not be obtained because the water-soluble polymer (B) itself has insufficient heat resistance. is there. Among them, the cellulose-based compound used for the water-soluble polymer (B1) and the water-soluble polymer (B2) is preferably the above-described cellulose.
• the water-soluble polymer contained in the porous layer of the laminated porous film of the present invention can be confirmed by analyzing the composition of the porous layer of the laminated porous film.
• the water-soluble polymer (B) used in the porous layer of the laminated porous film of the present invention can define a preferable molecular weight range by measuring the viscosity when a 1% by mass aqueous solution is used. .
• the viscosity of the 1% by mass aqueous solution is an index representing the molecular weight of the water-soluble polymer (B), and the higher the viscosity, the higher the molecular weight.
• the viscosity of a 1% by mass aqueous solution of the water-soluble polymer (B1) used for the porous layer is preferably 5 mPa ⁇ s or more and 3,000 mPa ⁇ s or less, and preferably 10 mPa ⁇ s or more and 2,500 mPa ⁇ s. s or less is more preferable, and 10 mPa ⁇ s or more and 900 mPa ⁇ s or less is more preferable.
• the water-soluble polymer (B1) can be quickly dissolved in the solvent of the coating liquid and then adsorbed onto the inorganic particles (A).
• the viscosity of the 1% by mass aqueous solution of the water-soluble polymer (B1) is less than 5 mPa ⁇ s, a decrease in heat resistance may be induced when a porous layer is formed. Moreover, since the solubility in a coating liquid will fall when it exceeds 3,000 mPa * s, undissolved locations aggregate while adsorbing to inorganic particles (A), and Mamako (inorganic particles (A) and In some cases, a water-soluble polymer (B1) aggregated adhesive) is formed.
• the viscosity of the water-soluble polymer (B1) can be adjusted to the above range by using the low-molecular weight water-soluble polymer (B1).
• the viscosity of the water-soluble polymer (B1) is evaluated using a B-type viscometer with a 1% by mass aqueous solution under the conditions of 25 ° C. and 60 rotations.
• the viscosity of a 1% by mass aqueous solution of the water-soluble polymer (B2) used in the porous layer is preferably 1,000 mPa ⁇ s or more and 5,000 mPa ⁇ s or less, and 2,000 mPa ⁇ s or less. More preferred is s to 4,000 mPa ⁇ s. Since the water-soluble polymer (B2) has low adsorptivity to the inorganic particles (A) and does not easily form coarse aggregates, the viscosity in the above range is used to make the viscosity of the coating solution suitable for coating.
• the viscosity of the 1% by mass aqueous solution is less than 1,000 mPa ⁇ s, when used in combination with the water-soluble polymer (B1), the viscosity of the coating solution cannot be controlled within a range suitable for coating, When the laminated porous film is bent, cracks and peeling may occur.
• the dispersibility of the water-soluble polymer (B2) in the coating solution is lowered, and mixed spots may be generated during coating, which may cause defects.
• the viscosity of the water-soluble polymer (B2) in the above range it can be achieved by using the water-soluble polymer (B2) having a high molecular weight.
• the viscosity of the water-soluble polymer (B2) is measured with a 1% by mass aqueous solution using a B-type viscometer at 25 ° C. and 30 rotations.
• the mass percentage of the water-soluble polymer (B1) in the porous layer is C b1 and the mass percentage of the water-soluble polymer (B2) is C b2 , C b1 / C b2 It is preferable to mix the water-soluble polymers (B1) and (B2) at a ratio such that the value is 0.2 or more and 8 or less.
• the value of C b1 / C b2 is 0.2 or less and 8 or more, the water content in the laminated porous film can be effectively reduced and the stability of the coating liquid for forming the porous layer can be maintained.
• the value of C b1 / C b2 is preferably 0.3 or more and 6 or less, more preferably 0.5 or more and 3 or less.
• the value of C b1 / C b2 is less than 0.2, the proportion of the water-soluble polymer (B1) that contributes to the dispersion stability of the coating liquid is small.
• the value of C b1 / C b2 exceeds 8, the water content may increase due to an increase in the water-soluble polymer (B1) in the composition of the porous layer.
• water-soluble polymer (B1) and water-soluble polymer (B2) contained in the porous layer of the laminated porous film of this invention when using multiple types of water-soluble polymer (B1), water-soluble polymer (When the total mass percentage of the water-soluble polymer (B1) belonging to B1) is C b1 and a plurality of water-soluble polymers (B2) are used, the water-soluble polymer (B2) belonging to the water-soluble polymer (B2) The above-mentioned C b1 / C b2 is calculated by using C b2 as the total mass percentage.
• the water-soluble polymer (B) contained in the porous layer of the laminated porous film of the present invention is within a range not impairing the performance of the laminated porous film, the water-soluble polymer (B1) and the water-soluble polymer ( A water-soluble polymer not belonging to any of B2) may be included.
• the total amount of the water-soluble polymer (B), that is, the total amount of the water-soluble polymers (B1) and (B2) and the water-soluble polymer that does not belong to any of the inorganic particles is used as the inorganic particles.
• the amount is preferably 0.5 to 10 parts by weight, more preferably 2 to 7 parts by weight, based on 100 parts by weight. By setting it as the said range, the effect of addition of water-soluble polymer (B) can be exhibited, without impairing physical properties, such as air permeability resistance.
• the viscosity of the coating liquid cannot be adjusted to an appropriate range for coating, and a porous layer is formed. In some cases, defects such as cistern and stripes may be induced during coating. On the other hand, when the total amount exceeds 10 parts by mass, the water-soluble polymer (B) may block the pores of the porous layer and cause a decrease in air resistance.
• the mixing ratio of the at least two or more water-soluble polymers (B) in the porous layer of the laminated porous film of the present invention and the total amount in the porous layer are determined when the composition of the composition contained in the coating liquid is clear. Can be calculated from the composition contained in the porous layer and the residual solvent amount. If the formulation is not clear, it can be confirmed by composition analysis of the porous layer of the laminated porous film.
• the moisture content of the laminated porous film of the present invention is preferably 0.1 ppm or more and 3,000 ppm or less.
• the moisture content refers to the mass percentage of moisture contained in the laminated porous film.
• a halogen acid such as hydrogen fluoride (HF) or hydrogen.
• the water content is preferably from 0.1 ppm to 2,000 ppm, more preferably from 0.1 ppm to 1,500 ppm.
• the method for setting the moisture content within the above range can be achieved by using the specific water-soluble polymer (B) described above for the porous layer of the laminated porous film.
• the moisture content of the laminated porous film can be confirmed by the method described later.
• the resin (C) used for the porous layer may bind other materials (for example, between inorganic particles (A), between inorganic particles (A) and a substrate, etc.). A material that can be made.
• Examples of the resin (C) used for the porous layer of the laminated porous film of the present invention include ethylene-acrylates such as polyvinylidene fluoride (PVDF), acrylic (excluding water-soluble acrylic resin), and ethylene-ethyl acrylate copolymer (EEA).
• PVDF polyvinylidene fluoride
• ESA ethylene-ethyl acrylate copolymer
• Acrylic acid copolymer fluorine rubber, styrene butadiene rubber (SBR), cross-linked acrylic resin, polyurethane, epoxy resin, modified polyolefin, silicon alkoxides, zirconium compound, colloidal silica, and oxirane ring-containing compound.
• SBR styrene butadiene rubber
• cross-linked acrylic resin polyurethane
• epoxy resin modified polyolefin
• silicon alkoxides zirconium compound
• colloidal silica colloidal silica
• the other materials are preferably bound by melting the resin (C).
• the resin (C) melts into the pores of the inorganic particles (A) and part of the surface openings of the porous film, thereby expressing the anchor effect. Since it shows a strong binding force, it is possible to suppress the removal of the inorganic particles (A) from the porous layer and the peeling of the porous layer from the porous film.
• the binding property between the other materials (between the inorganic particles (A), between the inorganic particles (A) and the base material) by the resin (C) can be evaluated by the rate of change K of the friction coefficient ⁇ k and the peel strength described later. Details of the evaluation method will be described later.
• the rate of change K of the friction coefficient ⁇ k when the film running test is carried out so that the surface of the porous layer is in contact with the roll is preferably less than 500% and more preferably less than 300%.
• the inorganic particles (A) may fall off during film running, and white powder may be generated.
• the drop of the inorganic particles (A) may cause defects such as the yield of the battery assembly process and the mixing of foreign substances.
• it can achieve by using resin (C).
• the binding property between the porous layer and the porous film of the laminated porous film of the present invention can be evaluated by the peel strength when the laminated porous film is peeled off at the porous layer / porous film interface.
• This peel strength is an index of the binding force between the porous film and the porous layer. The higher the peel strength, the more the inorganic particles (A) between the resin (C) and the substrate, and the inorganic particles (A) in the porous layer. It shows that the binding power of is high.
• the peel strength can be evaluated by the method described later.
• the laminated porous film of the present invention can be peeled off at the porous layer / porous film interface.
• the peel strength when peeled at the porous layer / porous film interface is preferably 10 to 500 g / 25 mm width, and more preferably 20 to 300 g / 25 mm width.
• the peel strength is less than 10 g / 25 mm, the porous layer is more easily peeled from the laminated porous film, and when the laminated porous film is used as a separator, partial peeling may occur in the cutting / slit process.
• the peel strength within a preferable range it can be achieved by making the surface pore diameter into a preferable range and / or using the resin (C).
• the resin (C) in order to bind between the inorganic particles (A) and between the inorganic particles (A) and the base material by fusing the resin (C), the resin (C) has a lower melting point or softening point than the porous film. It is preferable to use a resin.
• the melting point or softening point of the resin (C) used for the porous layer of the laminated porous film of the present invention is preferably 70 to 120 ° C, more preferably 80 to 110 ° C.
• the heat resistance of the laminated porous film may be lowered when the resin (C) is added to the porous layer.
• the melting point or softening point is higher than 120 ° C., it is necessary to process at a high temperature when the resin (C) is melt-bonded between the inorganic particles (A) and between the inorganic particles (A) and the substrate. In some cases, shrinkage of the porous film is caused to deteriorate characteristics such as air resistance and flatness.
• the melting point or softening point of the resin (C) can be confirmed by a method described later.
• the blending ratio of the resin (C) used in the porous layer of the porous film of the present invention in the porous layer is preferably 1 to 30 parts by mass with respect to 100 parts by mass of the inorganic particles (A) from the viewpoint of adhesion. More preferred is 20 parts by mass, and even more preferred is 5 to 15 parts by mass.
• the blending ratio of the resin (C) is less than 1 part by mass, the adhesive force between the inorganic particles (A) and between the inorganic particles (A) and the substrate is insufficient, and the inorganic particles (A) fall off or the porous layer is peeled off. May occur.
• it exceeds 30 mass parts since the hole inside a porous layer is obstruct
• the porous layer of the laminated porous film of the present invention has a carboxyl group and / or a molecular structure of the resin (C) from the viewpoint of improving the binding property between the inorganic particles (A) and between the inorganic particles (A) and the substrate.
• it preferably contains a hydroxyl group.
• Examples of the resin (C) containing a carboxyl group and / or a hydroxyl group in the molecular structure include an acrylate copolymer and a modified polyolefin into which an unsaturated carboxylic acid skeleton is introduced.
• the modified polyolefin preferably comprises an olefin skeleton and an unsaturated carboxylic acid skeleton.
• the olefin skeleton include olefins having 2 to 6 carbon atoms such as propylene, ethylene, isobutylene, 1-butene, 1-pentene, 1-hexene, and the unsaturated carboxylic acid skeleton includes at least one carboxyl in the molecule.
• a compound having a group or an acid anhydride group is preferable, and in addition to acrylic acid, methacrylic acid, maleic acid, maleic anhydride, itaconic acid, itaconic anhydride, fumaric acid, crotonic acid, etc., unsaturated dicarboxylic acid half ester, half Examples include amides.
• the surface of the olefin is high because of its high surface tension, and repelling, streaks, etc. are applied during the coating of the coating liquid that forms the porous layer.
• the resin (C) contains an olefin-based resin, so that familiarity can be suppressed and repelling can be suppressed.
• the melting point or softening point temperature for melting and binding the resin (C) is used.
• the porous film itself may be deformed, resulting in deterioration of air permeability or loss of flatness.
• the melting point of the porous film and the melting point or softening point temperature of the resin (C) are within the above-described range, and further, drying is performed in the temperature range described below, thereby providing excellent defect quality such as repelling and streaking, and A laminated porous film having excellent adhesion between the porous film and the porous layer and good flatness can be obtained, which is preferable.
• the porous layer of the laminated porous film of the present invention can contain thermoplastic resin particles having a melting point of 120 to 160 ° C. from the viewpoint of imparting shutdown properties to the laminated porous film.
• the shutdown property refers to a characteristic that, when the laminated porous film is used as a separator, the through-holes of the laminated porous film are blocked by components contained in the film when the battery is abnormally heated and the flow of ions is blocked. If the melting point of the thermoplastic resin particles is less than 120 ° C, the operating environment will shut down the through-holes of the film at a low temperature of about 120 ° C, which is not a problem for other materials of the electricity storage device, and will malfunction Will occur.
• the shutdown preferably functions at 125 to 150 ° C. from the viewpoint of the thermal stability of the positive electrode, and the melting point of the thermoplastic resin particles is 125 to 150 ° C. More preferably, the melting point is preferably changed in consideration of the thermal stability of the positive electrode.
• the thermoplastic resin particles have a plurality of melting points, the highest temperature melting point may be within the above range.
• thermoplastic resin particles When the thermoplastic resin particles are included in the porous layer of the laminated porous film of the present invention, it is not particularly limited as long as it is composed of a thermoplastic resin having a melting point falling within the above range, but the heat composed of an olefin resin.
• Plastic resin particles are preferable, and thermoplastic resin particles made of an olefin resin such as polyethylene, polyethylene copolymer, polypropylene, and polypropylene copolymer are particularly preferable.
• the average particle size of the thermoplastic resin particles is preferably 0.5 to 5 ⁇ m, more preferably 0.8 to 3 ⁇ m.
• the proportion in the porous layer is preferably 10 to 40% by mass, more preferably 15 to 35% by mass.
• the pores in the porous layer may not be sufficiently blocked during heat generation, and the shutdown property may not be exhibited.
• it exceeds 40 mass% the heat resistance at the time of using a laminated porous film as a separator may fall.
• the coating liquid for forming the porous layer is prepared by dispersing the above-described components for forming the porous layer in a solvent.
• Any solvent can be used for the coating liquid as long as it can be stably dispersed without reacting with the components forming the porous layer.
• the resin A solvent having a boiling point of from 120 ° C. to the melting point or softening point of C
• the solvent of the coating liquid for forming the porous layer an alcohol solvent having a boiling point of about 60 to 120 ° C., water, and a mixed liquid of the alcohol solvent and water can be preferably used.
• a method for preparing the coating liquid used for the porous layer of the laminated porous film a method of mixing the composition with a dispersing device can be mentioned.
• the mixing apparatus include a ball mill, a bead mill, a jet mill, a homogenizer, and an ultrasonic disperser, but any method may be used.
• the laminated porous film of the present invention as a method for forming a porous layer, other compositions such as inorganic particles (A), at least two water-soluble polymers (B), a resin (C), a solvent and the like are contained.
• a method of applying a coating liquid is preferably employed.
• any generally performed method may be used.
• the coating may be performed by a coating method such as a reverse coating method, a bar coating method, a gravure coating method, a rod coating method, a die coating method, or a spray coating method. What is necessary is just to apply
• you may add a dispersing agent etc. suitably in order to prevent the uneven distribution of the inorganic particle (A) in a porous layer.
• the viscosity of the coating liquid used for forming the porous layer is preferably 30 mPa ⁇ s or more and 500 mPa ⁇ s or less, more preferably 50 mPa ⁇ s or more and 300 mPa ⁇ s or less, and still more preferably 70 mPa ⁇ s. ⁇ S to 200 mPa ⁇ s.
• the viscosity of the coating liquid is less than 30 mPa ⁇ s, the fluidity of the coating liquid is high during the formation of the coating film, which may cause defects such as repellency.
• the viscosity of the coating liquid forming the porous layer can be controlled in the above range by the amount of inorganic particles (A), water-soluble polymer (B1), water-soluble polymer (B2) added.
• the viscosity of the coating liquid is measured with a tuning fork type vibration viscometer at 25 ° C. and a natural frequency of 30 Hz.
• the drying temperature in the coating step for forming the porous layer is from the viewpoint of melting and binding the resin (C) and from the viewpoint of keeping the flatness by suppressing the thermal shrinkage of the laminated porous film.
• the melting point or softening point of the resin (C) is preferably from 120 to 120 ° C., more preferably from the melting point or softening point of the resin (C) to 5 to 120 ° C. If the melting point or softening point of the resin (C) is not reached, the resin (C) does not melt or soften, so that the binding property is inferior, or the moisture content of the porous layer becomes high, which causes problems when used as a battery separator. May occur. Moreover, when it exceeds 120 degreeC, shrinkage
• the air resistance of the laminated porous film is preferably 50 to 500 seconds / 100 ml. If the air permeability resistance is less than 50 seconds / 100 ml, the insulation between the electrodes may not be sufficiently maintained. On the other hand, if it exceeds 500 seconds / 100 ml, the output characteristics of the battery may be deteriorated when the laminated porous film is used as a separator.
• the air resistance of the laminated porous film is preferably 80 to 490 seconds / 100 ml, more preferably 150 to 390 seconds / 100 ml, although it depends on the application.
• the method for setting the air resistance of the laminated porous film in the above range can be achieved by containing inorganic particles (A) having an aspect ratio of 2 or more in the porous layer.
• the air resistance of the laminated porous film can be confirmed by a method described later.
• the thermal contraction rate in the longitudinal direction and the width direction of the laminated porous film of the present invention at 150 ° C. is preferably 0 to 3%, more preferably 0 to 2%.
• the thermal shrinkage rate in the longitudinal direction and the width direction of the film at 150 ° C. is larger than 3%, when used as a battery separator, the film may easily shrink due to generated heat and cause a short circuit. On the other hand, if it is less than 0%, it may affect the dimensional stability of the battery itself when used as a battery separator, which may cause problems.
• the porous layer contains the specific water-soluble polymer (B) described above and the specific inorganic particles described above ( It can be effectively achieved by using A). The heat resistance of the laminated porous film can be confirmed by a method described later.
• the porous film constituting the laminated porous film of the present invention and the method for producing the laminated porous film will be specifically described.
• stacking porous film of this invention is not limited to this.
• the porous film a polypropylene porous film by a ⁇ crystal method, and the composition of the porous layer is inorganic carbonate (A) calcium carbonate, water-soluble polymer (B) carboxymethylcellulose (B1) and hydroxyethylcellulose (B2), An example in which a modified polyethylene emulsion is used for the resin (C) will be described.
• the polypropylene resin As the polypropylene resin, 94.7% by mass of a commercially available homopolypropylene resin having an MFR of 8 g / 10 min, 5 parts by mass of an ultra-low density polyethylene resin having a melt index of 18 g / 10 min, N, N′-dicyclohexyl-2,6-naphthalenedicarboxy
• the raw material which mixed 0.3 mass% of amides and mixed beforehand in the predetermined ratio using the twin-screw extruder is prepared. At this time, the melting temperature is preferably 270 to 300 ° C.
• the mixed raw material is supplied to a single-screw melt extruder, and melt extrusion is performed at 200 to 230 ° C. And after removing a foreign material, a modified polymer, etc. with the filter installed in the middle of the polymer pipe
• the surface temperature of the cast drum is preferably 105 to 130 ° C. from the viewpoint of controlling the ⁇ crystal form performance of the cast film to be high.
• the end portion is sprayed with spot air to adhere to the drum.
• the polymer may be brought into close contact with the cast drum using a method in which air is blown over the entire surface from the contact state of the entire sheet on the drum using an air knife or an electrostatic application method as necessary.
• the unstretched sheet obtained is biaxially oriented to form pores in the film.
• a biaxial orientation method the film is stretched in the longitudinal direction of the film and then stretched in the width direction, or the sequential biaxial stretching method in which the film is stretched in the width direction and then stretched in the longitudinal direction.
• the simultaneous biaxial stretching method can be used, but it is preferable to adopt the sequential biaxial stretching method in that it is easy to obtain a highly air-permeable film, and in particular, it is possible to stretch in the width direction after stretching in the longitudinal direction. preferable.
• the unstretched sheet is controlled to a temperature for stretching in the longitudinal direction.
• a temperature control method a method using a temperature-controlled rotating roll, a method using a hot air oven, or the like can be adopted.
• the stretching temperature in the longitudinal direction is preferably 90 to 140 ° C, more preferably 110 to 135 ° C.
• the draw ratio is 3 to 6 times, more preferably 4 to 5.5 times.
• the end of the film is gripped and introduced into a stenter type stretching machine. Then, it is preferably heated to 130 to 155 ° C. and stretched 2 to 12 times, more preferably 4 to 10 times in the width direction.
• the transverse stretching speed at this time is preferably 300 to 5,000% / min, more preferably 500 to 3,000% / min.
• heat setting is performed in the stenter as it is, and the temperature is preferably from the transverse stretching temperature to 165 ° C. Further, the heat setting may be performed while relaxing in the longitudinal direction and / or the width direction of the film, and in particular, the relaxation rate in the width direction is preferably 5 to 35% from the viewpoint of thermal dimensional stability.
• this coating solution After stirring this coating solution for 4 hours, it is applied on the porous film by a coating method using a die coater and dried at 100 ° C. for 1 minute to form a porous layer having a laminated thickness of 1 to 30 ⁇ m.
• the laminated porous film of the present invention Since the laminated porous film of the present invention has excellent output characteristics, flatness, and air permeability, it can be suitably used as a separator for an electricity storage device.
• the electricity storage device include various batteries, particularly non-aqueous electrolyte secondary batteries represented by lithium ion secondary batteries, and electric double layer capacitors such as lithium ion capacitors. Since such an electricity storage device can be repeatedly used by charging and discharging, it can be used as a power supply device for industrial devices, household equipment, electric vehicles, hybrid electric vehicles, and the like.
• the electricity storage device using the laminated porous film of the present invention as a separator can be suitably used for industrial equipment and automobile power supply devices because of the excellent characteristics of the separator.
• the melting peak observed when the temperature is raised (second run) again at 10 ° C / min after holding for 5 minutes is the melting peak of 145 ° C to 157 ° C and the melting peak of the ⁇ crystal is 158 ° C or higher
• the melting of the ⁇ crystal is taken as the melting peak of the ⁇ crystal, and the melting heat of the ⁇ crystal is obtained from the area of the region surrounded by the baseline and the peak drawn from the flat part on the high temperature side.
• the heat of fusion of ⁇ H ⁇ and ⁇ crystals was ⁇ H ⁇
• the value calculated by the following formula was defined as ⁇ crystal forming ability.
• the heat of fusion was calibrated using indium.
• ⁇ crystal forming ability (%) [ ⁇ H ⁇ / ( ⁇ H ⁇ + ⁇ H ⁇ )] ⁇ 100
• the sample used for the measurement of the thickness is selected from a total of 10 arbitrary positions at intervals of at least 5 cm in the longitudinal direction, and the average of the measured values of the 10 samples is the thickness (la) of the laminated porous film of the sample, The thickness (lb) and the porous layer thickness (lc) were used.
• the surface pore size ratio of the sample was calculated.
• Surface pore diameter ratio (N A ) / (N B )
• Air permeation resistance of laminated porous film Air permeation resistance of laminated porous film A square of 150 mm in length on one side of the laminated porous film was taken as a cut sample, and a B-shaped Gurley tester of JIS P 8117 (2009) was used, and the relative humidity was 65%. Then, the permeation time of 100 ml of air was measured at three arbitrary locations. The average value of the permeation times at three locations was taken as the air resistance of the laminated porous film.
• the major axis and minor axis of the particles were determined using image analysis software, and the values were inserted into the following formula to obtain the aspect ratio of the particles in the porous layer.
• the aspect ratio was calculated for 100 particles, and the average was taken as the aspect ratio of the inorganic particles (A) in the porous layer.
• Aspect ratio long particle diameter / short particle diameter
• the laminated porous film was cut into rectangles whose longitudinal and width directions were 150 mm x 10 mm and 10 mm x 150 mm, respectively, and used as samples. Marks were drawn on the sample at intervals of 100 mm, and a heat treatment was performed by placing in a hot air oven heated to 150 ° C. with a 3 g weight suspended for 1 hour. After the heat treatment, it was allowed to cool, the distance between the marked lines was measured, and the thermal shrinkage rate in the longitudinal direction and the width direction was calculated from the change in the distance between the marked lines before and after heating, and used as an index of dimensional stability. The measurement was carried out at 5 points each in the longitudinal direction and the width direction, and the average value was taken as each measured value.
• the absolute value of the measurement value in the longitudinal direction and the width direction was evaluated according to the following criteria in the direction in which the shrinkage rate was large.
• Rate of change K of friction coefficient ⁇ k Using a tape runnability tester TBT-300 (manufactured by Yokohama System Laboratory Co., Ltd.), a laminated porous film slit into a tape shape with a width of 1 cm is run in an atmosphere of 23 ° C. and 50% RH, and friction. The coefficient ⁇ k was determined. The sample was installed so that the porous layer side was in contact with the guide. The guide diameter is 6 mm ⁇ , the guide material is SUS27 (surface roughness 0.2S), the winding angle is 90 °, the running speed is 3.3 cm / sec, and the repetition is 1 to 50 times.
• Friction coefficient change rate K (%) (Friction coefficient at the 50th repetition ( ⁇ k 50 ) / Friction coefficient at the first repetition ( ⁇ k 1 )) ⁇ 100
• LiCoO 2 lithium cobalt oxide
• the negative electrode, the laminated porous film or porous film, and the positive electrode are stacked in this order so that the positive electrode active material and the negative electrode active material surface face each other, and a small stainless steel container with a lid (manufactured by Hosen Co., Ltd., HS cell, The spring pressure was 1 kgf).
• the container and the lid are insulated, the container is in contact with the negative electrode copper foil, and the lid is in contact with the positive electrode aluminum foil.
• the discharge capacity 50 at the 50th charge / discharge was measured, and the cycle characteristics obtained by the formula of [(discharge capacity 50 / discharge capacity 1) ⁇ 100] were evaluated according to the following criteria. In addition, 10 test pieces were measured and evaluated by the average value. A: 90% or more B: 70% or more and less than 90% C: Less than 70% or one or more is less than 20%.
• Peel strength is 10 to 500 g / 25 mm width
• Peel strength is outside the range of 10 to 500 g / 25 mm width, or peel strength is in the range of 10 to 500 g / 25 mm width
• breakage occurs in the porous layer or breakage occurs in the porous film layer.
• Viscosity of coating liquid Using a tuning fork type vibration viscometer (“SV-1A” manufactured by A & D Co., Ltd.), change the viscosity of 2 ml of coating liquid at a circulating water temperature of 25 ° C. and change the sampling location of the coating liquid. Three measurements were taken. The average value of the three times of viscosity was defined as the viscosity of the coating liquid.
• SV-1A tuning fork type vibration viscometer
• high density polyethylene density 0.95, viscosity average molecular weight 250,000
• extrusion was performed from a T die attached to the tip of the extruder. Immediately, it was cooled and solidified with a cast roll cooled to 25 ° C. to form an unstretched sheet having a thickness of 1.2 mm.
• This unstretched sheet was stretched 7 ⁇ 7 times at 120 ° C. with a simultaneous biaxial stretching machine, then dipped in methylene chloride, extracted after removing liquid paraffin, and dried at 125 ° C. with a tenter stretching machine. After stretching in the transverse direction by 1.5 times, heat treatment was performed by relaxing in the width direction by 7% at 130 ° C. to obtain a porous film 1 having a thickness of 18 ⁇ m.
• the resulting porous film had an air resistance of 200 seconds / 100 ml and a porosity of 40%.
• the composition for forming the porous layer was weighed and mixed according to the formulation shown in Table 1-2 to prepare a coating solution for forming the porous layer. This was coated on one side of the porous film (the surface in contact with the drum during melt extrusion, hereinafter referred to as D-side) using a die coater so that the laminated thickness after drying was 7 ⁇ m, and 100 ° C. Was dried for 1 minute to form a porous layer, and a laminated porous film was produced.
• Example 2 to 12 94.45% by mass of polypropylene (manufactured by Sumitomo Chemical Co., Ltd., FLX80E4) as resin (D), which is the raw material of the porous film, “Engage” manufactured by Dow Chemical, which is an ethylene-octene-1 copolymer (Registered trademark) "8411 (melt index: 18 g / 10 min, hereinafter simply referred to as PE-1) is added to 5% by mass, and N, N'-dicyclohexyl-2,6-naphthalene, a ⁇ crystal nucleating agent, is added.
• PE-1 ethylene-octene-1 copolymer
• This chip is supplied to a single screw extruder and melt extruded at 220 ° C. After removing foreign matter with a 25 ⁇ m cut sintered filter, it is discharged from a T-die onto a cast drum whose surface temperature is controlled at 120 ° C. Casting was performed indirectly for 15 seconds to obtain an unstretched sheet having a thickness of 200 ⁇ m and a width of 250 mm. Next, preheating was performed using a ceramic roll heated to 120 ° C., and the film was stretched 4.5 times in the longitudinal direction of the film. After cooling, the end portion was introduced into a tenter type stretching machine by holding it with a clip, and stretched 6 times at 145 ° C. As it was, heat treatment was performed at 155 ° C.
• the composition for forming the porous layer was weighed and mixed according to the formulation shown in Table 1-2, and the porous layer was formed on the porous film in the same manner as in Example 1 to obtain a laminated porous film.
• each layer was dried at 60 ° C. and 130 ° C. for 1 minute to form a porous layer, thereby producing a laminated porous film.
• Example 1 The porous film before forming the porous layer in Example 2 was evaluated as it was.
• composition used for coating solution Inorganic particles (A) ⁇ Calcium carbonate “PC” manufactured by Calcium Shiraishi Co., Ltd., average particle size 3.0 ⁇ m, aspect ratio 4 ⁇ Silica Denki Kagaku Kogyo "SFP-30", average particle diameter 0.7 ⁇ m, aspect ratio 1
• Water-soluble polymer (B1) ⁇ Carboxymethylcellulose A (CMC A) “CMC Daicel 1220” manufactured by Daicel Finechem Co., Ltd. ⁇ Carboxymethylcellulose B (CMC B) "CMC Daicel 2200” manufactured by Daicel Finechem Co., Ltd. ⁇ Polyacrylic acid "AS58” manufactured by Nippon Shokubai Co., Ltd. ⁇ Polyacrylamide "Polystron 117” manufactured by Arakawa Chemical Industries, Ltd.
• Water-soluble polymer (B2) ⁇ Hydroxyethyl cellulose A (HEC A) “HEC EP-850” manufactured by Daicel Finechem Co., Ltd. ⁇ Hydroxyethyl cellulose B (HEC B) "HEC EE-820” manufactured by Daicel Finechem Co., Ltd. ⁇ Polyvinyl alcohol “Goselan L3266” manufactured by Nippon Synthetic Chemical Industry Co., Ltd.
• Resin (C) ⁇ Modified polyethylene aqueous dispersion (modified PE) “Chemical S-100” manufactured by Mitsui Chemicals, Inc., 20% by weight solids diluted product ⁇ Styrene butadiene rubber aqueous dispersion (SBR) “TRD2001” manufactured by JSR Corporation , 20% by weight solid content diluted product
• Example 1 The evaluation results for the samples of Examples 1 to 12 and Comparative Examples 1 to 5 are shown in Tables 1-3 and 2-3.
• the peel strength was slightly weak due to the influence of the base material and particles, and the evaluation was B.
• the bond with the base material was slightly weak due to the influence of the binder (resin (C)) used, and the peel strength was evaluated as B.
• the amount of the binder (resin (C)) was small, the binding with the base material was slightly weak, and the peel strength was evaluated as B.
• Example 10 since the binding between the porous layer and the porous film was strong and the breakage occurred in the layer of the porous film, the peel strength was evaluated as B.
• Example 11 since the drying temperature was low, destruction occurred in the layer of the porous layer, and the peel strength was evaluated as B.
• the laminated porous film of the present invention can achieve heat resistance, low moisture content and high quality, it has excellent safety and battery performance, is low in cost, and is an electricity storage device, particularly a non-aqueous electrolyte secondary battery. It can use suitably as a separator of a lithium ion battery.

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