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WO2020045627A1 - Metal plate for cell container, and method for manufacturing metal plate for cell container - Google Patents

Metal plate for cell container, and method for manufacturing metal plate for cell container Download PDF

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Publication number
WO2020045627A1
WO2020045627A1 PCT/JP2019/034121 JP2019034121W WO2020045627A1 WO 2020045627 A1 WO2020045627 A1 WO 2020045627A1 JP 2019034121 W JP2019034121 W JP 2019034121W WO 2020045627 A1 WO2020045627 A1 WO 2020045627A1
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WO
WIPO (PCT)
Prior art keywords
metal plate
battery container
base material
layer
plating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2019/034121
Other languages
French (fr)
Japanese (ja)
Inventor
利文 小柳
興 吉岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Kohan Co Ltd
Original Assignee
Toyo Kohan Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Kohan Co Ltd filed Critical Toyo Kohan Co Ltd
Priority to JP2020539627A priority Critical patent/JP7413264B2/en
Priority to CN201980056086.0A priority patent/CN112639171A/en
Priority to KR1020217002247A priority patent/KR102872693B1/en
Publication of WO2020045627A1 publication Critical patent/WO2020045627A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/116Primary casings; Jackets or wrappings characterised by the material
    • H01M50/117Inorganic material
    • H01M50/119Metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/01Layered products comprising a layer of metal all layers being exclusively metallic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/04Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B15/08Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • B32B15/085Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin comprising polyolefins
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C28/00Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10Electroplating with more than one layer of the same or of different metals
    • C25D5/12Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00Electroplating characterised by the article coated
    • C25D7/06Wires; Strips; Foils
    • C25D7/0614Strips or foils
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/116Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/116Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • H01M50/126Primary casings; Jackets or wrappings characterised by the material having a layered structure comprising three or more layers
    • H01M50/129Primary casings; Jackets or wrappings characterised by the material having a layered structure comprising three or more layers with two or more layers of only organic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/131Primary casings; Jackets or wrappings characterised by physical properties, e.g. gas permeability, size or heat resistance
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/131Primary casings; Jackets or wrappings characterised by physical properties, e.g. gas permeability, size or heat resistance
    • H01M50/133Thickness
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/102Primary casings; Jackets or wrappings characterised by their shape or physical structure
    • H01M50/105Pouches or flexible bags
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present invention relates to a metal plate suitable for a battery container such as a lithium ion secondary battery and a method for producing the metal plate for a battery container.
  • a lithium-ion secondary battery (hereinafter, also referred to as “LiB”) has attracted attention as a high-output, long-life high-performance battery.
  • LiB lithium-ion secondary battery
  • battery containers for accommodating a non-aqueous electrolyte, a positive electrode active material, a negative electrode active material, and the like also take various forms such as a cylindrical shape and a rectangular shape.
  • Patent Literature 1 discloses a technique of accommodating electrodes and the like in a pouch using a laminated metal plate in which a thin metal plate is coated with a resin. According to Patent Document 1, it is mentioned that iron or an alloy of iron is used as a metal foil core material.
  • Patent Documents 2 and 3 a rolled metal plate having a thickness of 200 ⁇ m or less is used, Ni is plated on the rolled metal plate, and then rolling and heat treatment are performed.
  • a technique for forming a diffusion alloy layer containing Ni and Fe is disclosed.
  • a polyolefin-based resin may be formed on a rolled metal plate in order to improve corrosion resistance against an electrolytic solution or the like.
  • the use of the diffusion alloy layer allows the rolled metal plate and the polyolefin-based resin to be formed. It is mentioned that the adhesiveness is improved.
  • the surface treatment layer (plating layer) formed on the base material side is required to have not only properties that can withstand severe processing but also content resistance and adhesion to the film.
  • a metal plate for a battery container has excellent workability (formability), adhesion to a film, and content resistance to a non-aqueous electrolyte such as an organic electrolyte obtained by dissolving a lithium salt in an organic solvent. Improving is very important for gaining competitiveness.
  • An object of the present invention is to solve the above-described problem as an example.For example, even when performing a forming process using a metal plate for battery use, it is possible to suppress cracking of the base material and peeling of the resin, and the coating is performed.
  • the object of the present invention is to provide a metal plate for a battery container, which has excellent adhesion to a resin film, and has excellent content resistance to a nonaqueous electrolytic solution filled in the container, and a method for producing the metal plate for a battery container. I do.
  • a metal plate for a battery container is (1) a metal plate for a battery container used as a battery container, which is made of iron or an alloy of iron and has a thickness of 10 mm.
  • a substrate which is ⁇ 100 [mu] m, at least formed on one surface, 0.5 ⁇ 50.0g / m 2 of Ni plating layer and 0.05 Cr plating ⁇ 10.0 g / m 2 of the substrate And an electroplating layer containing at least one of the layers.
  • the electrochromic plating layer has a higher proportion of metallic Cr than a proportion of hydrated Cr oxide.
  • the electric Ni plating layer is a Ni plating layer composed of only Ni, or a Fe—Ni diffusion layer in which Fe is diffused. , And one selected from Fe-Ni alloy plating layers in which both Fe and Ni are electrodeposited.
  • a surface of the base material which is an inner surface side of the battery container is coated with a polyolefin-based resin. Is preferred.
  • the polyolefin-based resin is a polypropylene resin, and an acid-modified polyolefin layer is interposed between the base material and the polypropylene resin. Is preferred.
  • a surface of the base material which is an outer surface side of the battery container may be a polyester resin, a polyamide resin, or a polyolefin. Preferably, it is coated with one of the resins.
  • the tensile strength of the base material is 260 to 700 MPa, and the elongation of the base material is 5 to 55%. It is preferred that
  • the ratio of the crystal grain size in the plane direction and the thickness direction of the base material is 0.8 to 8. Is preferred.
  • the Ni plating layer and the Ni plating layer An electroplating layer containing at least one of a Cr plating layer is formed, and a surface of the substrate on the outer surface side of the battery container is a Zn plating layer or a Zn alloy of 3 to 30 g / m 2. It is preferable that an electroplating layer containing a plating layer is formed.
  • a method for manufacturing a metal plate for a battery container is a method for manufacturing a metal plate for a battery container including a base material of iron or an alloy of iron, Cold rolling the material to a thickness of 10 to 100 ⁇ m; and forming a Ni plating layer of 0.5 to 50.0 g / m 2 on at least one surface of the base material and a 0.05 to 10. forming an electroplated layer containing at least one of Cr plating layer 0 g / m 2, and having a.
  • ADVANTAGE OF THE INVENTION According to this invention, it can withstand severe shaping
  • a metal plate for a battery container can be realized.
  • the metal plate 10 for a battery container of the present embodiment will be described with reference to FIG.
  • the thickness direction of the battery container metal plate 10 will be referred to as the Z direction
  • the rolling direction of the battery container metal plate 10 will be referred to as the X direction.
  • the definition of these directions does not reduce the scope of the present invention.
  • the metal plate 10 for a battery container according to the present embodiment has a surface treatment layer 2 (electroplating layer 2) on a substrate 1 made of iron or an alloy of iron.
  • the iron alloy include various steel plates applicable as a base material of a battery container.
  • low carbon aluminum killed steel carbon content of 0.01 to 0.15% by weight
  • Ultra-low carbon steel having a carbon content of 0.003% by weight or less or non-aging ultra-low carbon steel obtained by further adding Ti or Nb to ultra-low carbon steel is also included.
  • the thickness of the base material 1 according to the present embodiment is preferably 10 to 100 ⁇ m, more preferably 15 to 60 ⁇ m.
  • the quality tends to be unstable, such as generation of pinholes in the cold rolling step or unstable thickness difference.
  • cracks may occur in the molding process, and the effects intended by the present application may not be obtained.
  • the thickness exceeds 100 ⁇ m, the effect of weight reduction cannot be obtained.
  • the base material 1 is desirably ultra-low carbon steel, and has a thickness of 20 to 80 ⁇ m. And more preferably 30 to 60 ⁇ m.
  • C 0.0001 to 0.1% by weight
  • C is an element that increases the strength of the substrate 1. If the content of C is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the content of C is set to 0.1% by weight.
  • the lower limit of the C content is not particularly limited, but the lower limit of the C content is 0.0001% by weight in consideration of cost.
  • the content of C is more preferably 0.0005 to 0.03% by weight, and still more preferably 0.001 to 0.01% by weight.
  • Si 0.001 to 0.5% by weight
  • Si is an element that increases the strength of the substrate 1. If the Si content is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the Si content is set to 0.5% by weight.
  • the lower limit of the Si content is not particularly limited, but the lower limit of the Si content is 0.001% by weight in consideration of cost. The content of Si is more preferably 0.001 to 0.02% by weight.
  • Mn is an element that increases the strength of the substrate 1. If the content of Mn is excessive, the strength is excessively increased and the rollability decreases, so the upper limit of the content of Mn is set to 1.0% by weight.
  • the lower limit of the Mn content is not particularly limited, but the lower limit of the Mn content is set to 0.01% by weight in consideration of cost.
  • the Mn content is more preferably 0.01 to 0.5% by weight.
  • P is an element that increases the strength of the substrate 1. If the content of P is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the content of P is set to 0.05% by weight.
  • the lower limit of the P content is not particularly limited, but the lower limit of the P content is 0.001% by weight in consideration of cost. The P content is more preferably 0.001 to 0.02% by weight.
  • S is an element that lowers the corrosion resistance of the substrate 1. Therefore, the smaller the S content, the better. In particular, when the content of S exceeds 0.02% by weight, the corrosion resistance is significantly reduced, so the upper limit of the content of S is set to 0.02% by weight.
  • the lower limit of the S content is not particularly limited, but the lower limit of the S content is set to 0.0001% by weight in consideration of cost. The S content is more preferably 0.001 to 0.01% by weight.
  • Al 0.0005 to 0.20% by weight
  • Al is added, for example, as a deoxidizing element for the substrate 1.
  • the Al content is preferably set to 0.0005% by weight or more.
  • the upper limit of the Al content is set to 0.20% by weight.
  • the lower limit of the Al content is not particularly limited, but the lower limit of the Al content is 0.0005% by weight in consideration of cost.
  • the content of Al is more preferably 0.001 to 0.10%.
  • N is an element that lowers the workability of the substrate 1. Therefore, the smaller the content of N, the better. In particular, when the content of N exceeds 0.0040% by weight, the workability is significantly reduced. Therefore, the upper limit of the content of N is set to 0.0040% by weight.
  • the lower limit of the N content is not particularly limited, but the lower limit of the N content is 0.0001% by weight in consideration of cost.
  • the content of N is more preferably 0.001 to 0.0040% by weight.
  • the main element in the remainder of the base material 1 is Fe, and the other elements are impurities which are inevitably mixed during the production.
  • Ti, Nb, B, Cu, Ni, Sn, Cr and the like may be contained as additional components.
  • Ti and Nb have the effect of fixing C and N in the base material 1 as carbides and nitrides and improving the workability of the base material 1, so that Ti: 0.01 to 0.8% by weight, Nb: One or two kinds may be contained in the range of 0.005 to 0.05% by weight.
  • the base material 1 according to the present embodiment is more preferably a steel sheet having less than 10.5% of Cr.
  • the base material 1 according to the present embodiment preferably has at least one of the following characteristics by being annealed after being cold-rolled.
  • the temperature and time required for annealing in the present embodiment are 2 to 9 hours, more preferably 2 to 6 hours when the annealing is performed at 450 ° C. to 650 ° C. (more preferably 500 to 600 ° C.).
  • the required time is 20 to 120 seconds.
  • the tensile strength of the substrate 1 according to the present embodiment is preferably from 260 to 700 MPa. If the tensile strength is less than 260 MPa, there is a problem in that when used as a battery container, it is deformed by an external force, thereby generating cracks and holes, thereby causing leakage of the electrolyte. Further, when the tensile strength exceeds 700 MPa, the workability becomes poor.
  • the tensile strength of the substrate 1 is more preferably 270 to 650 MPa. When more workability is required, it is more preferably 280 to 450 MPa.
  • the tensile strength of the substrate 1 was measured according to the “metallic material tensile test method” described in JIS standard Z2241.
  • the elongation of the substrate 1 according to the present embodiment is preferably 5 to 55%. If the elongation of the base material 1 is less than 5%, workability is poor at corners (corners), and cracks may occur during processing. On the other hand, if the elongation exceeds 55%, a high temperature and a long time are required as annealing conditions for obtaining such characteristics, so that productivity is deteriorated.
  • the elongation of the substrate 1 is more preferably 15 to 55%, and further preferably 20 to 50%.
  • the elongation of the base material 1 was performed according to "Equation (7) of measurement of elongation at break (%) A" of "metallic material tensile test method" described in JIS standard Z2241.
  • the elongation of the base material 1 is preferably 20% or more, and more preferably 30% or more, from the viewpoint of suppressing cracking of the base material 1 during molding and peeling of the resin film from the base material 1. It is still desirable.
  • the ratio of the crystal grain size in the plane direction (rolling direction) and the thickness direction (plane direction / thickness direction) of the substrate 1 according to this embodiment is preferably 0.8 to 8.
  • the “crystal grain size” in the present embodiment is an average value of the crystal grain size existing per unit area (for example, 1 ⁇ m ⁇ 1 ⁇ m).
  • There is no particular limitation on the method of measuring the average crystal grain size For example, a cross-sectional photograph of a metal plate is taken with a scanning electron microscope (SEM) and then, in accordance with JIS G0551 (Annex B or C). Can be measured.
  • the crystal grain size is determined based on each of the test line along the plane direction and the test line along the thickness direction, and the ratio is calculated.
  • the ratio of the crystal grain size described above may be calculated by comparing the longest length value in the rolling direction and the longest length value in the thickness direction in each of the plurality of particles to be measured. It is difficult for the substrate 1 to have a crystal grain ratio of less than 0.8 in a general manufacturing method. On the other hand, when the above-mentioned ratio of crystal grain diameters exceeds 8, cracks are likely to occur during processing.
  • the ratio of the crystal grain diameter of the substrate 1 is more preferably 0.8 to 5. When more workability is required, the ratio of the crystal grain size of the substrate 1 is more preferably 0.8 to 4.
  • a surface treatment layer 2 (also referred to as an electroplating layer) by electroplating is formed on at least a surface on the inner surface side of the battery container on the base material 1 according to the present embodiment.
  • the surface of the substrate 1 on the outer surface side of the battery container is the same as the above-mentioned inner surface or at least one layer from the viewpoint of establishing oxidation prevention and ease of manufacture.
  • the surface treatment layer 2 may be formed.
  • the surface treatment layer 2 is formed by electroplating, for example, to improve adhesion to a resin film when immersed in an electrolytic solution and to ensure corrosion resistance to the electrolytic solution when the resin film has a defect.
  • Examples thereof include a Cr plating layer to be formed, and a Ni alloy plating exemplified by a Ni plating layer and an Fe—Ni alloy plating layer. Further, a plurality of these plating layers may be provided. For example, a Ni plating layer may be formed on the base material 1 and then a Cr plating layer may be formed.
  • the surface treatment layer of this embodiment may be formed, for example, after the base material 1 is annealed after cold rolling, or formed after the base material 1 is cold-rolled and before annealing. It is also possible.
  • the Fe—Ni diffusion layer may be formed by heat treatment. At this time, an Fe—Ni diffusion layer may be formed between the Ni plating layer and the substrate 1, or the iron of the substrate 1 diffuses throughout the Ni plating layer, and An Fe—Ni diffusion layer may be directly formed.
  • the surface treatment layers 2 are formed on both surfaces of the substrate 1 in FIG. 1, the surface treatment layer 2 may be formed on at least the inner surface of the battery container. Alternatively, different types of surface treatment layers 2 (electroplating layers) may be formed on both surfaces of the substrate 1. For example, an electroplating layer (first electroplating layer) containing at least one of a Ni plating layer and a Cr plating layer is formed on a surface of the base material 1 on the inner surface side of the battery container.
  • first electroplating layer first electroplating layer containing at least one of a Ni plating layer and a Cr plating layer is formed on a surface of the base material 1 on the inner surface side of the battery container.
  • a Zn plating layer or a Zn alloy layer (for example, Zn—Ni, Zn—Co, Zn—Co—Mo, Zn—Fe, Zn—Sn) having a different corrosion resistance mechanism (as a sacrificial anticorrosion layer) is formed on the outer surface.
  • a second electroplating layer may be formed.
  • the electroplating layer containing the Zn plating layer or the Zn alloy plating layer as the sacrificial anticorrosion layer preferably has a Zn plating amount of, for example, 3 to 30 g / m 2 , and more preferably 5 to 25 g / m 2 . More preferably, the amount of plating is used.
  • Zn plating dissolves in the electrolytic solution, so it cannot be used as an inner surface that is always in contact.
  • it is effective for sacrificial corrosion prevention when a small amount of the electrolytic solution adheres.
  • Zn is preferentially dissolved at the end face, so that corrosion of the iron as the base material is prevented. This is effective because it can suppress the leakage of the electrolytic solution.
  • the cold-rolled metal plate is electrolytically degreased and pickled by a usual method, and then, for example, the following Ni plating bath is used as an example. be able to.
  • a Ni plating bath a nickel sulfate bath called a Watt bath is mainly used, but a sulfamic acid bath, a borofluoride bath, a chloride bath, or the like may be used.
  • Nickel sulfate 200-350g / l Nickel chloride: 20-60 g / l Boric acid: 10-50 g / l pH: 1.5 to 5.0 Bath temperature: 40-70 ° C Current density: 1 to 40 A / dm 2
  • the Ni plating as the surface treatment layer 2 formed on the substrate 1 is formed using not only pure Ni but also an alloy containing Ni such as a Ni—Co alloy or an Fe—Ni alloy. May be used.
  • the surface treatment layer 2 is made of one of a Ni plating layer composed of only Ni, an Fe—Ni diffusion layer in which Fe is diffused, and an Fe—Ni alloy plating layer in which both Fe and Ni are electrodeposited. May be included.
  • “composed of only Ni” means having only Ni as a metal element, and a substance derived from a plating bath additive or unavoidably mixed in a plating formation process. Impurities such as less than 1% carbon and less than 0.05% sulfur are allowed to be contained.
  • the Ni plating of this embodiment is preferably a Ni plating having a plating amount of 0.5 to 50.0 g / m 2 . If the plating amount of the Ni plating is less than 0.5 g / m 2 , the surface coverage is insufficient, the exposure of the base material is extremely increased, and there arises a problem that the content resistance is insufficient. On the other hand, if the plating amount of the Ni plating exceeds 50.0 g / m 2 , the thickness of the metal layer 10 increases due to an increase in the thickness of the plating layer, which leads to an increase in weight. Further, an increase in the plating processing time or the amount of plating causes a problem that productivity is lowered and manufacturing cost is increased.
  • an Fe—Ni diffusion layer can be formed.
  • the Fe—Ni diffusion layer preferably has a thickness of 0.2 ⁇ m or more and 3.0 ⁇ m or less.
  • the cold-rolled metal plate is electrolytically degreased and pickled by a usual method, and then, for example, the following Cr plating bath is used as an example. be able to.
  • Cr plating bath composition, conditions CrO 3 : 30 to 200 g / l NaF: 1 to 10 g / l pH: 1.0 or less Bath temperature: 35-65 ° C Current density: 5 to 50 A / dm 2
  • the Cr plating as the surface treatment layer 2 is preferably a Cr plating having a plating amount of 0.05 to 10.0 g / m 2 . If the plating amount of the Cr plating is less than 0.05 g / m 2 , the surface coverage is insufficient and the exposure of the base material 1 is extremely increased, resulting in a problem that the content resistance is insufficient. On the other hand, if the plating amount of the Cr plating exceeds 10.0 g / m 2 , similar problems as described above arise, such as an increase in weight, a decrease in productivity, and an increase in manufacturing cost.
  • the Cr plating layer has a higher proportion of metallic Cr than that of Cr hydrated oxide (CrOx).
  • CrOx Cr hydrated oxide
  • At least one surface of the metal plate 10 for a battery container according to the present embodiment may be covered with the thermoplastic resin 3.
  • the surface treatment layer 2 may be coated with a thermoplastic resin as a resin-coated metal plate for a battery container.
  • the battery container metal plate 10 may be configured as a laminate plate in which the surface treatment layer 2 is coated with a thermoplastic resin, or may have a configuration in which only the surface treatment layer 2 is formed. Is also good.
  • the thickness of such a thermoplastic resin 3 is 10 to 100 ⁇ m, and more preferably 10 to 50 ⁇ m.
  • thermoplastic resin 3 of the present embodiment a polyolefin resin, a polyester resin, or a polyamide resin is exemplified.
  • the polyolefin resin, polyester resin or polyamide resin preferably covers both surfaces of the battery container metal plate 10.
  • one surface (the inner surface side of the battery can) of the metal plate 10 for a battery container is preferably covered with a polyolefin-based resin (particularly, a polypropylene resin).
  • various polypropylene resins such as a random propylene resin, a homopropylene resin, and a block propylene resin may be used in a single layer, or they may be used as a multilayer by overlapping them.
  • a known additive may be added to the polypropylene resin.
  • additives include a low-crystalline ethylene butene copolymer, a low-crystalline propylene butene copolymer, a terpolymer composed of a three-component copolymer of ethylene, butene, and propylene, silica, zeolite, Examples thereof include anti-blocking agents such as acrylic resin beads and fatty acid amide-based slip agents.
  • a slip agent for improving the physical stability of the material
  • an antioxidant may be added as the above-mentioned additives.
  • the other surface (outer surface side of the battery can) of the metal plate 10 for a battery container is preferably coated with any of a polyester resin, a polyamide resin, and a polyolefin resin.
  • the polyester resin is preferably coated with polyethylene terephthalate.
  • the polyester resin in addition to polyethylene terephthalate, for example, polybutylene terephthalate, polyethylene naphthalate, polybutylene naphthalate, or the like can be used.
  • a modified resin such as a urethane-modified polyester resin, an acryl-modified polyester resin, or an epoxy-modified polyester resin may be used.
  • the thickness of the resin covering one surface (for example, the inner surface side of the battery can) and the thickness of the resin covering the other surface (for example, the outer surface side of the battery can) of the battery container metal plate 10 are required.
  • the thickness may be adjusted appropriately within the above thickness range depending on the corrosion resistance and workability, and the thickness of both surfaces may be the same or different.
  • the polyester resin is preferably non-oriented.
  • the other surface (outer surface side of the battery can) of the battery container metal plate 10 is not limited to the polyester resin (polyethylene terephthalate) described above. Good.
  • both surfaces of the battery container metal plate 10 may be covered with a polyester resin.
  • the thermoplastic resin 3 may be in a form in which the metal plate 10 for a battery container is covered with a known adhesive.
  • a known adhesive for example, an inorganic adhesive such as an acid-modified polyolefin resin, an epoxy resin, an acrylic resin, a urethane resin, a silicone resin, a polyisobutylene-based resin, a fluororesin, or water glass can be used.
  • an acid-modified polyolefin resin layer between the base material 1 and the thermoplastic resin 3 described above. In this case, the surface treatment layer 2, the acid-modified polyolefin layer, and the thermoplastic resin 3 are formed in this order from the substrate 1.
  • Such an acid-modified polyolefin layer is effective for improving the adhesion between the metal plate 10 for a battery container and the polypropylene resin, particularly when the thermoplastic resin 3 is a polypropylene resin.
  • Specific examples of the acid-modified polyolefin layer include, for example, polypropylene graft-modified with an unsaturated carboxylic acid, and a copolymer obtained by copolymerizing propylene with acrylic acid or methacrylic acid.
  • the acid-modified polyolefin layer is preferably an acid-modified polypropylene having a melting point of 145 ° C. to 165 ° C. from the viewpoint of preventing abnormal heat generation and surging and neck-in during melt extrusion.
  • the thermoplastic resin 3 may be laminated on the substrate 1 on which the surface treatment layer 2 is formed, or the thermoplastic resin 3 melted by heating may be extruded by an extrusion width of an extruder.
  • the film may be extruded into a film by the slit and directly laminated on the substrate 1 on which the surface treatment layer 2 is formed by an extrusion lamination method.
  • the presence or absence of stretching of the film is not particularly limited.
  • the film may be a non-stretched film, a uniaxially stretched film, or a biaxially stretched film.
  • the laminating method of the thermoplastic resin 3 may be different between one surface (the inner surface side of the battery can) and the other surface (the outer surface side of the battery can) of the metal plate 10 for a battery container.
  • the other surface (the outer surface side of the battery can) of the base material 1 is further coated on the surface treatment layer 2 with the thermoplastic resin 3 stretched via, for example, a two-component curable polyurethane-based adhesive.
  • a stretched PET film or a stretched polyamide film may be dry-laminated.
  • a method in which polypropylene and acid-modified polypropylene are extruded into a multilayer film and directly laminated on the surface treatment layer 2 a multilayer film of polypropylene and acid-modified polypropylene is prepared in advance, and A method of thermally laminating on the surface treatment layer 2 or the like can also be adopted.
  • a method for manufacturing the metal plate 10 for a battery container of the present embodiment will be described with reference to FIG.
  • a metal plate made of iron or an iron alloy is prepared, and cold rolling is performed by putting the metal plate into a rolling mill that performs press working (step 1).
  • a cold-rolled substrate 1 having a thickness of 10 to 100 ⁇ m is formed. This cold rolling may be performed in multiple stages as necessary, or a heat treatment may be performed in between.
  • an annealing treatment is performed on the obtained base material 1 (step 2).
  • the temperature of the substrate 1 in the annealing treatment is 450 to 650 ° C, more preferably 500 to 600 ° C.
  • the time required for this annealing treatment is 2 to 9 hours, more preferably 2 to 6 hours.
  • the annealing can be performed in 20 to 120 seconds, but is preferably performed in the former temperature range from the viewpoint of improving workability.
  • the substrate 1 is subjected to a surface treatment (plating treatment), and on at least one surface of the substrate 1, a surface treatment layer 2 (at least one of a Ni plating layer and a Cr plating layer) A plating layer is formed (Step 3).
  • the surface treatment layer 2 (electroplating layer) formed in step 3 is, for example, a plating amount of 0.5 to 50.0 g / m 2 for a Ni plating layer, and a plating amount for a Cr plating layer. Is preferably 0.05 to 10.0 g / m 2 .
  • the annealing in Step 2 may be performed after the surface treatment layer 2 is formed.
  • a heat treatment may be further performed, for example, for the purpose of improving workability.
  • the heat treatment at this time can be performed under the same conditions as the annealing conditions described in Step 2. If the rolling process of Step 1 is performed after the plating treatment, cracks may be generated on the surface of the Ni plating film, and the adhesion and corrosion resistance may be reduced, which is not preferable.
  • the substrate 1 after steps 2 and 3 has a tensile strength of 260 to 700 MPa, an elongation of 5 to 55%, and a ratio of the crystal grain size in the plane direction (rolling direction) of the substrate 1 to the thickness direction. It is preferable to have at least one of the characteristics of 0.8 to 8. After the steps 2 and 3 as described above, the metal plate 10 for a battery container can be obtained.
  • step 4 the substrate 1 on which the surface treatment layer 2 is formed is subjected to the above-described process of coating the thermoplastic resin 3 with a thickness of about 10 to 50 ⁇ m (resin coating process).
  • Step 4 is not an essential step in the method for manufacturing the metal plate 10 for a battery container of the present embodiment, and may be omitted as long as it is not configured as a laminate plate (a resin-coated metal plate for a battery container).
  • a polypropylene resin is formed on one surface of the substrate 1 on which the surface treatment layer 2 is formed on the inner surface side of the container, and polyethylene is formed on one surface on the outer surface side of the container. Forming a terephthalate resin or a polypropylene resin can be exemplified.
  • the method of forming the resin is such that, as described above, the side of the substrate 1 on which the surface treatment layer 2 is formed on the container outer surface side employs a dry lamination method via a urethane-based adhesive, The extrusion lamination method via a molten acid-modified polypropylene can be adopted on the side to be formed.
  • the lamination method is not limited to the above, and any side of the substrate 1 on which the surface treatment layer 2 is formed may be a film lamination or an extrusion lamination.
  • the temperature of the substrate 1 on which the surface treatment layer 2 is formed when the thermoplastic resin 3 is coated is adjusted, for example, from room temperature to 280 ° C., and preferably 250 ° C. or lower according to the lamination mode.
  • a resin-coated metal plate for a battery container can be obtained.
  • the dry lamination method it is preferable to perform aging after dry lamination in a temperature environment of, for example, 30 to 100 ° C. for a period of 1 to 7 days.
  • the container shape of the present embodiment has a depth in which corners of a radius of curvature Rc (referred to as Rc because it is a corner in the circumferential direction) are formed at four corners so that a rectangular electrode plate can be accommodated.
  • D has a rectangular concave portion.
  • the side wall of the concave portion and the bottom surface of the concave portion are connected by a radius of curvature Rp (referred to as Rp because it is defined by R of the punch).
  • Rp radius of curvature
  • the corners R of the four corners of the above-mentioned concave portion are equal, but Rc and Rp may be different values.
  • the reason why the metal plate 10 for a battery case of the present embodiment is very effective for the shape of the battery case having the shapes of the curvature radii Rc and Rp and the depth D will be described in detail below.
  • Rc and Rp and depth D for higher capacity
  • Rc at the four corners of the above-described concave portion during molding, Rp between the side wall and the bottom surface of the concave portion, and depth D are important, but the balance between Rp and depth D is particularly important. Establishing such a balance is ideal because it is ideal to increase the size of each battery so that the battery characteristics of multiple batteries can be guaranteed by one battery. This is particularly important as a battery container for use in vehicles. It is important not only for a single-cell battery but also for a case where a plurality of batteries are assembled and used as a module.
  • Rc and Rp described above it is desirable that both have as small a radius of curvature as possible from the viewpoint of further increasing the area in which the electrodes are arranged and reducing the dead space in the battery.
  • the value of such a radius of curvature Rp is preferably less than 2 mm, more preferably 1.5 mm or less.
  • the value of the radius of curvature Rc varies depending on the use and battery size used, but is preferably less than 10 mm, more preferably 8 mm or less, and still more preferably 5 mm or less, and particularly the length of the short side of the container. If it is less than 50 mm, it is preferably 3 mm or less.
  • the depth D is preferably 5 mm or more, more preferably 6 mm or more.
  • the present inventors have conducted intensive studies on the relationship between the desired radius of curvature Rp and the depth D.
  • the metal plate 10 for a battery container is processed under the above-described conditions to increase the capacity. In this case, there were problems in moldability, adhesion to the resin film after molding, and content resistance after molding.
  • the radius of curvature Rp is set to 1.5 mm or less, the degree of difficulty increases dramatically.
  • the depth D the deeper the forming process is performed, the more severe the processing conditions for the material of the battery container metal plate 10 become.
  • the following three problems occur when the condition that the curvature radius Rp is less than 2 mm and the condition that the depth D is 5 mm or more are combined.
  • the first problem is that the base material 1 is easily cracked during the forming process.
  • the thickness has to be increased and stable molding is difficult, so that it has not been put to practical use.
  • the waving and wrinkles of the flange portion when drawing is performed are increased, and the sealing of the container becomes uncertain.
  • the specific gravity is larger than that of aluminum, so that the thickness of the base material 1 is reduced to suppress an increase in battery weight. Need to be thin.
  • the substrate 1 itself may be used.
  • Content resistance is required. That is, when press molding is performed under severe processing conditions as described above, the resin film covering the substrate 1 may be damaged. Further, even when the resin film itself has a defect such as a pinhole in the first place, the defect tends to spread in severe molding processing. In such a case, since the electrolytic solution comes into contact with the surface of the substrate 1, it is necessary to make the surface of the substrate 1 difficult to elute. In the case where aluminum is used as the base material as in the prior art, processing under the above-mentioned strict processing conditions becomes impossible in the first place due to the poor formability of aluminum.
  • the battery case is hermetically sealed after accommodating battery elements such as an electrode plate and an electrolytic solution.
  • the metal plate for a battery case 10 of the present embodiment can also be applied as a lid member of a battery case used for sealing.
  • the lid member which is a constituent member of such a battery container, may have an accommodation space similar to that of the battery container body shown in FIG. 4 or may be used as a flat plate.
  • the battery container it is preferable to heat seal the lid with the lid member at a peripheral flange portion of the battery container main body having the drawn housing portion.
  • the covering resin on the surface facing the battery container body and the lid member be configured so that the same type of resin such as polypropylene resins or polyester resins face each other.
  • the above-described sealing method is an example and is not limited thereto.
  • a known adhesive may be used.
  • the battery case obtained in the present embodiment is formed using the battery case metal plate 10 of the present embodiment, the adhesion between the nickel-plated metal plate or the chromium-plated metal plate and the resin is obtained. Therefore, it can be suitably used as a battery container for various primary batteries or secondary batteries such as alkaline batteries, nickel-metal hydride batteries, nickel-cadmium batteries, and lithium ion batteries.
  • a cold-rolled plate (thickness: 80 ⁇ m) of ultra low carbon steel having the chemical composition shown below was prepared.
  • the prepared metal plate (metal foil) was annealed at 650 ° C. for 3 hours to obtain a substrate 1 having the following characteristics.
  • TS -Tensile strength
  • EL Elongation
  • Ratio of crystal grain size in plane (rolling) direction and thickness direction 1.2
  • FIG. 3 after taking a photograph of a cross section of the metal plate 10 for a battery container with a scanning electron microscope (SEM), in accordance with JIS G0551 (Annex C), The measurement was performed in each of the plane direction and the thickness direction.
  • SEM scanning electron microscope
  • Ni plating layer 2 (Formation of surface treatment layer 2) Then, the base material 1 after the annealing is subjected to electrolytic degreasing and acid pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer having a Ni plating amount of 4.5 g / m 2. 2 (Ni plating layer) was formed.
  • the conditions for forming the Ni plating layer were as follows. (Formation condition of Ni plating layer) Bath composition: nickel sulfate, nickel chloride, boric acid, pit inhibitor pH: 4.3 Bath temperature: 55 ° C Current density: 10 A / dm 2
  • thermoplastic resin 3 a stretched polyamide film having a thickness of 25 ⁇ m was prepared as the thermoplastic resin 3.
  • a urethane-based adhesive was applied to one surface of the stretched polyamide film by a gravure roll. Thereafter, the applied urethane-based adhesive was dried by heating.
  • the substrate 1 on which the surface treatment layer 2 is formed and the stretched polyamide film to which the urethane-based adhesive is applied are rewound so that the surface treatment layer 2 and the urethane-based adhesive are in contact with each other, and are pressed and dried.
  • the thermoplastic resin 3 was formed by a lamination method.
  • the stretched polyamide film was laminated only on one side of the substrate 1 on which the surface treatment layer 2 was formed. Thus, a metal plate 10 for a battery container was obtained.
  • the outer shape was cut into a size of 80 mm x 120 mm, and the depth D of each of the concave portions after molding was 5 mm using a 33 mm x 54 mm mold. And a press molding (molding pressure: 0.9 MPa) so as to be 6 mm. The press molding was performed such that the side of the stretched polyamide film was on the outer surface side of the battery container.
  • Electrode used for evaluation of content resistance 1 mol / l of lithium hexafluorophosphate (LiPF 6 ) was added to an electrolyte in which ethylene carbonate (EC), dimethyl carbonate (DMC), and diethyl carbonate (DEC) were in a weight ratio of 1: 1 to 1; 1000 ppm of water was added to lithium hexafluorophosphate.
  • EC lithium hexafluorophosphate
  • DMC dimethyl carbonate
  • DEC diethyl carbonate
  • the metal plate 10 for a battery container cut into a size of 15 mm in width ⁇ 100 mm in length was immersed in this electrolytic solution, and stored as an immersion plating material for a predetermined number of days (for example, 14 days) in an environment of 85 ° C.
  • a metal plate having a Ni plating layer formed thereon and not covered with the thermoplastic resin 3 was used as the metal plate 10 for battery containers in this evaluation.
  • the evaluation was performed in a state where the press working at the depth D was not performed. Further, sealing was performed on the side of the metal plate 10 for battery containers that was not evaluated.
  • the immersion plated material was returned to room temperature after a predetermined number of days (for example, 1, 7, or 14 days), and then visually observed.
  • Example 2 The same substrate as in Example 1 was used. The process was performed in the same manner as in Example 1 except that the plating amount of Ni as the surface treatment layer 2 (electroplating layer) was 17.8 g / m 2 .
  • Example 3 The same substrate as in Example 1 was used. The process was performed in the same manner as in Example 1 except that the plating amount of Ni as the surface treatment layer 2 (electroplating layer) was 44.5 g / m 2 .
  • Example 4 The same substrate as in Example 1 was used. After Ni plating having a plating amount of 8.9 g / m 2 was formed on the substrate, the surface treatment layer 2 (electroplating layer) was subjected to a heat treatment at 700 ° C. for 1 minute. Other than that, it carried out similarly to Example 1 mentioned above.
  • Example 5 The same substrate as in Example 1 was used.
  • the base material after the annealing was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating was performed under the following conditions.
  • an Fe—Ni alloy plating was performed on a copper plate, and the amount of Ni and Fe deposited was determined by X-ray fluorescence. Thereafter, Fe—Ni alloy plating was performed on the iron base material under the same conditions. In this example, the total of Fe and Ni was 8.9 g / m 2 .
  • the conditions for the electroplating were as follows.
  • Example 6 The same substrate as in Example 1 was used. Then, the base material was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer 2 (Cr plating) having a Cr plating amount of 0.05 g / m 2. Layer).
  • the conditions for the electroplating were as follows. (Cr plating conditions) CrO 3 : 50 g / l NaF: 1.7 g / l Bath temperature: 45 ° C Current density: 30 A / dm 2
  • the metal sheet 10 for a battery container obtained above was evaluated for moldability and content resistance in the same manner as in Example 1.
  • Example 7 The same substrate as in Example 1 was used. Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 0.36 g / m 2 , the same procedure was performed as in Example 6 described above.
  • Example 8 The same substrate as in Example 1 was used. Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 3.6 g / m 2 , the same procedure was performed as in Example 6 described above.
  • Example 9 The same substrate as in Example 1 was used. Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 7.19 g / m 2 , the same procedure as in Example 6 was performed.
  • Example 1 The same substrate as in Example 1 was used. Except that the amount of Ni plating as the surface treatment layer 2 (electroplating layer) was 0.1 g / m 2 , the procedure was the same as in Example 1 described above.
  • Example 2 The same substrate as in Example 1 was used.
  • the base material is subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating is performed under the following conditions to obtain an electroplating layer 2 (Zn plating) having a Zn plating amount of 3.6 g / m 2. Layer).
  • the conditions for the electroplating were as follows.
  • Example 4 The same substrate as in Example 1 was used. Then, the base material was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer 2 (Sn plating) having a Sn plating amount of 1.4 g / m 2. Layer).
  • the conditions for the electroplating were as follows.
  • Example 7 The same substrate as in Example 1 was used.
  • the metal plate 10 for a battery container was obtained without forming the surface treatment layer 2 (electroplating layer) on the substrate. Then, in the same manner as in Example 1, evaluation of the moldability and the evaluation of the content resistance were performed on the battery container metal plate 10 (surface-treated pear).
  • Example 10 The same substrate as in Example 1 was used. An electroplating layer 2 (Ni plating layer) having a Ni plating amount of 8.9 g / m 2 was formed on this base material in the same manner as in Example 1. Next, a polypropylene film was formed by extrusion lamination on one surface (on the Ni plating layer) on the inner surface side of the container via the molten acid-modified polypropylene with respect to the base material thus obtained. Further, a stretched polyamide film was formed on one surface on the outer surface side of the container via a urethane-based adhesive by a dry laminating method, whereby a metal plate 10 for a battery container was obtained. The lamination temperature (base temperature) at this time was 250 ° C.
  • Example 2 Evaluation of content resistance 2 As the electrolytic solution used for the content resistance, the same electrolytic solution as in Example 1 described above was used.
  • the above-described pressed metal plate 10 for a battery container was immersed in the electrolytic solution, and stored as an immersion laminate material for a predetermined number of days (for example, 14 days) in an environment of 85 ° C. After a predetermined number of days (1 day, 7 days or 14 days) has elapsed, the temperature of the immersion laminate material is returned to room temperature, and the temperature of the immersion laminate material between the TENSILON RTC-1210A substrate 1 made by ORIENTEC and the adhesive (acid-modified polypropylene) was measured for laminate strength.
  • a predetermined number of days for example, 14 days
  • the temperature of the immersion laminate material is returned to room temperature, and the temperature of the immersion laminate material between the TENSILON RTC-1210A substrate 1 made by ORIENTEC and the adhesive (acid-modified polypropylene) was measured for laminate strength.
  • T-peeling was performed under the condition of a tensile speed of 100 mm / min. Then, when the value of the lamination strength at the first day in the case where the base material was aluminum (Comparative Example 12) was set to 100%, the ratio of the lamination strength after the number of days described above was calculated for each sample, and the peel strength was calculated. The residual rate was used.
  • Example 11 The same substrate as in Example 1 was used. As in Example 10 described above, except that a Cr plating layer having a Cr plating amount of 0.1 g / m 2 was used as the surface treatment layer 2 (electroplating layer) using the same Cr plating bath as in Example 6. went.
  • ⁇ Comparative Example 9> A hard base material having the same thickness as that of Comparative Example 8 (50 ⁇ m) and not subjected to annealing was used. Using the Zn plating bath shown in Comparative Example 2 for this substrate, the Zn plating layer having a Zn plating amount of 5.0 g / m 2 was used as the surface treatment layer 2 (electroplating layer) as described above. Performed in the same manner as in Example 10. As shown in FIG. 5, the crystal grain size was determined by taking a cross-sectional photograph of the battery container metal plate 10 with a scanning electron microscope (SEM) and then conforming to JIS G0551 (Annex C). The measurement was performed in each of the plane direction and the thickness direction.
  • SEM scanning electron microscope
  • Example 12 A 40 ⁇ m-thick cold-rolled aluminum plate (O-material) was prepared as a substrate. On this base material, as in Example 10, a polypropylene film was formed by extrusion lamination on one surface on the inner surface side of the container via a molten acid-modified polypropylene, and one surface on the outer surface side of the container. Then, a stretched polyamide film was formed by a dry lamination method via a urethane-based adhesive to obtain a metal plate 10 for a battery container. In addition, the surface treatment layer 2 was not formed. With respect to the metal plate 10 for a battery container obtained above, the evaluation of the moldability and the evaluation of the content resistance were performed in the same manner as in Example 10.
  • Example 12 The same substrate as in Example 1 was used. On one surface of the substrate, a surface treatment layer 2 composed of a Ni—Fe diffusion layer (Ni plating layer) was formed in the same manner as in Example 4 described above. Next, on the other surface of the base material, a Zn plating layer and a surface treatment layer 2 formed by a chromate treatment were formed in the same manner as in Comparative Example 11 described above.
  • a surface treatment layer 2 composed of a Ni—Fe diffusion layer (Ni plating layer) was formed in the same manner as in Example 4 described above.
  • a Zn plating layer and a surface treatment layer 2 formed by a chromate treatment were formed in the same manner as in Comparative Example 11 described above.
  • the substrate obtained by performing the surface treatment in this manner is configured such that the surface composed of the Ni—Fe diffusion layer is on the inner surface side and the surface composed of the Zn plating layer and the chromate treatment is the outer surface side.
  • a polypropylene film was laminated on the inner surface and a stretched polyamide film was laminated on the outer surface, whereby a metal plate 10 for a battery container was obtained.
  • the above-described moldability and content resistance were evaluated. As a result of the evaluation described above, there was no problem in the moldability on both the inner surface and the outer surface, and the content resistance was also “ ⁇ ” until the 14th day.
  • Table 1 shows the material specifications of each sample used in the above Examples 1 to 11 and Comparative Example.
  • Table 2 shows the surface treatment specifications and the plating amounts for the samples used in Examples 1 to 9 and Comparative Examples 1 to 12, and evaluations of the content resistance 1 and the moldability.
  • Table 3 shows the specifications of the surface treatment and the respective plating amounts, and the evaluation of the physical property resistance 2 and the moldability of the samples used in Examples 10 to 11 and Comparative Examples 9 to 12.
  • Comparative Examples 12 and 11 using aluminum were also used. As a result, it was possible to obtain a result having both the content resistance and the moldability that can withstand the use of a battery can. On the other hand, it was found that Comparative Examples 10 and 11 did not have the content resistance enough to withstand use as a battery container.
  • the metal plate for a battery container of the present invention and the method for producing the same can exhibit sufficient moldability and content resistance for use in a battery container such as a lithium ion secondary battery, and can be used in a wide range of industries using batteries. Applicable.

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Abstract

[Problem] To provide: a metal plate for a cell container, in which cracking of a substrate or peeling of a resin can be suppressed even when a forming process is performed using the metal plate for application in a cell, and the metal plate for a cell container has excellent adhesion to a resin film applied thereto, and has excellent content resistance to a nonaqueous liquid electrolyte with which the container is filled; and a method for manufacturing a metal plate for a cell container. [Solution] This metal plate for a cell container comprises iron or an iron alloy and is used as a cell container, the thickness of the metal plate being 10-100 µm, and the metal plate having, at least one surface thereof, an electroplating layer containing a 0.5-50.0-g/m2 Ni plating layer and/or a 0.05-10.0-g/m2 Cr plating layer.

Description

電池容器用金属板およびこの電池容器用金属板の製造方法Metal plate for battery container and method for producing the metal plate for battery container

 本発明は、リチウムイオン二次電池などの電池容器として好適な金属板およびこの電池容器用金属板の製造方法に関する。 The present invention relates to a metal plate suitable for a battery container such as a lithium ion secondary battery and a method for producing the metal plate for a battery container.

 近年における電子機器の小型化は目覚ましく、携帯電話や携帯情報端末などの携帯型電子機器が広く普及している。かような携帯型電子機器においては、その電力源として充電が可能な二次電池が搭載されている。
 また、二次電池は、上記した携帯型電子機器に搭載されるに留まらず、ガソリンの枯渇問題や環境問題などが相俟ってハイブリッド自動車や電気自動車などの車両へも徐々に搭載されてきている。
In recent years, the miniaturization of electronic devices has been remarkable, and portable electronic devices such as mobile phones and personal digital assistants have become widespread. Such portable electronic devices are equipped with rechargeable secondary batteries as power sources.
In addition, secondary batteries are not only installed in the above-mentioned portable electronic devices, but also gradually installed in vehicles such as hybrid vehicles and electric vehicles due to the depletion of gasoline and environmental problems. I have.

 上記した携帯型電子機器あるいは車両に搭載される二次電池においては、高出力で長寿命な高性能電池としてリチウムイオン二次電池(以下、「LiB」とも称する)が着目されている。
 リチウムイオン二次電池は用途によって様々な種類があり、非水系電解液と正極活物質や負極活物質などを収容する電池容器も円筒形や角型など様々な形態をとる。このうち特許文献1では、薄板状金属板に樹脂を被覆したラミネート金属板を用いたパウチ内に電極などを収容する技術が開示されている。また、この特許文献1によれば、鉄又は鉄の合金を金属箔芯材として用いる旨が言及されている。
In the above-described secondary battery mounted on a portable electronic device or a vehicle, a lithium-ion secondary battery (hereinafter, also referred to as “LiB”) has attracted attention as a high-output, long-life high-performance battery.
There are various types of lithium ion secondary batteries depending on applications, and battery containers for accommodating a non-aqueous electrolyte, a positive electrode active material, a negative electrode active material, and the like also take various forms such as a cylindrical shape and a rectangular shape. Among these, Patent Literature 1 discloses a technique of accommodating electrodes and the like in a pouch using a laminated metal plate in which a thin metal plate is coated with a resin. According to Patent Document 1, it is mentioned that iron or an alloy of iron is used as a metal foil core material.

 また、特許文献2や特許文献3では、厚さ200μm以下の圧延金属板を用い、この圧延金属板上にNiめっきを施した後で圧延および熱処理を施すことで、この圧延金属板の表面にNiおよびFeを含む拡散合金層を形成する技術が開示されている。電解液などに対する耐食性向上を図るため圧延金属板上にポリオレフィン系樹脂が形成されることがあるが、この特許文献2によれば上記拡散合金層を用いることで圧延金属板とポリオレフィン系樹脂との密着性を向上させる旨が言及されている。 Further, in Patent Documents 2 and 3, a rolled metal plate having a thickness of 200 μm or less is used, Ni is plated on the rolled metal plate, and then rolling and heat treatment are performed. A technique for forming a diffusion alloy layer containing Ni and Fe is disclosed. A polyolefin-based resin may be formed on a rolled metal plate in order to improve corrosion resistance against an electrolytic solution or the like. According to Patent Document 2, the use of the diffusion alloy layer allows the rolled metal plate and the polyolefin-based resin to be formed. It is mentioned that the adhesiveness is improved.

特開2001-202932号公報JP 2001-202932 A 国際公開第2016/013572号International Publication No. WO 2016/013572 国際公開第2016/013575号International Publication No. WO 2016/013575

 上記した車両や電子機器に搭載可能な二次電池は、高出力であることに加えて高容量であることも要求されている。ここで、単純に容量を増加させるだけでよい場合には、比較的大きな容器に相応の電極活物質を収容すれば事足りるかもしれない。しかしながら特に車両に搭載される二次電池においては、電池自体の重量増は燃費の悪化に即刻でつながるため、高容量を実現するためであっても重量の増加は極力抑制せねばならない。 二 In addition to high output, secondary batteries that can be mounted on the above-mentioned vehicles and electronic devices are required to have high capacity. Here, if it is sufficient to simply increase the capacity, it may be sufficient to store the corresponding electrode active material in a relatively large container. However, especially in a secondary battery mounted on a vehicle, an increase in the weight of the battery itself immediately leads to a deterioration in fuel efficiency. Therefore, even in order to realize a high capacity, an increase in the weight must be suppressed as much as possible.

 可能な限り重量増を避けつつ高容量を実現する手法として、より厳しい条件下における成形加工を行って、電池容器の内容量を増加させることが想定される。しかしながら、上記した特許文献1乃至3を含む従来の技術では、かような成形加工に適しているとは言えず改善の余地は大きい。
 さらに例えば携帯電話では既に一部で流通しているが、内蔵バッテリーとして利用されるパウチ型の二次電池では特に耐食性が問題となる。すなわち、かようなパウチ型の二次電池では電解液と接触する内面側はフィルムに被覆されているため容器の基材側(金属面)が電解液と接することは想定されていない。しかしながら高容量化などの要請から容積を最大化するため厳しい加工をせざるを得ない場合も想定できる。すると、このような難加工によって上記内面側のフィルムに損傷が発生した場合や、そもそもフィルム自体にピンホールなどの欠陥があった場合には、基材側が電解液と接触してしまう可能性が生じることになる。
 以上のごとき状況を鑑みれば、基材側に形成される表面処理層(めっき層)には厳しい加工に耐え得る特性だけに留まらず耐内容物性とフィルムとの密着性がさらに希求される。
 このように電池容器用としての金属板においては、優れた加工性(成形性)、フィルムとの密着性およびリチウム塩を有機溶媒に溶解した有機電解液などの非水電解液に対する耐内容物性を向上させることは、商品競争力の向上を得る上で非常に重要となる。
 本発明は上記した課題を一例として解決することを目的としており、例えば電池用途として金属板を用いて成形加工を行う場合でも基材の割れや樹脂の剥離を抑制可能であって、且つ被覆される樹脂フィルムとの密着性に優れ、さらに容器内部に充填される非水電解液に対する耐内容物性に優れた電池容器用金属板およびこの電池容器用金属板の製造方法を提供することを目的とする。
As a method of realizing high capacity while avoiding an increase in weight as much as possible, it is assumed that molding processing is performed under more severe conditions to increase the internal capacity of the battery container. However, the conventional techniques including Patent Documents 1 to 3 described above are not suitable for such a forming process, and there is much room for improvement.
Further, for example, a part of a mobile phone is already distributed, but a pouch-type secondary battery used as a built-in battery has a particular problem of corrosion resistance. That is, in such a pouch-type secondary battery, since the inner surface side in contact with the electrolytic solution is covered with the film, it is not assumed that the substrate side (metal surface) of the container is in contact with the electrolytic solution. However, it may be conceivable that severe processing must be performed in order to maximize the volume due to a demand for higher capacity. Then, if the film on the inner surface side is damaged due to such difficult processing, or if the film itself has a defect such as a pinhole in the first place, there is a possibility that the base material side comes into contact with the electrolyte. Will happen.
In view of the above situation, the surface treatment layer (plating layer) formed on the base material side is required to have not only properties that can withstand severe processing but also content resistance and adhesion to the film.
As described above, a metal plate for a battery container has excellent workability (formability), adhesion to a film, and content resistance to a non-aqueous electrolyte such as an organic electrolyte obtained by dissolving a lithium salt in an organic solvent. Improving is very important for gaining competitiveness.
An object of the present invention is to solve the above-described problem as an example.For example, even when performing a forming process using a metal plate for battery use, it is possible to suppress cracking of the base material and peeling of the resin, and the coating is performed. The object of the present invention is to provide a metal plate for a battery container, which has excellent adhesion to a resin film, and has excellent content resistance to a nonaqueous electrolytic solution filled in the container, and a method for producing the metal plate for a battery container. I do.

 上記した課題を解決するため、本発明の一実施形態における電池容器用金属板は、(1)電池容器として用いられる電池容器用金属板であって、鉄又は鉄の合金からなり、厚みが10~100μmである基材と、前記基材の少なくとも片方の面上に形成される、0.5~50.0g/mのNiめっき層および0.05~10.0g/mのCrめっき層の少なくとも1つを含有する電気めっき層と、を有することを特徴とする。 In order to solve the above-described problems, a metal plate for a battery container according to an embodiment of the present invention is (1) a metal plate for a battery container used as a battery container, which is made of iron or an alloy of iron and has a thickness of 10 mm. a substrate which is ~ 100 [mu] m, at least formed on one surface, 0.5 ~ 50.0g / m 2 of Ni plating layer and 0.05 Cr plating ~ 10.0 g / m 2 of the substrate And an electroplating layer containing at least one of the layers.

 なお上記した(1)に記載の電池容器用金属板においては、(2)前記電気Crめっき層は、Cr水和酸化物の割合よりも金属Crの割合が大であることが好ましい。 (2) In the metal plate for a battery container according to the above (1), it is preferable that (2) the electrochromic plating layer has a higher proportion of metallic Cr than a proportion of hydrated Cr oxide.

 また上記した(1)又は(2)に記載の電池容器用金属板においては、(3)前記電気Niめっき層は、Niのみで構成されるNiめっき層、Feが拡散したFe-Ni拡散層、及びFeとNiとが共に電析したFe-Ni合金めっき層の中から選択される1つを含むことが好ましい。 Further, in the metal plate for a battery container according to the above (1) or (2), (3) the electric Ni plating layer is a Ni plating layer composed of only Ni, or a Fe—Ni diffusion layer in which Fe is diffused. , And one selected from Fe-Ni alloy plating layers in which both Fe and Ni are electrodeposited.

 また上記した(1)~(3)のいずれかに記載の電池容器用金属板においては、(4)前記基材のうち前記電池容器の内面側となる面は、ポリオレフィン系樹脂で被覆されていることが好ましい。 Further, in the metal plate for a battery container according to any one of the above (1) to (3), (4) a surface of the base material which is an inner surface side of the battery container is coated with a polyolefin-based resin. Is preferred.

 また上記した(4)に記載の電池容器用金属板においては、(5)前記ポリオレフィン系樹脂はポリプロピレン樹脂であって、前記基材と前記ポリプロピレン樹脂との間には酸変性ポリオレフィン層が介在することが好ましい。 In the metal plate for a battery container according to the above (4), (5) the polyolefin-based resin is a polypropylene resin, and an acid-modified polyolefin layer is interposed between the base material and the polypropylene resin. Is preferred.

 また上記した(1)~(5)のいずれかに記載の電池容器用金属板においては、(6)前記基材のうち前記電池容器の外面側となる面は、ポリエステル樹脂、ポリアミド樹脂、ポリオレフィン樹脂のいずれかで被覆されていることが好ましい。 (6) In the metal plate for a battery container according to any one of the above (1) to (5), (6) a surface of the base material which is an outer surface side of the battery container may be a polyester resin, a polyamide resin, or a polyolefin. Preferably, it is coated with one of the resins.

 また上記した(1)~(6)のいずれかに記載の電池容器用金属板においては、(7)前記基材の引張強度が260~700MPaであり、前記基材の伸びが5~55%であることが好ましい。 (7) In the metal plate for a battery container according to any one of the above (1) to (6), (7) the tensile strength of the base material is 260 to 700 MPa, and the elongation of the base material is 5 to 55%. It is preferred that

 また上記した(1)~(7)のいずれかに記載の電池容器用金属板においては、(8)前記基材の平面方向と厚み方向における結晶粒径の比が0.8~8であることが好ましい。 In the metal plate for a battery container according to any one of the above (1) to (7), (8) the ratio of the crystal grain size in the plane direction and the thickness direction of the base material is 0.8 to 8. Is preferred.

 また上記した(1)~(8)のいずれかに記載の電池容器用金属板においては、(9)前記基材のうち前記電池容器の内面側となる面には、前記Niめっき層および前記Crめっき層の少なくとも1つを含有する電気めっき層が形成されているとともに、前記基材のうち前記電池容器の外面側となる面には、3~30g/mのZnめっき層又はZn合金めっき層を含有する電気めっき層が形成されていることが好ましい。 In the metal plate for a battery container according to any one of the above (1) to (8), (9) the Ni plating layer and the Ni plating layer An electroplating layer containing at least one of a Cr plating layer is formed, and a surface of the substrate on the outer surface side of the battery container is a Zn plating layer or a Zn alloy of 3 to 30 g / m 2. It is preferable that an electroplating layer containing a plating layer is formed.

 さらに上記した課題を解決するため、本発明の一実施形態における電池容器用金属板の製造方法は、鉄又は鉄の合金の基材からなる電池容器用金属板の製造方法であって、前記基材を冷間圧延してその厚みを10~100μmとする工程と、前記基材の少なくとも片方の面上に、0.5~50.0g/mのNiめっき層および0.05~10.0g/mのCrめっき層の少なくとも1つを含有する電気めっき層を形成する工程と、を有することを特徴とする。 In order to further solve the above-described problems, a method for manufacturing a metal plate for a battery container according to an embodiment of the present invention is a method for manufacturing a metal plate for a battery container including a base material of iron or an alloy of iron, Cold rolling the material to a thickness of 10 to 100 μm; and forming a Ni plating layer of 0.5 to 50.0 g / m 2 on at least one surface of the base material and a 0.05 to 10. forming an electroplated layer containing at least one of Cr plating layer 0 g / m 2, and having a.

 本発明によれば、電池用途としての厳しい成形加工にも耐えることができ且つ被覆される樹脂フィルムとの密着性に優れ、さらに容器内部に充填される非水電解液に対する耐内容物性に優れた電池容器用金属板を実現することができる。 ADVANTAGE OF THE INVENTION According to this invention, it can withstand severe shaping | molding processing as a battery use, is excellent in the adhesiveness with the resin film to be coat | covered, and also excellent in the content resistance with respect to the non-aqueous electrolyte solution filled inside a container. A metal plate for a battery container can be realized.

実施形態にかかる電池容器用金属板10を示す模式図である。It is a schematic diagram which shows the metal plate 10 for battery containers concerning embodiment. 実施形態にかかる電池容器用金属板10の製造方法を示すフローチャートである。It is a flowchart which shows the manufacturing method of the metal plate 10 for battery containers concerning embodiment. 顕微鏡で撮影した基材1における断面写真(その1)である。It is the cross section photograph (the 1) in the base material 1 image | photographed with the microscope. 実施形態にかかる電池容器用金属板10を用いて成形される電池容器の概要を示す図である。It is a figure which shows the outline | summary of the battery container shape | molded using the metal plate 10 for battery containers concerning embodiment. 顕微鏡で撮影した基材1における断面写真(その2)である。It is the cross section photograph (the 2) in the base material 1 image | photographed with the microscope.

 以下、図1を用いて本実施形態の電池容器用金属板10について説明する。なお図1においては、便宜上、電池容器用金属板10の厚み方向をZ方向とし、さらに電池容器用金属板10の圧延方向をX方向として説明する。しかしながらこれら方向の定義付けは本発明の権利範囲を減縮するものではない。 Hereinafter, the metal plate 10 for a battery container of the present embodiment will be described with reference to FIG. In FIG. 1, for convenience, the thickness direction of the battery container metal plate 10 will be referred to as the Z direction, and the rolling direction of the battery container metal plate 10 will be referred to as the X direction. However, the definition of these directions does not reduce the scope of the present invention.

<電池容器用金属板>
 本実施形態に係る電池容器用金属板10は、鉄又は鉄の合金からなる基材1上に、表面処理層2(電気めっき層2)を有する。
 基材1において、鉄の合金としては、電池容器の基材として適用可能な種々の鋼板などが例示でき、例えば炭素鋼として低炭素アルミキルド鋼(炭素量0.01~0.15重量%)、炭素量が0.003重量%以下の極低炭素鋼、または、極低炭素鋼にさらにTiやNbを添加してなる非時効性極低炭素鋼なども含むものとする。
<Metal plate for battery container>
The metal plate 10 for a battery container according to the present embodiment has a surface treatment layer 2 (electroplating layer 2) on a substrate 1 made of iron or an alloy of iron.
In the base material 1, examples of the iron alloy include various steel plates applicable as a base material of a battery container. For example, low carbon aluminum killed steel (carbon content of 0.01 to 0.15% by weight) as carbon steel, Ultra-low carbon steel having a carbon content of 0.003% by weight or less or non-aging ultra-low carbon steel obtained by further adding Ti or Nb to ultra-low carbon steel is also included.

 また、本実施形態に係る基材1の厚さは、10~100μmであることが好ましく、より好ましくは15~60μmである。厚みが10μmより小さいと、冷間圧延工程においてピンホールが発生する、あるいは板厚勾差が不安定になるなど品質が不安定となりやすい。また、成型工程において割れが発生し、本願の目的とする効果が得られないおそれがある。一方で厚みが100μmを超えると、軽量化の効果が得られないからである。
 なお後述するとおり、成形加工中の基材1の割れや基材1からの樹脂フィルムの剥離を抑制する観点からは、基材1としては極低炭素鋼が望ましく、その厚みとしては20~80μm、さらに30~60μmであることがより好適である。
Further, the thickness of the base material 1 according to the present embodiment is preferably 10 to 100 μm, more preferably 15 to 60 μm. When the thickness is less than 10 μm, the quality tends to be unstable, such as generation of pinholes in the cold rolling step or unstable thickness difference. In addition, cracks may occur in the molding process, and the effects intended by the present application may not be obtained. On the other hand, if the thickness exceeds 100 μm, the effect of weight reduction cannot be obtained.
As described later, from the viewpoint of suppressing cracking of the base material 1 during the forming process and peeling of the resin film from the base material 1, the base material 1 is desirably ultra-low carbon steel, and has a thickness of 20 to 80 μm. And more preferably 30 to 60 μm.

 ここで、基材1が鉄の合金である場合における成分組成の一例を次に示す。 
 (C:0.0001~0.1重量%)
 Cは、基材1の強度を高める元素である。Cの含有量が過剰であると強度が上昇し過ぎて圧延性が低下することから、Cの含有量の上限値を0.1重量%とする。一方でCの含有量の下限値は特に制限はないが、コストを考慮してCの含有量の下限値は0.0001重量%とする。なお、Cの含有量は、より好ましくは0.0005~0.03重量%、さらに好ましくは0.001~0.01重量%である。 
Here, an example of the component composition when the base material 1 is an iron alloy is shown below.
(C: 0.0001 to 0.1% by weight)
C is an element that increases the strength of the substrate 1. If the content of C is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the content of C is set to 0.1% by weight. On the other hand, the lower limit of the C content is not particularly limited, but the lower limit of the C content is 0.0001% by weight in consideration of cost. The content of C is more preferably 0.0005 to 0.03% by weight, and still more preferably 0.001 to 0.01% by weight.

 (Si:0.001~0.5重量%)
 Siは、基材1の強度を高める元素である。Siの含有量が過剰であると強度が上昇し過ぎて圧延性が低下することから、Siの含有量の上限値を0.5重量%とする。一方でSiの含有量の下限値は特に制限はないが、コストを考慮してSiの含有量の下限値は0.001重量%とする。なお、Siの含有量は、より好ましくは0.001~0.02重量%である。
(Si: 0.001 to 0.5% by weight)
Si is an element that increases the strength of the substrate 1. If the Si content is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the Si content is set to 0.5% by weight. On the other hand, the lower limit of the Si content is not particularly limited, but the lower limit of the Si content is 0.001% by weight in consideration of cost. The content of Si is more preferably 0.001 to 0.02% by weight.

 (Mn:0.01~1.0重量%)
 Mnは、基材1の強度を高める元素である。Mnの含有量が過剰であると強度が上昇し過ぎて圧延性が低下することから、Mnの含有量の上限値を1.0重量%とする。一方でMnの含有量の下限値は特に制限はないが、コストを考慮してMnの含有量の下限値は0.01重量%とする。なお、Mnの含有量は、より好ましくは0.01~0.5%重量%である。
(Mn: 0.01 to 1.0% by weight)
Mn is an element that increases the strength of the substrate 1. If the content of Mn is excessive, the strength is excessively increased and the rollability decreases, so the upper limit of the content of Mn is set to 1.0% by weight. On the other hand, the lower limit of the Mn content is not particularly limited, but the lower limit of the Mn content is set to 0.01% by weight in consideration of cost. The Mn content is more preferably 0.01 to 0.5% by weight.

 (P:0.001~0.05重量%)
 Pは、基材1の強度を高める元素である。Pの含有量が過剰になると強度が上昇し過ぎて圧延性が低下することから、Pの含有量の上限値を0.05重量%とする。一方、Pの含有量の下限値は特に制限はないが、コストを考慮してPの含有量の下限値は0.001重量%とする。なお、Pの含有量は、より好ましくは0.001~0.02重量%である。 
(P: 0.001 to 0.05% by weight)
P is an element that increases the strength of the substrate 1. If the content of P is excessive, the strength is excessively increased and the rollability is reduced. Therefore, the upper limit of the content of P is set to 0.05% by weight. On the other hand, the lower limit of the P content is not particularly limited, but the lower limit of the P content is 0.001% by weight in consideration of cost. The P content is more preferably 0.001 to 0.02% by weight.

 (S:0.0001~0.02重量%)
 Sは、基材1の耐腐食性を低下させる元素である。そのため、Sの含有量は少ないほど好ましい。特に、Sの含有量が0.02重量%を超えると耐腐食性の低下が顕著となることから、Sの含有量の上限値を0.02重量%とする。一方でSの含有量の下限値は特に制限はないが、コストを考慮してSの含有量の下限値は0.0001重量%とする。なお、Sの含有量は、より好ましくは0.001~0.01重量%である。 
(S: 0.0001 to 0.02% by weight)
S is an element that lowers the corrosion resistance of the substrate 1. Therefore, the smaller the S content, the better. In particular, when the content of S exceeds 0.02% by weight, the corrosion resistance is significantly reduced, so the upper limit of the content of S is set to 0.02% by weight. On the other hand, the lower limit of the S content is not particularly limited, but the lower limit of the S content is set to 0.0001% by weight in consideration of cost. The S content is more preferably 0.001 to 0.01% by weight.

 (Al:0.0005~0.20重量%)
 Alは、例えば基材1の脱酸元素として添加される。脱酸による効果を得るためには、Alの含有量を0.0005重量%以上とすることが好ましい。しかしながら、Alの含有量が過剰になると圧延性が低下することから、Alの含有量の上限値を0.20重量%とする。一方で、Alの含有量の下限値は特に制限はないが、コストを考慮してAlの含有量の下限値は0.0005重量%とする。なお、Alの含有量は、より好ましくは0.001~0.10%である。 
(Al: 0.0005 to 0.20% by weight)
Al is added, for example, as a deoxidizing element for the substrate 1. In order to obtain the effect of deoxidation, the Al content is preferably set to 0.0005% by weight or more. However, if the Al content is excessive, the rollability decreases, so the upper limit of the Al content is set to 0.20% by weight. On the other hand, the lower limit of the Al content is not particularly limited, but the lower limit of the Al content is 0.0005% by weight in consideration of cost. The content of Al is more preferably 0.001 to 0.10%.

 (N:0.0001~0.0040重量%)
 Nは、基材1の加工性を低下させる元素である。そのため、Nの含有量は少ないほど好ましい。特に、Nの含有量が0.0040重量%を超えると加工性の低下が顕著となることから、Nの含有量の上限値を0.0040重量%とする。一方でNの含有量の下限値は特に制限はないが、コストを考慮してNの含有量の下限値は0.0001重量%とする。なお、Nの含有量は、より好ましくは0.001~0.0040重量%である。
(N: 0.0001 to 0.0040% by weight)
N is an element that lowers the workability of the substrate 1. Therefore, the smaller the content of N, the better. In particular, when the content of N exceeds 0.0040% by weight, the workability is significantly reduced. Therefore, the upper limit of the content of N is set to 0.0040% by weight. On the other hand, the lower limit of the N content is not particularly limited, but the lower limit of the N content is 0.0001% by weight in consideration of cost. The content of N is more preferably 0.001 to 0.0040% by weight.

(残部:Fe及び不可避的不純物)
 基材1の残部のうち主要な元素はFeであり、その他は製造時に不可避的に混入してしまう不純物である。 
(Remainder: Fe and inevitable impurities)
The main element in the remainder of the base material 1 is Fe, and the other elements are impurities which are inevitably mixed during the production.

 その他、付加成分として、Ti、Nb、B、Cu、Ni、Sn、及びCrなどが含有されていてもよい。特にTi及びNbは、基材1中のC及びNを炭化物及び窒化物として固定して、基材1の加工性を向上させる効果を有するので、Ti:0.01~0.8重量%、Nb:0.005~0.05重量%の範囲で1種または2種を含有させてもよい。また、本実施形態に係る基材1はCrが10.5%未満の鋼板がより好ましい。 In addition, Ti, Nb, B, Cu, Ni, Sn, Cr and the like may be contained as additional components. In particular, Ti and Nb have the effect of fixing C and N in the base material 1 as carbides and nitrides and improving the workability of the base material 1, so that Ti: 0.01 to 0.8% by weight, Nb: One or two kinds may be contained in the range of 0.005 to 0.05% by weight. Further, the base material 1 according to the present embodiment is more preferably a steel sheet having less than 10.5% of Cr.

 なお本実施形態に係る基材1は、冷間圧延された後で焼鈍されることで、以下の特性の少なくともいずれか1つを備えていることが好ましい。なお、本実施形態の焼鈍に必要な温度と時間は、450℃~650℃(より好ましくは500~600℃)で行う場合は2~9時間、さらに好ましくは2~6時間である。また、700~800℃で焼鈍を行う場合、その所要時間は20~120秒である。 Note that the base material 1 according to the present embodiment preferably has at least one of the following characteristics by being annealed after being cold-rolled. The temperature and time required for annealing in the present embodiment are 2 to 9 hours, more preferably 2 to 6 hours when the annealing is performed at 450 ° C. to 650 ° C. (more preferably 500 to 600 ° C.). When annealing at 700 to 800 ° C., the required time is 20 to 120 seconds.

(引張強度)
 本実施形態に係る基材1の引張強度は、260~700MPaであることが好ましい。引張強度が260MPaより小さいと、電池容器として用いた際に外部からの力で変形してしまうことにより割れ・孔が発生し、これにより電解液の漏れなどが発生してしまう問題がある。また、引張強度が700MPaを超えると加工性が乏しくなってしまうためである。なお、基材1の引張強度は、より好ましくは、270~650MPaである。より加工性を必要とする場合には、更に好ましくは280~450MPaである。
 なお基材1の引張強度は、JIS規格のZ2241に記載された「金属材料引張試験方法」に準じて行った。
(Tensile strength)
The tensile strength of the substrate 1 according to the present embodiment is preferably from 260 to 700 MPa. If the tensile strength is less than 260 MPa, there is a problem in that when used as a battery container, it is deformed by an external force, thereby generating cracks and holes, thereby causing leakage of the electrolyte. Further, when the tensile strength exceeds 700 MPa, the workability becomes poor. The tensile strength of the substrate 1 is more preferably 270 to 650 MPa. When more workability is required, it is more preferably 280 to 450 MPa.
The tensile strength of the substrate 1 was measured according to the “metallic material tensile test method” described in JIS standard Z2241.

(伸び)
 本実施形態に係る基材1の伸びは、5~55%であることが好ましい。基材1の伸びが5%未満だと角(隅)部において加工性が乏しくなり、加工の際に割れが生じるおそれがあるためである。また、伸びが55%を超えるとこのような特性を出すための焼鈍条件として高い温度・長い時間が必要となるため、生産性が悪くなるためである。なお、基材1の伸びは、より好ましくは15~55%であり、さらに好ましくは20~50%である。
 なお基材1の伸びは、JIS規格のZ2241に記載された「金属材料引張試験方法」の「20:破断伸び(%)Aの測定の式(7)」に準じて行った。
 なお後述するとおり、成形加工中の基材1の割れや基材1からの樹脂フィルムの剥離を抑制する観点からは、基材1の伸びは20%以上が好ましく、さらには30%以上であることがなお望ましい。
(Elongation)
The elongation of the substrate 1 according to the present embodiment is preferably 5 to 55%. If the elongation of the base material 1 is less than 5%, workability is poor at corners (corners), and cracks may occur during processing. On the other hand, if the elongation exceeds 55%, a high temperature and a long time are required as annealing conditions for obtaining such characteristics, so that productivity is deteriorated. The elongation of the substrate 1 is more preferably 15 to 55%, and further preferably 20 to 50%.
In addition, the elongation of the base material 1 was performed according to "Equation (7) of measurement of elongation at break (%) A" of "metallic material tensile test method" described in JIS standard Z2241.
As described later, the elongation of the base material 1 is preferably 20% or more, and more preferably 30% or more, from the viewpoint of suppressing cracking of the base material 1 during molding and peeling of the resin film from the base material 1. It is still desirable.

(結晶粒径の比)
 本実施形態に係る基材1の平面方向(圧延方向)と厚み方向における結晶粒径の比(平面方向/厚み方向)は、0.8~8であることが好ましい。なお本実施形態の「結晶粒径」は、単位面積(例えば1μm×1μm)当たりに存在する結晶粒径の平均値である。この平均結晶粒径を測定する方法に特に制限はないが、例えば走査型電子顕微鏡(SEM)で金属板の断面写真の撮影を行った上でJIS G0551(附属書BまたはC)に準拠して測定することができる。平面方向(圧延方向)と厚み方向における比を求めるには、平面方向に沿った試験線と厚み方向に沿った試験線のそれぞれに基づいて結晶粒径を求め、その比を計算する。なお、測定対象となる複数の粒子それぞれにおいて、圧延方向における最長の長さ値と、厚み方向における最長の長さ値とを対比することで上述した結晶粒径の比を算出してもよい。
 基材1の上記した結晶粒径の比が0.8未満となるようなものは一般的な製造方法において困難である。また、上記した結晶粒径の比が8を超えると加工の際に割れが生じやすい。なお、基材1の上記した結晶粒径の比は、より好ましくは0.8~5である。より加工性が求められる場合、基材1の上記した結晶粒径の比は、更に好適には0.8~4である。
(Ratio of crystal grain size)
The ratio of the crystal grain size in the plane direction (rolling direction) and the thickness direction (plane direction / thickness direction) of the substrate 1 according to this embodiment is preferably 0.8 to 8. The “crystal grain size” in the present embodiment is an average value of the crystal grain size existing per unit area (for example, 1 μm × 1 μm). There is no particular limitation on the method of measuring the average crystal grain size. For example, a cross-sectional photograph of a metal plate is taken with a scanning electron microscope (SEM) and then, in accordance with JIS G0551 (Annex B or C). Can be measured. To determine the ratio between the plane direction (rolling direction) and the thickness direction, the crystal grain size is determined based on each of the test line along the plane direction and the test line along the thickness direction, and the ratio is calculated. The ratio of the crystal grain size described above may be calculated by comparing the longest length value in the rolling direction and the longest length value in the thickness direction in each of the plurality of particles to be measured.
It is difficult for the substrate 1 to have a crystal grain ratio of less than 0.8 in a general manufacturing method. On the other hand, when the above-mentioned ratio of crystal grain diameters exceeds 8, cracks are likely to occur during processing. The ratio of the crystal grain diameter of the substrate 1 is more preferably 0.8 to 5. When more workability is required, the ratio of the crystal grain size of the substrate 1 is more preferably 0.8 to 4.

<表面処理層>
 本実施形態に係る基材1上の少なくとも電池容器の内面側となる面には、電気めっきによる表面処理層2(電気めっき層とも称する)が形成される。なお、基材1の電池容器の外面側となる面についても、酸化防止と製造の容易性を確立するなどの観点から、上記した内面側となる面と同じである又は少なくとも一層が同じである表面処理層2が形成されていてもよい。この表面処理層2としては、例えば電解液に浸漬した際の樹脂フィルムとの密着性向上のため、および、上記樹脂フィルムに欠損が生じた場合における電解液への耐食性確保のため、電気めっきによって形成されるCrめっき層、並びにNiめっき層及びFe-Ni合金めっき層に例示されるNiの合金めっきが挙げられる。また、これらのめっき層を複数有していてもよく、例えば基材1上にNiめっき層を形成した後、Crめっき層を形成してもよい。
 なお本実施形態の表面処理層は、例えば基材1が冷間圧延後に焼鈍された後に形成してもよいし、基材1が冷間圧延された後であって焼鈍される前に形成することも可能である。このうち焼鈍される前にNiめっきを施した際には、熱処理によってFe-Ni拡散層が形成されていてもよい。このとき、Niめっき層と基材1との間にFe-Ni拡散層が形成されていてもよく、または、基材1の鉄がNiめっき層の全体に拡散し、基材1の上に直接Fe-Ni拡散層が形成されていてもよい。
<Surface treatment layer>
A surface treatment layer 2 (also referred to as an electroplating layer) by electroplating is formed on at least a surface on the inner surface side of the battery container on the base material 1 according to the present embodiment. In addition, the surface of the substrate 1 on the outer surface side of the battery container is the same as the above-mentioned inner surface or at least one layer from the viewpoint of establishing oxidation prevention and ease of manufacture. The surface treatment layer 2 may be formed. The surface treatment layer 2 is formed by electroplating, for example, to improve adhesion to a resin film when immersed in an electrolytic solution and to ensure corrosion resistance to the electrolytic solution when the resin film has a defect. Examples thereof include a Cr plating layer to be formed, and a Ni alloy plating exemplified by a Ni plating layer and an Fe—Ni alloy plating layer. Further, a plurality of these plating layers may be provided. For example, a Ni plating layer may be formed on the base material 1 and then a Cr plating layer may be formed.
In addition, the surface treatment layer of this embodiment may be formed, for example, after the base material 1 is annealed after cold rolling, or formed after the base material 1 is cold-rolled and before annealing. It is also possible. When Ni plating is performed before annealing, the Fe—Ni diffusion layer may be formed by heat treatment. At this time, an Fe—Ni diffusion layer may be formed between the Ni plating layer and the substrate 1, or the iron of the substrate 1 diffuses throughout the Ni plating layer, and An Fe—Ni diffusion layer may be directly formed.

 また、図1においては基材1の両面に表面処理層2が形成されているが、少なくとも電池容器の内面側となる面に表面処理層2が形成される態様でもよい。
 または、基材1の両面でそれぞれ異なる種類の表面処理層2(電気めっき層)が形成されていてもよい。例えば基材1のうち電池容器の内面側となる面には、Niめっき層およびCrめっき層の少なくとも1つを含有する電気めっき層(第1電気めっき層)が形成されるとともに、電池容器の外面側となる面には異なる耐食メカニズム(犠牲防食層として)のZnめっき層又はZn合金層(例えば、Zn-Ni、Zn-Co、Zn-Co-Mo、Zn-Fe、Zn-Snなど)を含有する電気めっき層(第2電気めっき層)が形成されてもよい。この場合、犠牲防食層としてのZnめっき層又はZn合金めっき層を含有する電気めっき層は、例えばZnが3~30g/mのめっき量であることが好ましく、さらに5~25g/mのめっき量であることが尚好ましい。Znめっきは電解液に溶解するので、常に接触する内面側としては使用できないが、電池容器の外面側に使用することで、電解液が少量付着した際の犠牲防食に有効である。特に、端面に電解液が少量付着した際には、上記のごとく片面(外面側)がZnめっきである場合には、端面においてZnが優先的に溶けることにより、基材である鉄の腐食を抑制することができ、以って電解液の漏出を防ぐことができるので効果的である。
Although the surface treatment layers 2 are formed on both surfaces of the substrate 1 in FIG. 1, the surface treatment layer 2 may be formed on at least the inner surface of the battery container.
Alternatively, different types of surface treatment layers 2 (electroplating layers) may be formed on both surfaces of the substrate 1. For example, an electroplating layer (first electroplating layer) containing at least one of a Ni plating layer and a Cr plating layer is formed on a surface of the base material 1 on the inner surface side of the battery container. A Zn plating layer or a Zn alloy layer (for example, Zn—Ni, Zn—Co, Zn—Co—Mo, Zn—Fe, Zn—Sn) having a different corrosion resistance mechanism (as a sacrificial anticorrosion layer) is formed on the outer surface. (A second electroplating layer) may be formed. In this case, the electroplating layer containing the Zn plating layer or the Zn alloy plating layer as the sacrificial anticorrosion layer preferably has a Zn plating amount of, for example, 3 to 30 g / m 2 , and more preferably 5 to 25 g / m 2 . More preferably, the amount of plating is used. Zn plating dissolves in the electrolytic solution, so it cannot be used as an inner surface that is always in contact. However, by using it on the outer surface of the battery container, it is effective for sacrificial corrosion prevention when a small amount of the electrolytic solution adheres. In particular, when a small amount of the electrolytic solution adheres to the end face, if one side (outer side) is plated with Zn as described above, Zn is preferentially dissolved at the end face, so that corrosion of the iron as the base material is prevented. This is effective because it can suppress the leakage of the electrolytic solution.

 なお、基材1上に表面処理層2としてNiめっきを施す場合には、冷間圧延した金属板を通常の方法で電解脱脂、酸洗した後、例えば一例として以下に示すNiめっき浴を用いることができる。なおNiめっき浴としてはワット浴と称される硫酸ニッケル浴が主と用いられるが、この他、スルファミン酸浴、ほうフッ化物浴、塩化物浴などを用いてもよい。
(Niめっき浴組成、条件)
 硫酸ニッケル:200~350g/l
 塩化ニッケル:20~60g/l
 ほう酸:10~50g/l
 pH:1.5~5.0
 浴温度:40~70℃
 電流密度:1~40A/dm
When Ni plating is applied as the surface treatment layer 2 on the base material 1, the cold-rolled metal plate is electrolytically degreased and pickled by a usual method, and then, for example, the following Ni plating bath is used as an example. be able to. As a Ni plating bath, a nickel sulfate bath called a Watt bath is mainly used, but a sulfamic acid bath, a borofluoride bath, a chloride bath, or the like may be used.
(Ni plating bath composition, conditions)
Nickel sulfate: 200-350g / l
Nickel chloride: 20-60 g / l
Boric acid: 10-50 g / l
pH: 1.5 to 5.0
Bath temperature: 40-70 ° C
Current density: 1 to 40 A / dm 2

 また、基材1上に形成される表面処理層2としてのNiめっきは、純粋なNiだけでなく、Ni-Co合金や、Fe-Ni合金などのようにNiを含む合金を用いて形成されたものであってもよい。換言すれば、表面処理層2は、Niのみで構成されるNiめっき層、Feが拡散したFe-Ni拡散層、及びFeとNiとが共に電析したFe-Ni合金めっき層のいずれかを含んでいてもよい。なお本明細書で「Niのみで構成される」とは、金属元素としてはNiのみを有する意味であり、めっき浴添加剤に由来する物質あるいはめっき形成過程で不回避的に混入される0.1%未満の炭素や0.05%未満の硫黄などの不純物は含有することを許容するものである。 The Ni plating as the surface treatment layer 2 formed on the substrate 1 is formed using not only pure Ni but also an alloy containing Ni such as a Ni—Co alloy or an Fe—Ni alloy. May be used. In other words, the surface treatment layer 2 is made of one of a Ni plating layer composed of only Ni, an Fe—Ni diffusion layer in which Fe is diffused, and an Fe—Ni alloy plating layer in which both Fe and Ni are electrodeposited. May be included. In the present specification, “composed of only Ni” means having only Ni as a metal element, and a substance derived from a plating bath additive or unavoidably mixed in a plating formation process. Impurities such as less than 1% carbon and less than 0.05% sulfur are allowed to be contained.

 また、本実施形態のNiめっきは、めっき量として0.5~50.0g/mのNiめっきであることが好ましい。Niめっきのめっき量が0.5g/m未満では、表面の被覆が不十分で基材の露出が極端に増え、耐内容物性が不足するという問題が生じてしまう。一方でNiめっきのめっき量が50.0g/mを超えると、めっき層の厚みが厚くなる事によって金属板10の厚みも厚くなり重量増加につながってしまう。また、めっきの処理時間やめっき量の増加は生産性の悪化や製造コストの増大を招くという問題が生じるからである。
 また、表面処理層2としてNiめっきを基材1上に形成した後、熱処理を施す場合、Fe-Ni拡散層を形成することができる。加工性向上の観点から、このFe-Ni拡散層は0.2μm以上であって3.0μm以下の厚さであることが好ましい。
Further, the Ni plating of this embodiment is preferably a Ni plating having a plating amount of 0.5 to 50.0 g / m 2 . If the plating amount of the Ni plating is less than 0.5 g / m 2 , the surface coverage is insufficient, the exposure of the base material is extremely increased, and there arises a problem that the content resistance is insufficient. On the other hand, if the plating amount of the Ni plating exceeds 50.0 g / m 2 , the thickness of the metal layer 10 increases due to an increase in the thickness of the plating layer, which leads to an increase in weight. Further, an increase in the plating processing time or the amount of plating causes a problem that productivity is lowered and manufacturing cost is increased.
Further, when heat treatment is performed after Ni plating is formed on the substrate 1 as the surface treatment layer 2, an Fe—Ni diffusion layer can be formed. From the viewpoint of improving workability, the Fe—Ni diffusion layer preferably has a thickness of 0.2 μm or more and 3.0 μm or less.

 また、基材1上に表面処理層2としてCrめっきを施す場合には、冷間圧延した金属板を通常の方法で電解脱脂、酸洗した後、例えば一例として以下に示すCrめっき浴を用いることができる。
(Crめっき浴組成、条件)
 CrO:30~200g/l
 NaF:1~10g/l
 pH:1.0以下
 浴温度:35~65℃
 電流密度:5~50A/dm
When Cr plating is performed as the surface treatment layer 2 on the base material 1, the cold-rolled metal plate is electrolytically degreased and pickled by a usual method, and then, for example, the following Cr plating bath is used as an example. be able to.
(Cr plating bath composition, conditions)
CrO 3 : 30 to 200 g / l
NaF: 1 to 10 g / l
pH: 1.0 or less Bath temperature: 35-65 ° C
Current density: 5 to 50 A / dm 2

 この場合、表面処理層2としてのCrめっきは、めっき量として0.05~10.0g/mのCrめっきであることが好ましい。Crめっきのめっき量が0.05g/m未満では、表面の被覆が不十分で基材1の露出が極端に増えてしまい、耐内容物性が不足するという問題が生じてしまう。一方でCrめっきのめっき量が10.0g/mを超えると、上記と同様に重量の増加、生産性の悪化や製造コストの増大という問題が生じるからである。 In this case, the Cr plating as the surface treatment layer 2 is preferably a Cr plating having a plating amount of 0.05 to 10.0 g / m 2 . If the plating amount of the Cr plating is less than 0.05 g / m 2 , the surface coverage is insufficient and the exposure of the base material 1 is extremely increased, resulting in a problem that the content resistance is insufficient. On the other hand, if the plating amount of the Cr plating exceeds 10.0 g / m 2 , similar problems as described above arise, such as an increase in weight, a decrease in productivity, and an increase in manufacturing cost.

 また、表面処理層2としてCrめっきを施す場合には、Cr水和酸化物(CrOx)の割合よりも金属Crの割合が大であるCrめっき層であることが更に好ましい。ここで金属CrとCr水和酸化物(CrOx)の算出方法としては、例えば以下に示す方法で実施できる。まずステップ1として、基材上に施したCrめっきの全Cr量を測定する。次いでステップ2として、このCrめっきが施された基材を高温アルカリで溶解処理することで、Cr水和酸化物を溶解させ、基材に残ったCr量を金属Cr量として測定する。最後にステップ3として、Cr水和酸化物量を計算(Cr水酸化物量=全Cr量-金属Cr量)で算出する。なお上記測定は、全て市販の蛍光X線測定器によって実施することができる。 In the case where Cr plating is performed as the surface treatment layer 2, it is more preferable that the Cr plating layer has a higher proportion of metallic Cr than that of Cr hydrated oxide (CrOx). Here, as a calculation method of metal Cr and Cr hydrated oxide (CrOx), for example, the following method can be used. First, as step 1, the total amount of Cr in the Cr plating applied to the substrate is measured. Next, as step 2, the Cr-plated substrate is subjected to a dissolution treatment with a high-temperature alkali to dissolve the hydrated Cr oxide, and the amount of Cr remaining on the substrate is measured as the amount of metallic Cr. Finally, as Step 3, the amount of Cr hydrated oxide is calculated by calculation (Cr hydroxide amount = Total Cr amount−Cr metal amount). In addition, all of the above measurements can be performed by a commercially available X-ray fluorescence meter.

<熱可塑性樹脂>
 本実施形態に係る電池容器用金属板10は、少なくとも一方の面が熱可塑性樹脂3で被覆されていてもよい。なお、本実施形態の電池容器用金属板10においては、電池容器用樹脂被覆金属板として表面処理層2上を熱可塑性樹脂で被覆していてもよい。換言すれば、電池容器用金属板10は、表面処理層2上が熱可塑性樹脂で被覆されたラミネート板として構成されていてもよく、あるいは表面処理層2が形成されるに留まる構成であってもよい。
 かような熱可塑性樹脂3の厚みは、10~100μmであり、より好ましくは10~50μmである。
 また、本実施形態の熱可塑性樹脂3としては、ポリオレフィン系樹脂、ポリエステル系樹脂又はポリアミド樹脂が例示される。そしてこのポリオレフィン系樹脂、ポリエステル系樹脂又はポリアミド樹脂は、電池容器用金属板10の両面を被覆していることが好ましい。この場合においては、電池容器用金属板10のうち一方の面(電池缶の内面側)はポリオレフィン系樹脂(特にポリプロピレン樹脂)で被覆されることが好ましい。
<Thermoplastic resin>
At least one surface of the metal plate 10 for a battery container according to the present embodiment may be covered with the thermoplastic resin 3. In the metal plate 10 for a battery container of the present embodiment, the surface treatment layer 2 may be coated with a thermoplastic resin as a resin-coated metal plate for a battery container. In other words, the battery container metal plate 10 may be configured as a laminate plate in which the surface treatment layer 2 is coated with a thermoplastic resin, or may have a configuration in which only the surface treatment layer 2 is formed. Is also good.
The thickness of such a thermoplastic resin 3 is 10 to 100 μm, and more preferably 10 to 50 μm.
In addition, as the thermoplastic resin 3 of the present embodiment, a polyolefin resin, a polyester resin, or a polyamide resin is exemplified. The polyolefin resin, polyester resin or polyamide resin preferably covers both surfaces of the battery container metal plate 10. In this case, one surface (the inner surface side of the battery can) of the metal plate 10 for a battery container is preferably covered with a polyolefin-based resin (particularly, a polypropylene resin).

 かようなポリプロピレン樹脂としては、ランダムプロピレン樹脂、ホモプロピレン樹脂、およびブロックプロピレン樹脂などの各種のポリプロピレン樹脂を単層で使用してもよいし、これらを重ね合わせて多層化して使用してもよい。
 また、本実施形態では、ポリプロピレン樹脂に公知の添加剤を添加してもよい。このような添加剤としては、例えば、低結晶性のエチレンーブテン共重合体、低結晶性のプロピレンーブテン共重合体、エチレンとブテンとプロピレンの3成分共重合体からなるターポリマー、シリカ、ゼオライト、アクリル樹脂ビーズ等のアンチブロッキング剤、脂肪酸アマイド系のスリップ剤などが例示できる。さらには、例えばスリップ剤(材料の物理的な安定性向上のため)や酸化防止剤なども上記した添加剤として添加してよい。
As such a polypropylene resin, various polypropylene resins such as a random propylene resin, a homopropylene resin, and a block propylene resin may be used in a single layer, or they may be used as a multilayer by overlapping them. .
In the present embodiment, a known additive may be added to the polypropylene resin. Examples of such additives include a low-crystalline ethylene butene copolymer, a low-crystalline propylene butene copolymer, a terpolymer composed of a three-component copolymer of ethylene, butene, and propylene, silica, zeolite, Examples thereof include anti-blocking agents such as acrylic resin beads and fatty acid amide-based slip agents. Further, for example, a slip agent (for improving the physical stability of the material) and an antioxidant may be added as the above-mentioned additives.

 一方で、電池容器用金属板10のうち他方の面(電池缶の外面側)は、ポリエステル樹脂、ポリアミド樹脂、ポリオレフィン樹脂のいずれかで被覆されていることが好ましい。このうちポリエステル樹脂としては、ポリエチレンテレフタレートで被覆することが好ましい。なおポリエステル樹脂としては、ポリエチレンテレフタレートの他に例えば、ポリブチレンテレフタレート、ポリエチレンナフタレート、ポリブチレンナフタレート等を使用することができる。また、ウレタン変性ポリエステル樹脂、アクリル変性ポリエステル樹脂、エポキシ変性ポリエステル樹脂などの変性樹脂を用いても良い。 On the other hand, the other surface (outer surface side of the battery can) of the metal plate 10 for a battery container is preferably coated with any of a polyester resin, a polyamide resin, and a polyolefin resin. Among them, the polyester resin is preferably coated with polyethylene terephthalate. As the polyester resin, in addition to polyethylene terephthalate, for example, polybutylene terephthalate, polyethylene naphthalate, polybutylene naphthalate, or the like can be used. Further, a modified resin such as a urethane-modified polyester resin, an acryl-modified polyester resin, or an epoxy-modified polyester resin may be used.

 なお、電池容器用金属板10のうち一方の面(例えば電池缶の内面側)を被覆する樹脂の厚みと、他方の面(例えば電池缶の外面側)を被覆する樹脂の厚みは、要求される耐食性・加工性により上記厚み範囲の間で適宜調整すればよく、両面の厚みは同じでも異なっていてもよい。
 また、ポリエステル樹脂を使用する場合、このポリエステル樹脂は無配向であることが好ましい。
 また、電池容器用金属板10のうち他方の面(電池缶の外面側)は、上記したポリエステル樹脂(ポリエチレンテレフタレート)に限られず、電池容器用金属板10の両面共にポリプロピレン樹脂で被覆してもよい。あるいは、電池容器用金属板10の両面共にポリエステル樹脂で被覆してもよい。
The thickness of the resin covering one surface (for example, the inner surface side of the battery can) and the thickness of the resin covering the other surface (for example, the outer surface side of the battery can) of the battery container metal plate 10 are required. The thickness may be adjusted appropriately within the above thickness range depending on the corrosion resistance and workability, and the thickness of both surfaces may be the same or different.
When a polyester resin is used, the polyester resin is preferably non-oriented.
Further, the other surface (outer surface side of the battery can) of the battery container metal plate 10 is not limited to the polyester resin (polyethylene terephthalate) described above. Good. Alternatively, both surfaces of the battery container metal plate 10 may be covered with a polyester resin.

 また、熱可塑性樹脂3は、公知の接着剤を介して電池容器用金属板10を被覆している形態であってもよい。なお公知の接着剤としては、例えば、酸変性ポリオレフィン樹脂、エポキシ樹脂、アクリル樹脂、ウレタン樹脂、シリコン樹脂、ポリイソブチレン系樹脂、フッ素樹脂、或いは水ガラス等の無機接着剤などを用いることができる。
 特に本実施形態の電池容器用金属板10では、基材1と上記した熱可塑性樹脂3との間に酸変性ポリオレフィン層を介在させることが好ましい。なおこの場合、基材1から順に、表面処理層2、酸変性ポリオレフィン層、熱可塑性樹脂3、のように形成される。このような酸変性ポリオレフィン層は、特に熱可塑性樹脂3がポリプロピレン樹脂である場合に、電池容器用金属板10における当該ポリプロピレン樹脂との密着性を向上させるために有効となる。酸変性ポリオレフィン層の具体例としては、例えば不飽和カルボン酸でグラフト変性したポリプロピレンや、プロピレンに対してアクリル酸又はメタクリル酸を共重合させた共重合体などが例示できる。さらにこれらの酸変性ポリオレフィン層に対し、さらに必要に応じてブテン成分、エチレン-プロピレン-ブテン共重合体、プロピレン-α-オレフィン共重合体等を5%以上添加してもよい。なお、酸変性ポリオレフィン層は、異常発熱の防止および溶融押出し時におけるサージングやネックイン防止の観点から、融点が145℃~165℃の酸変性ポリプロピレンが好ましい。
The thermoplastic resin 3 may be in a form in which the metal plate 10 for a battery container is covered with a known adhesive. As the known adhesive, for example, an inorganic adhesive such as an acid-modified polyolefin resin, an epoxy resin, an acrylic resin, a urethane resin, a silicone resin, a polyisobutylene-based resin, a fluororesin, or water glass can be used.
In particular, in the metal plate 10 for a battery container of the present embodiment, it is preferable to interpose an acid-modified polyolefin layer between the base material 1 and the thermoplastic resin 3 described above. In this case, the surface treatment layer 2, the acid-modified polyolefin layer, and the thermoplastic resin 3 are formed in this order from the substrate 1. Such an acid-modified polyolefin layer is effective for improving the adhesion between the metal plate 10 for a battery container and the polypropylene resin, particularly when the thermoplastic resin 3 is a polypropylene resin. Specific examples of the acid-modified polyolefin layer include, for example, polypropylene graft-modified with an unsaturated carboxylic acid, and a copolymer obtained by copolymerizing propylene with acrylic acid or methacrylic acid. Further, to these acid-modified polyolefin layers, if necessary, a butene component, an ethylene-propylene-butene copolymer, a propylene-α-olefin copolymer or the like may be added in an amount of 5% or more. The acid-modified polyolefin layer is preferably an acid-modified polypropylene having a melting point of 145 ° C. to 165 ° C. from the viewpoint of preventing abnormal heat generation and surging and neck-in during melt extrusion.

 前記熱可塑性樹脂3は、フィルムを形成した後に、表面処理層2を形成した基材1上にラミネートするものであってもよいし、加熱溶融した前記熱可塑性樹脂3を押し出し成形機の押し出し幅のスリットによってフィルム状に押し出し、表面処理層2を形成した基材1上に直接的にラミネートする押し出しラミネート法によるものであってもよい。上記フィルムを形成した後でラミネートする場合、上記フィルムの延伸の有無は特に限定されず、たとえば、無延伸フィルムであっても一軸延伸フィルムであっても二軸延伸フィルムであってもよい。 After forming the film, the thermoplastic resin 3 may be laminated on the substrate 1 on which the surface treatment layer 2 is formed, or the thermoplastic resin 3 melted by heating may be extruded by an extrusion width of an extruder. The film may be extruded into a film by the slit and directly laminated on the substrate 1 on which the surface treatment layer 2 is formed by an extrusion lamination method. When laminating after forming the film, the presence or absence of stretching of the film is not particularly limited. For example, the film may be a non-stretched film, a uniaxially stretched film, or a biaxially stretched film.

 一例として、電池容器用金属板10のうち一方の面(電池缶の内面側)と他方の面(電池缶の外面側)とで、熱可塑性樹脂3のラミネート方法を異ならせることもできる。
 例えば、基材1のうち他方の面(電池缶の外面側)については、表面処理層2の上にさらに、例えば2液硬化型のポリウレタン系接着剤を介して、延伸した熱可塑性樹脂3からなるフィルム(例えば延伸PETフィルムや延伸ポリアミドフィルム)をドライラミネートしてもよい。
 一方で、電池容器用金属板10のうち一方の面(電池缶の内面側)については、表面処理層2を形成した基材1において、該表面処理層2と熱可塑性樹脂3としてのポリプロピレンフィルムとの間に酸変性ポリプロピレンを溶融押出しして、この溶融押し出しを行った酸変性ポリプロピレンを基材1とポリプロピレンフィルムとの間でサンドイッチしてラミネート処理することができる。さらに内面側のラミネートについてはこの他、ポリプロピレンと酸変性ポリプロピレンを多層フィルム状に押出成形して表面処理層2上に直接ラミネートする方法、予めポリプロピレンと酸変性ポリプロピレンの多層フィルムを用意してこれを表面処理層2上に熱ラミネートする方法、等を採用することもできる。
As an example, the laminating method of the thermoplastic resin 3 may be different between one surface (the inner surface side of the battery can) and the other surface (the outer surface side of the battery can) of the metal plate 10 for a battery container.
For example, the other surface (the outer surface side of the battery can) of the base material 1 is further coated on the surface treatment layer 2 with the thermoplastic resin 3 stretched via, for example, a two-component curable polyurethane-based adhesive. (For example, a stretched PET film or a stretched polyamide film) may be dry-laminated.
On the other hand, with respect to one surface (the inner surface side of the battery can) of the metal plate 10 for a battery container, in the substrate 1 on which the surface treatment layer 2 is formed, a polypropylene film as the surface treatment layer 2 and the thermoplastic resin 3 The melt-extruded acid-modified polypropylene is sandwiched between the base material 1 and the polypropylene film to perform a lamination treatment. Further, for the lamination on the inner surface side, in addition to this, a method in which polypropylene and acid-modified polypropylene are extruded into a multilayer film and directly laminated on the surface treatment layer 2, a multilayer film of polypropylene and acid-modified polypropylene is prepared in advance, and A method of thermally laminating on the surface treatment layer 2 or the like can also be adopted.

<電池容器用金属板の製造方法>
 次いで、図2を参照しつつ本実施形態の電池容器用金属板10の製造方法について説明する。
 まず、鉄又は鉄の合金からなる金属板を準備し、プレス加工を行う圧延機に当該金属板を投入することによって冷間圧延を行う(ステップ1)。これにより、厚さが10~100μmの冷間圧延された基材1が形成される。この冷間圧延は必要に応じて多段階で行ってもよく、間に熱処理を行ってもよい。
<Production method of metal plate for battery container>
Next, a method for manufacturing the metal plate 10 for a battery container of the present embodiment will be described with reference to FIG.
First, a metal plate made of iron or an iron alloy is prepared, and cold rolling is performed by putting the metal plate into a rolling mill that performs press working (step 1). Thus, a cold-rolled substrate 1 having a thickness of 10 to 100 μm is formed. This cold rolling may be performed in multiple stages as necessary, or a heat treatment may be performed in between.

 次いで、得られた基材1に対して焼鈍処理を行う(ステップ2)。このとき、焼鈍処理における基材1の温度は、450℃~650℃、より好ましくは500~600℃である。また、この焼鈍処理における所要時間は、2~9時間、より好ましくは2~6時間行われる。また、700~800℃で焼鈍処理を行う場合は20~120秒で行うこともできるが、加工性向上の観点から前者の温度範囲で行うのが好ましい。 Next, an annealing treatment is performed on the obtained base material 1 (step 2). At this time, the temperature of the substrate 1 in the annealing treatment is 450 to 650 ° C, more preferably 500 to 600 ° C. The time required for this annealing treatment is 2 to 9 hours, more preferably 2 to 6 hours. When the annealing is performed at 700 to 800 ° C., the annealing can be performed in 20 to 120 seconds, but is preferably performed in the former temperature range from the viewpoint of improving workability.

 ステップ2の後、基材1に表面処理(めっき処理)を施して当該基材1の少なくとも片方の面上に、Niめっき層およびCrめっき層の少なくとも1つを含有する表面処理層2(電気めっき層)を形成する(ステップ3)。
 なお、ステップ3で形成される表面処理層2(電気めっき層)としては、例えばNiめっき層であればめっき量を0.5~50.0g/mとし、Crめっき層であればめっき量を0.05~10.0g/mであることが好適である。なお、ステップ2の焼鈍は表面処理層2を形成した後に行ってもよい。また、ステップ2の焼鈍を行った後で表面処理層2を形成した後に、例えば加工性向上を狙いとして熱処理(拡散処理)をさらに施してもよい。このときの熱処理条件としては、ステップ2で記載される焼鈍条件と同様の条件で行うことが可能である。なお、ステップ1の圧延工程をめっき処理の後に行うと、Niめっき皮膜の表面にクラックが生じて密着性、耐食性が低下する可能性があり、好ましくない。
After step 2, the substrate 1 is subjected to a surface treatment (plating treatment), and on at least one surface of the substrate 1, a surface treatment layer 2 (at least one of a Ni plating layer and a Cr plating layer) A plating layer is formed (Step 3).
The surface treatment layer 2 (electroplating layer) formed in step 3 is, for example, a plating amount of 0.5 to 50.0 g / m 2 for a Ni plating layer, and a plating amount for a Cr plating layer. Is preferably 0.05 to 10.0 g / m 2 . The annealing in Step 2 may be performed after the surface treatment layer 2 is formed. Further, after forming the surface treatment layer 2 after performing the annealing in step 2, a heat treatment (diffusion treatment) may be further performed, for example, for the purpose of improving workability. The heat treatment at this time can be performed under the same conditions as the annealing conditions described in Step 2. If the rolling process of Step 1 is performed after the plating treatment, cracks may be generated on the surface of the Ni plating film, and the adhesion and corrosion resistance may be reduced, which is not preferable.

 なお、ステップ2、3を経た後の基材1は、引張強度が260~700MPa、伸びが5~55%、且つ基材1の平面方向(圧延方向)と厚み方向における結晶粒径の比が0.8~8という特性の少なくとも1つを備えていることが好ましい。
 上記のようにステップ2、3を経た後で、電池容器用金属板10を得ることができる。
The substrate 1 after steps 2 and 3 has a tensile strength of 260 to 700 MPa, an elongation of 5 to 55%, and a ratio of the crystal grain size in the plane direction (rolling direction) of the substrate 1 to the thickness direction. It is preferable to have at least one of the characteristics of 0.8 to 8.
After the steps 2 and 3 as described above, the metal plate 10 for a battery container can be obtained.

 次にステップ4では、表面処理層2が形成された基材1に対して、上記で説明した熱可塑性樹脂3を10~50μm程度の厚みで被覆する処理(樹脂被覆処理)を行う。なお、このステップ4は、本実施形態の電池容器用金属板10の製造方法においては必須の工程ではなく、ラミネート板(電池容器用樹脂被覆金属板)として構成しない限りは適宜省略してもよい。
 ステップ4についてより具体的には、表面処理層2が形成された基材1のうち容器内面側となる一方の面にはポリプロピレン樹脂を形成するとともに、容器外面側となる一方の面にはポリエチレンテレフタレート樹脂又はポリプロピレン樹脂を形成することが例示できる。
Next, in step 4, the substrate 1 on which the surface treatment layer 2 is formed is subjected to the above-described process of coating the thermoplastic resin 3 with a thickness of about 10 to 50 μm (resin coating process). Step 4 is not an essential step in the method for manufacturing the metal plate 10 for a battery container of the present embodiment, and may be omitted as long as it is not configured as a laminate plate (a resin-coated metal plate for a battery container). .
More specifically, in step 4, a polypropylene resin is formed on one surface of the substrate 1 on which the surface treatment layer 2 is formed on the inner surface side of the container, and polyethylene is formed on one surface on the outer surface side of the container. Forming a terephthalate resin or a polypropylene resin can be exemplified.

 樹脂の形成方法としては、上述したように、表面処理層2が形成された基材1のうち容器外面側となる側はウレタン系接着剤を介してドライラミネート法を採用しつつ、容器内面側となる側には溶融した酸変性ポリプロピレンを介した押し出しラミネート法を採用できる。ラミネート法は上記に限られず、表面処理層2が形成された基材1のうちいずれの側であってもフィルムラミネートでも良いし、押し出しラミネートによる方法でも良い。なお、この熱可塑性樹脂3を被覆する際の表面処理層2が形成された基材1の温度は、例えばラミネートの態様に応じて常温~280℃、好ましくは250℃以下に調整される。上記のようにステップ4を経た後で、電池容器用樹脂被覆金属板を得ることができる。なおドライラミネート法を採用した場合には、例えば30~100℃の温度環境下で1~7日間の期間でドライラミネート後のエージングを行うことが好ましい。 As described above, the method of forming the resin is such that, as described above, the side of the substrate 1 on which the surface treatment layer 2 is formed on the container outer surface side employs a dry lamination method via a urethane-based adhesive, The extrusion lamination method via a molten acid-modified polypropylene can be adopted on the side to be formed. The lamination method is not limited to the above, and any side of the substrate 1 on which the surface treatment layer 2 is formed may be a film lamination or an extrusion lamination. The temperature of the substrate 1 on which the surface treatment layer 2 is formed when the thermoplastic resin 3 is coated is adjusted, for example, from room temperature to 280 ° C., and preferably 250 ° C. or lower according to the lamination mode. After step 4 as described above, a resin-coated metal plate for a battery container can be obtained. When the dry lamination method is employed, it is preferable to perform aging after dry lamination in a temperature environment of, for example, 30 to 100 ° C. for a period of 1 to 7 days.

 そしてステップ5では、深絞り加工を行って、電池容器用金属板10を図4に示すような容器形状に成形する。より具体的には、本実施形態の容器形状は、矩形の電極板が収容可能なように四隅に曲率半径Rc(周方向のコーナーであるためRcと称する)の隅部が形成された深さDの矩形状の凹部を有している。また、この凹部の側壁と凹部の底面との間は曲率半径Rp(パンチのRで規定されるためRpと称する)でつながっている。なお、図4の容器では上述した凹部の四隅のコーナーRが等しくなっているが、このRc及びRpはそれぞれ異なった値としてもよい。
 ここで、かような曲率半径Rc及びRpと深さDの形状を有する電池容器の形状に対して本実施形態の電池容器用金属板10が非常に有効である理由について以下に詳述する。
Then, in step 5, deep drawing is performed to form the metal plate 10 for a battery container into a container shape as shown in FIG. More specifically, the container shape of the present embodiment has a depth in which corners of a radius of curvature Rc (referred to as Rc because it is a corner in the circumferential direction) are formed at four corners so that a rectangular electrode plate can be accommodated. D has a rectangular concave portion. The side wall of the concave portion and the bottom surface of the concave portion are connected by a radius of curvature Rp (referred to as Rp because it is defined by R of the punch). In the container of FIG. 4, the corners R of the four corners of the above-mentioned concave portion are equal, but Rc and Rp may be different values.
Here, the reason why the metal plate 10 for a battery case of the present embodiment is very effective for the shape of the battery case having the shapes of the curvature radii Rc and Rp and the depth D will be described in detail below.

<高容量化のための曲率半径Rc及びRpと深さD>
 まず電池容器用金属板10を電池容器として用いて高容量化するためには、成形加工の際の上記した凹部における四隅のRcと、凹部の側壁と底面との間のRp、および深さDのいずれも重要だが、特にRpと深さDのバランスが重要になる。なお、かようなバランスを確立することは、個々の電池を大型化させて、これまでの電池の複数個分の電池特性を一つの電池で担保できるようにすることが理想的になることから車載用途の電池容器として特に重要となる。また単セルの電池に限らず、複数の電池を集合させモジュール化して使用するような場合においても重要である。
 そして上記したRcとRpは、電極が配置される面積をより広げ、さらに電池内のデッドスペースを少なくする観点などから可能な限り双方とも曲率半径を小さくすることが望ましい。
 かような曲率半径Rpの値としては、好ましくは2mm未満、より好ましくは1.5mm以下である。
 また、かような曲率半径Rcの値としては、使用される用途及び電池サイズにより異なるが、好ましくは10mm未満、より好ましくは8mm以下、更に好ましくは5mm以下であり、特に容器の短辺の長さが50mmを下回る場合は3mm以下が好ましい。
<Radius of curvature Rc and Rp and depth D for higher capacity>
First, in order to increase the capacity by using the battery container metal plate 10 as a battery container, Rc at the four corners of the above-described concave portion during molding, Rp between the side wall and the bottom surface of the concave portion, and depth D Are important, but the balance between Rp and depth D is particularly important. Establishing such a balance is ideal because it is ideal to increase the size of each battery so that the battery characteristics of multiple batteries can be guaranteed by one battery. This is particularly important as a battery container for use in vehicles. It is important not only for a single-cell battery but also for a case where a plurality of batteries are assembled and used as a module.
For Rc and Rp described above, it is desirable that both have as small a radius of curvature as possible from the viewpoint of further increasing the area in which the electrodes are arranged and reducing the dead space in the battery.
The value of such a radius of curvature Rp is preferably less than 2 mm, more preferably 1.5 mm or less.
The value of the radius of curvature Rc varies depending on the use and battery size used, but is preferably less than 10 mm, more preferably 8 mm or less, and still more preferably 5 mm or less, and particularly the length of the short side of the container. If it is less than 50 mm, it is preferably 3 mm or less.

 一方で電池容器として用いて高容量化のためには、積層して収容する電極の数が増えることで電池全体としての容量増が図れることから、深さDを大きくすることも有効となる。かような深さDの値としては、5mm以上が好ましく、より好ましくは6mm以上である。
 このような背景の下で本発明者らが望ましい曲率半径Rpと深さDの関係について鋭意検討したところ、高容量化のために電池容器用金属板10を上記のような条件で加工を施す場合には成形性、成形後の樹脂フィルムとの密着性および成形後の耐内容物性の3面で課題があることに帰結した。
On the other hand, in order to increase the capacity by using it as a battery container, it is effective to increase the depth D because the capacity of the entire battery can be increased by increasing the number of electrodes that are stacked and accommodated. Such a value of the depth D is preferably 5 mm or more, more preferably 6 mm or more.
Under these circumstances, the present inventors have conducted intensive studies on the relationship between the desired radius of curvature Rp and the depth D. The metal plate 10 for a battery container is processed under the above-described conditions to increase the capacity. In this case, there were problems in moldability, adhesion to the resin film after molding, and content resistance after molding.

 すなわち、まず曲率半径Rpが小さくなればなるほど成形加工の難易度があがり、特に曲率半径Rpを1.5mm以下とすれば難易度が飛躍的にあがってしまう。さらに、深さDについては深い成形加工をしようとすればするほど、電池容器用金属板10の材料に対する加工条件が厳しくなってくる。特に曲率半径Rpが2mm未満という条件と、深さDが5mm以上という条件とを組み合わせた場合には、下記のような3つ課題が生じることが新たに判明した。 That is, first, the smaller the radius of curvature Rp becomes, the more difficult the molding process becomes. Particularly, if the radius of curvature Rp is set to 1.5 mm or less, the degree of difficulty increases dramatically. Further, as to the depth D, the deeper the forming process is performed, the more severe the processing conditions for the material of the battery container metal plate 10 become. In particular, it has been newly found that the following three problems occur when the condition that the curvature radius Rp is less than 2 mm and the condition that the depth D is 5 mm or more are combined.

 まず一つ目の課題としては、成形加工中の基材1の割れが生じやすくなることである。そもそも上記のような加工条件においては、従来のアルミニウムを基材1とした場合には、厚みを厚くしなければならなかったり、安定的な成形が難しかったりするため、実用には至っていない。安定的な成形が難しいという点において、例えば、絞り加工を行った際のフランジ部の波打ちやシワが大きくなり、容器の封止が不確実となるおそれがあった。
 一方で、本実施形態で説明したように基材1として鉄または鉄合金を用いる場合には、アルミニウムに比して比重が大きいため、電池重量の増加を抑制するために基材1の厚みを薄くする必要がある。このように基材1の厚みを薄くした場合には、基材1の割れなどが発生しやすくなることが分かった。
 次に二つ目の課題としては、成形加工後の基材1と樹脂フィルムとの密着性が挙げられる。上記のように基材1の厚みを薄くした場合には、成形加工時における基材1の変形の影響で樹脂フィルムの基材1からの剥離を誘発することが分かった。
The first problem is that the base material 1 is easily cracked during the forming process. In the first place, when the conventional aluminum is used as the base material 1 under the above-described processing conditions, the thickness has to be increased and stable molding is difficult, so that it has not been put to practical use. In terms of difficulty in stable molding, for example, there is a possibility that the waving and wrinkles of the flange portion when drawing is performed are increased, and the sealing of the container becomes uncertain.
On the other hand, when iron or an iron alloy is used as the base material 1 as described in the present embodiment, the specific gravity is larger than that of aluminum, so that the thickness of the base material 1 is reduced to suppress an increase in battery weight. Need to be thin. It has been found that when the thickness of the substrate 1 is reduced in this way, cracks and the like of the substrate 1 are likely to occur.
Next, as a second problem, the adhesion between the base material 1 after the forming process and the resin film can be mentioned. It has been found that when the thickness of the base material 1 is reduced as described above, the resin film is peeled off from the base material 1 under the influence of the deformation of the base material 1 during molding.

 次に三つ目の課題としては、成形加工後の耐内容物性(電解液に対する耐性)が挙げられる。かような成形加工後の耐内容物としては、電解液に浸漬した際の基材1と樹脂フィルムとの密着性の維持という課題の他、上記のような加工条件においては基材1そのものの耐内容物性が必要となる。すなわち、上記のごとく厳しい加工条件でプレス成形を行った場合には、基材1を被覆する樹脂フィルムにおいて損傷を受ける可能性がある。また、樹脂フィルム自体にそもそもピンホールなどの欠陥があった場合にも、当該欠陥が厳しい成形加工の中で広がりやすくなってしまう。
 このような場合には、電解液と基材1の表面とが接触することとなってしまうため、基材1の表面を溶出しにくい形態とする必要が生じてくる。なお、従来のようにアルミニウムを基材として採用しようとする場合、そもそもアルミニウムの成形性が悪いために上記のような厳しい加工条件での加工はそもそも不可能となる。
Next, as a third problem, there is a problem of content resistance (resistance to an electrolytic solution) after molding. As the resistant content after such molding, in addition to the problem of maintaining the adhesion between the substrate 1 and the resin film when immersed in the electrolytic solution, under the above-mentioned processing conditions, the substrate 1 itself may be used. Content resistance is required. That is, when press molding is performed under severe processing conditions as described above, the resin film covering the substrate 1 may be damaged. Further, even when the resin film itself has a defect such as a pinhole in the first place, the defect tends to spread in severe molding processing.
In such a case, since the electrolytic solution comes into contact with the surface of the substrate 1, it is necessary to make the surface of the substrate 1 difficult to elute. In the case where aluminum is used as the base material as in the prior art, processing under the above-mentioned strict processing conditions becomes impossible in the first place due to the poor formability of aluminum.

 以上で詳述した各課題に対し、本実施形態においては、上記したとおり0.5g/m以上のNiめっき層および0.05g/m以上のCrめっき層の少なくとも1つを含有する表面処理層2(電気めっき層)を有することにより、基材が電解液に溶出してしまうことを防ぐことが可能となり、さらに厳しい成形加工における樹脂フィルムとの密着性も十分に担保できることを見出したのである。 Surface to each problem detailed above, in the present embodiment, which contains at least one of the above-mentioned as 0.5 g / m 2 or more Ni plating layer and 0.05 g / m 2 or more Cr plating layer By having the treatment layer 2 (electroplating layer), it was possible to prevent the base material from being eluted into the electrolytic solution, and it was found that the adhesion to the resin film in severe molding processing could be sufficiently ensured. It is.

 なお電池容器は、電極板や電解液などの電池要素を収容した後で密封されるが、本実施形態の電池容器用金属板10は密封に用いられる電池容器の蓋部材としても適用できる。かような電池容器の構成部材である蓋部材は、図4に示した電池容器本体と同様な収容空間が形成されていてもよいし、平板のまま用いることもできる。また、電池容器の密封に際しては、絞り加工された収容部を有する電池容器本体の周縁のフランジ部で、上記した蓋部材とヒートシールするのが好ましい。この場合、電池容器本体と蓋部材の向かい合う面の被覆樹脂が、ポリプロピレン樹脂同士またはポリエステル樹脂同士のように同種類の樹脂が向き合うよう構成することが好ましい。なお上記した密封方法は一例であってこれに限らず、例えば公知の接着剤を用いてもよい。 The battery case is hermetically sealed after accommodating battery elements such as an electrode plate and an electrolytic solution. However, the metal plate for a battery case 10 of the present embodiment can also be applied as a lid member of a battery case used for sealing. The lid member, which is a constituent member of such a battery container, may have an accommodation space similar to that of the battery container body shown in FIG. 4 or may be used as a flat plate. When the battery container is sealed, it is preferable to heat seal the lid with the lid member at a peripheral flange portion of the battery container main body having the drawn housing portion. In this case, it is preferable that the covering resin on the surface facing the battery container body and the lid member be configured so that the same type of resin such as polypropylene resins or polyester resins face each other. Note that the above-described sealing method is an example and is not limited thereto. For example, a known adhesive may be used.

 本実施形態で得られた電池容器は、上述した本実施形態の電池容器用金属板10を用いて形成されるものであるため、ニッケルめっき金属板またはクロムめっき金属板と、樹脂との密着性が高く、それでいて量産加工性に優れるものであるため、アルカリ電池、ニッケル水素電池、ニッケル・カドミウム電池、リチウムイオン電池など種々の一次電池または二次電池の電池容器として好適に用いることができる。 Since the battery case obtained in the present embodiment is formed using the battery case metal plate 10 of the present embodiment, the adhesion between the nickel-plated metal plate or the chromium-plated metal plate and the resin is obtained. Therefore, it can be suitably used as a battery container for various primary batteries or secondary batteries such as alkaline batteries, nickel-metal hydride batteries, nickel-cadmium batteries, and lithium ion batteries.

 次に実施例を挙げて本発明についてより具体的に説明する。 Next, the present invention will be described more specifically with reference to examples.

<実施例1>
 まず基材1となる金属板(金属箔)として、下記に示す化学組成を有する極低炭鋼の冷間圧延板(厚さ80μm)を準備した。
C:0.01重量%、Mn:0.22重量%、Si:0.01重量%、P:0.012重量%、S:0.014重量%、残部:Feおよび不可避的不純物
<Example 1>
First, as a metal plate (metal foil) serving as the base material 1, a cold-rolled plate (thickness: 80 μm) of ultra low carbon steel having the chemical composition shown below was prepared.
C: 0.01% by weight, Mn: 0.22% by weight, Si: 0.01% by weight, P: 0.012% by weight, S: 0.014% by weight, balance: Fe and inevitable impurities

 次に、準備した金属板(金属箔)について焼鈍を650℃3時間行うことで、以下の特性を有する基材1を得た。
 ・引張強度(TS):293MPa
 ・伸び(EL):46%
 ・平面(圧延)方向と厚み方向の結晶粒径の比:1.2
 なお、結晶粒径は、図3に示すように、走査型電子顕微鏡(SEM)で電池容器用金属板10の断面写真の撮影を行った上でJIS G0551(附属書C)に準拠して、平面方向及び厚み方向のそれぞれについて測定した。
Next, the prepared metal plate (metal foil) was annealed at 650 ° C. for 3 hours to obtain a substrate 1 having the following characteristics.
-Tensile strength (TS): 293MPa
・ Elongation (EL): 46%
・ Ratio of crystal grain size in plane (rolling) direction and thickness direction: 1.2
In addition, as shown in FIG. 3, as shown in FIG. 3, after taking a photograph of a cross section of the metal plate 10 for a battery container with a scanning electron microscope (SEM), in accordance with JIS G0551 (Annex C), The measurement was performed in each of the plane direction and the thickness direction.

(表面処理層2の形成)
 そしてこの焼鈍後の基材1に対し、電解脱脂、硫酸浸漬の酸洗を行った後、下記条件にて電気めっきを行って、Niのめっき量が4.5g/mである電気めっき層2(Niめっき層)を形成した。なお、上記のNiめっき層の形成条件は、以下の通りとした。
(Niめっき層の形成条件)
 浴組成:硫酸ニッケル、塩化ニッケル、ホウ酸、ピット抑制剤
 pH:4.3
 浴温:55℃
 電流密度:10A/dm
(Formation of surface treatment layer 2)
Then, the base material 1 after the annealing is subjected to electrolytic degreasing and acid pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer having a Ni plating amount of 4.5 g / m 2. 2 (Ni plating layer) was formed. The conditions for forming the Ni plating layer were as follows.
(Formation condition of Ni plating layer)
Bath composition: nickel sulfate, nickel chloride, boric acid, pit inhibitor pH: 4.3
Bath temperature: 55 ° C
Current density: 10 A / dm 2

(熱可塑性樹脂3の形成)
 まず、熱可塑性樹脂3として、厚み25μmの延伸ポリアミドフィルムを準備した。該延伸ポリアミドフィルムの片面に、ウレタン系接着剤をグラビアロールにより塗布した。その後、塗布したウレタン系接着剤を加熱して乾燥させた。
 次に、表面処理層2が形成された基材1と、ウレタン系接着剤を塗布した延伸ポリアミドフィルムとを、表面処理層2とウレタン系接着剤とが接するように巻き戻して圧着し、ドライラミネート法により熱可塑性樹脂3を形成した。なお、延伸ポリアミドフィルムは表面処理層2が形成された基材1の片面にのみラミネートした。
 このようにして、電池容器用金属板10を得た。
(Formation of thermoplastic resin 3)
First, a stretched polyamide film having a thickness of 25 μm was prepared as the thermoplastic resin 3. A urethane-based adhesive was applied to one surface of the stretched polyamide film by a gravure roll. Thereafter, the applied urethane-based adhesive was dried by heating.
Next, the substrate 1 on which the surface treatment layer 2 is formed and the stretched polyamide film to which the urethane-based adhesive is applied are rewound so that the surface treatment layer 2 and the urethane-based adhesive are in contact with each other, and are pressed and dried. The thermoplastic resin 3 was formed by a lamination method. The stretched polyamide film was laminated only on one side of the substrate 1 on which the surface treatment layer 2 was formed.
Thus, a metal plate 10 for a battery container was obtained.

(成形性の評価)
 上記で得られた電池容器用金属板10に対し、外形が80mm×120mmの大きさに切断した上で、33mm×54mmの金型を用いて上記した凹部の成形後における深さDがそれぞれ5mm及び6mmとなるようにプレス成形(成形圧:0.9MPa)を行った。プレス成形は、延伸ポリアミドフィルムの側が電池容器外面側となるようにして行った。
(Evaluation of moldability)
With respect to the metal plate 10 for a battery container obtained above, the outer shape was cut into a size of 80 mm x 120 mm, and the depth D of each of the concave portions after molding was 5 mm using a 33 mm x 54 mm mold. And a press molding (molding pressure: 0.9 MPa) so as to be 6 mm. The press molding was performed such that the side of the stretched polyamide film was on the outer surface side of the battery container.

 なお、プレス成形した後における電池容器用金属板10に対する成形性の評価は、電池容器の四隅で基材1の割れや熱可塑性樹脂3の浮きや割れを目視にて観察し、次の基準で行った。
[評価基準]
 ○:目視で判定した結果、基材の割れや熱可塑性樹脂の浮き/割れが認められなかった。
 △:目視で判定した結果、実用には供せるが一部に割れや浮きが認められた。
 ×:目視で判定した結果、実用に供せない程度の基材の割れや熱可塑性樹脂の浮き/割れが認められた。
In addition, the evaluation of the moldability of the metal plate 10 for a battery container after the press molding was performed by visually observing cracks in the base material 1 and floating or cracking of the thermoplastic resin 3 at the four corners of the battery container, and according to the following criteria. went.
[Evaluation criteria]
:: As a result of visual judgment, no cracking of the base material or floating / cracking of the thermoplastic resin was observed.
B: As a result of visual judgment, cracking or floating was recognized in a part although it could be put to practical use.
X: As a result of visual judgment, cracks in the base material and floating / cracking of the thermoplastic resin were found to such an extent that they could not be put to practical use.

(耐内容物性の評価その1)
 耐内容物性に用いる電解液として、多くの使用が一般的に想定される下記の電解液を用いた。
[耐内容物性の評価に用いた電解液]
 エチレンカーボネート(EC)、ジメチルカーボネート(DMC)、ジエチルカーボネート(DEC)を重量比で1対1対1にした電解液に1mol/lの6フッ化リン酸リチウム(LiPF)を加え、その後、6フッ化リン酸リチウムに対し1000ppmの水分を添加。
(Evaluation of content resistance part 1)
As the electrolyte used for the content resistance, the following electrolyte, which is generally assumed to be used in many cases, was used.
[Electrolyte used for evaluation of content resistance]
1 mol / l of lithium hexafluorophosphate (LiPF 6 ) was added to an electrolyte in which ethylene carbonate (EC), dimethyl carbonate (DMC), and diethyl carbonate (DEC) were in a weight ratio of 1: 1 to 1; 1000 ppm of water was added to lithium hexafluorophosphate.

 この電解液に幅15mm×長さ100mmのサイズでカットした電池容器用金属板10を浸漬し、85℃の環境下で浸漬めっき材として所定の日数(一例として14日間)だけ保管した。なお、本評価における電池容器用金属板10としては、Niめっき層が形成され、熱可塑性樹脂3は被覆されていないものを使用した。また、深さDのプレス加工は未実施の状態で評価を行った。さらに電池容器用金属板10のうち評価を実施しない側についてはシーリングを行った。
 そしてこの浸漬めっき材に対し、所定の日数(例えば1日、7日又は14日)が経過した時点において常温に戻した後に目視により外観を観察した。
The metal plate 10 for a battery container cut into a size of 15 mm in width × 100 mm in length was immersed in this electrolytic solution, and stored as an immersion plating material for a predetermined number of days (for example, 14 days) in an environment of 85 ° C. In addition, as the metal plate 10 for battery containers in this evaluation, a metal plate having a Ni plating layer formed thereon and not covered with the thermoplastic resin 3 was used. In addition, the evaluation was performed in a state where the press working at the depth D was not performed. Further, sealing was performed on the side of the metal plate 10 for battery containers that was not evaluated.
The immersion plated material was returned to room temperature after a predetermined number of days (for example, 1, 7, or 14 days), and then visually observed.

 なお浸漬めっき材に対する耐内容物性評価その1は以下の基準で行った。
[評価基準]
 ○:目視で判定した結果、外観の変化が無かった。
 △:目視で判定した結果、変色するなど一部に外観の変化が有った。
 ×:目視で判定した結果、実用に供せない程度の基材の露出が認められた。
In addition, the evaluation of the physical property resistance to immersion plating material No. 1 was performed according to the following criteria.
[Evaluation criteria]
:: There was no change in the appearance as a result of the visual judgment.
B: As a result of visual judgment, there was a change in appearance such as discoloration in a part.
X: As a result of visual judgment, the base material was exposed to such an extent that it could not be practically used.

<実施例2>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのNiのめっき量が17.8g/mである点以外は、上記した実施例1と同様に行った。
<Example 2>
The same substrate as in Example 1 was used.
The process was performed in the same manner as in Example 1 except that the plating amount of Ni as the surface treatment layer 2 (electroplating layer) was 17.8 g / m 2 .

<実施例3>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのNiのめっき量が44.5g/mである点以外は、上記した実施例1と同様に行った。
<Example 3>
The same substrate as in Example 1 was used.
The process was performed in the same manner as in Example 1 except that the plating amount of Ni as the surface treatment layer 2 (electroplating layer) was 44.5 g / m 2 .

<実施例4>
 上記した実施例1と同じ基材を用いた。
 この基材に対してめっき量が8.9g/mのNiめっきを形成した後で、この表面処理層2(電気めっき層)に対して700℃で1分間の熱処理を施した。それ以外は、上記した実施例1と同様に行った。
<Example 4>
The same substrate as in Example 1 was used.
After Ni plating having a plating amount of 8.9 g / m 2 was formed on the substrate, the surface treatment layer 2 (electroplating layer) was subjected to a heat treatment at 700 ° C. for 1 minute. Other than that, it carried out similarly to Example 1 mentioned above.

<実施例5>
 上記した実施例1と同じ基材を用いた。
 この焼鈍後の基材に対し、電解脱脂、硫酸浸漬の酸洗を行った後、下記条件にて電気めっきを行った。正確なめっき量を測定するため、まずは銅板の上にFe-Ni合金めっきを実施し、蛍光X線にてNiとFeの付着量を求めた。その後、同条件にて鉄基材の上にFe-Ni合金めっきを実施した。本実施例においては、FeとNiの合計が8.9g/mであった。なお、上記の電気めっきの条件は、以下の通りとした。
(Fe-Ni合金めっきの条件)
 浴組成:硫酸第一鉄、硫酸ニッケル、ホウ酸、サッカリン、塩化ニッケル、ピット抑制剤、クエン酸類
 pH:2.0~3.0
 浴温:50℃
 電流密度:20~50A/dm
 上記した点以外については、実施例1と同様に行った。
<Example 5>
The same substrate as in Example 1 was used.
The base material after the annealing was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating was performed under the following conditions. In order to accurately measure the amount of plating, first, an Fe—Ni alloy plating was performed on a copper plate, and the amount of Ni and Fe deposited was determined by X-ray fluorescence. Thereafter, Fe—Ni alloy plating was performed on the iron base material under the same conditions. In this example, the total of Fe and Ni was 8.9 g / m 2 . The conditions for the electroplating were as follows.
(Fe-Ni alloy plating conditions)
Bath composition: ferrous sulfate, nickel sulfate, boric acid, saccharin, nickel chloride, pit inhibitors, citric acids pH: 2.0 to 3.0
Bath temperature: 50 ° C
Current density: 20-50 A / dm 2
Except for the above points, the same procedure as in Example 1 was performed.

<実施例6>
 上記した実施例1と同じ基材を用いた。
 そしてこの基材に対し、電解脱脂、硫酸浸漬の酸洗を行った後、下記条件にて電気めっきを行って、Crのめっき量が0.05g/mである電気めっき層2(Crめっき層)を形成した。なお、上記の電気めっきの条件は、以下の通りとした。
(Crめっきの条件)
 CrO:50g/l
 NaF:1.7g/l
 浴温度:45℃
 電流密度:30A/dm
 上記で得られた電池容器用金属板10に対し、実施例1と同様にして成形性の評価および耐内容物性の評価を行った。
<Example 6>
The same substrate as in Example 1 was used.
Then, the base material was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer 2 (Cr plating) having a Cr plating amount of 0.05 g / m 2. Layer). The conditions for the electroplating were as follows.
(Cr plating conditions)
CrO 3 : 50 g / l
NaF: 1.7 g / l
Bath temperature: 45 ° C
Current density: 30 A / dm 2
The metal sheet 10 for a battery container obtained above was evaluated for moldability and content resistance in the same manner as in Example 1.

<実施例7>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのCrめっき量が0.36g/mである点以外は、上記した実施例6と同様に行った。
<Example 7>
The same substrate as in Example 1 was used.
Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 0.36 g / m 2 , the same procedure was performed as in Example 6 described above.

<実施例8>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのCrめっき量が3.6g/mである点以外は、上記した実施例6と同様に行った。
<Example 8>
The same substrate as in Example 1 was used.
Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 3.6 g / m 2 , the same procedure was performed as in Example 6 described above.

<実施例9>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのCrめっき量が7.19g/mである点以外は、上記した実施例6と同様に行った。
<Example 9>
The same substrate as in Example 1 was used.
Except that the amount of Cr plating as the surface treatment layer 2 (electroplating layer) was 7.19 g / m 2 , the same procedure as in Example 6 was performed.

<比較例1>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのNiのめっき量が0.1g/mである点以外は、上記した実施例1と同様に行った。
<Comparative Example 1>
The same substrate as in Example 1 was used.
Except that the amount of Ni plating as the surface treatment layer 2 (electroplating layer) was 0.1 g / m 2 , the procedure was the same as in Example 1 described above.

<比較例2>
 上記した実施例1と同じ基材を用いた。
 そしてこの基材に対し、電解脱脂、硫酸浸漬の酸洗を行った後、下記条件にて電気めっきを行って、Znのめっき量が3.6g/mである電気めっき層2(Znめっき層)を形成した。なお、上記の電気めっきの条件は、以下の通りとした。
(Znめっきの条件)
 ZnSO・7HO:220~300g/L
 硫酸アンモニウム:25~35g/L
 pH:1.0~2.0
 浴温 :50~60 ℃
 電流密度 :10 A/dm
 上記で得られた電池容器用金属板10に対し、実施例1と同様にして成形性の評価および耐内容物性の評価を行った。
<Comparative Example 2>
The same substrate as in Example 1 was used.
The base material is subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating is performed under the following conditions to obtain an electroplating layer 2 (Zn plating) having a Zn plating amount of 3.6 g / m 2. Layer). The conditions for the electroplating were as follows.
(Conditions for Zn plating)
ZnSO 4 · 7H 2 O: 220 ~ 300g / L
Ammonium sulfate: 25-35 g / L
pH: 1.0 to 2.0
Bath temperature: 50-60 ° C
Current density: 10 A / dm 2
With respect to the metal plate 10 for a battery container obtained above, evaluation of the moldability and the evaluation of the content resistance were performed in the same manner as in Example 1.

<比較例3>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのZnのめっき量が7.14g/mである点以外は、上記した比較例2と同様に行った。
<Comparative Example 3>
The same substrate as in Example 1 was used.
Except that the plating amount of Zn as the surface treatment layer 2 (electroplating layer) was 7.14 g / m 2 , the same procedure was performed as in Comparative Example 2 described above.

<比較例4>
 上記した実施例1と同じ基材を用いた。
 そしてこの基材に対し、電解脱脂、硫酸浸漬の酸洗を行った後、下記条件にて電気めっきを行って、Snのめっき量が1.4g/mである電気めっき層2(Snめっき層)を形成した。なお、上記の電気めっきの条件は、以下の通りとした。
(Snめっきの条件)
 硫酸第一錫:30~80g/L
 フェノールスルフォン酸:30~60g/L
 エトキシ化-αナフトール:2~6g/L
 エトキシ化-αナフトールスルフォン酸:4~12g/L
 pH:1.0~2.0
 浴温:40~55℃
 電流密度:2.5~10A/dm
 上記で得られた電池容器用金属板10に対し、実施例1と同様にして成形性の評価および耐内容物性の評価を行った。
<Comparative Example 4>
The same substrate as in Example 1 was used.
Then, the base material was subjected to electrolytic degreasing and pickling by immersion in sulfuric acid, and then electroplating under the following conditions to obtain an electroplating layer 2 (Sn plating) having a Sn plating amount of 1.4 g / m 2. Layer). The conditions for the electroplating were as follows.
(Sn plating conditions)
Stannous sulfate: 30-80 g / L
Phenolsulfonic acid: 30-60 g / L
Ethoxy-α-naphthol: 2 to 6 g / L
Ethoxylated α-naphtholsulfonic acid: 4 to 12 g / L
pH: 1.0 to 2.0
Bath temperature: 40-55 ° C
Current density: 2.5 to 10 A / dm 2
With respect to the metal plate 10 for a battery container obtained above, evaluation of the moldability and the evaluation of the content resistance were performed in the same manner as in Example 1.

<比較例5>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのSnのめっき量が2.8g/mである点以外は、上記した比較例4と同様に行った。
<Comparative Example 5>
The same substrate as in Example 1 was used.
Except that the amount of Sn plating as the surface treatment layer 2 (electroplating layer) was 2.8 g / m 2 , the same procedure was performed as in Comparative Example 4 described above.

<比較例6>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)としてのSnのめっき量が11.2g/mである点以外は、上記した比較例4と同様に行った。
<Comparative Example 6>
The same substrate as in Example 1 was used.
Except that the amount of Sn plating as the surface treatment layer 2 (electroplating layer) was 11.2 g / m 2 , the same procedure was performed as in Comparative Example 4 described above.

<比較例7>
 上記した実施例1と同じ基材を用いた。
 この基材に対して表面処理層2(電気めっき層)は形成せずに電池容器用金属板10を得た。そしてこの電池容器用金属板10(表面処理ナシ)に対し、実施例1と同様にして成形性の評価および耐内容物性の評価を行った。
<Comparative Example 7>
The same substrate as in Example 1 was used.
The metal plate 10 for a battery container was obtained without forming the surface treatment layer 2 (electroplating layer) on the substrate. Then, in the same manner as in Example 1, evaluation of the moldability and the evaluation of the content resistance were performed on the battery container metal plate 10 (surface-treated pear).

<比較例8>
 板厚を50μmに変更した以外は、比較例7と同様に行った。
<Comparative Example 8>
The same operation as in Comparative Example 7 was performed except that the plate thickness was changed to 50 μm.

<実施例10>
 上記した実施例1と同じ基材を用いた。
 この基材に対し、実施例1と同様の手法にて、Niのめっき量が8.9g/mである電気めっき層2(Niめっき層)を形成した。
 次いで、このようにして得られた基材に対し、容器内面側となる一方の面(Niめっき層上)には溶融した酸変性ポリプロピレンを介してポリプロピレンフィルムを押し出しラミネート法で形成した。さらに容器外面側となる一方の面にはウレタン系接着剤を介して延伸ポリアミドフィルムをドライラミネート法で形成し、これにより電池容器用金属板10を得た。なお、このときのラミネート温度(基材の温度)は、250℃とした。
<Example 10>
The same substrate as in Example 1 was used.
An electroplating layer 2 (Ni plating layer) having a Ni plating amount of 8.9 g / m 2 was formed on this base material in the same manner as in Example 1.
Next, a polypropylene film was formed by extrusion lamination on one surface (on the Ni plating layer) on the inner surface side of the container via the molten acid-modified polypropylene with respect to the base material thus obtained. Further, a stretched polyamide film was formed on one surface on the outer surface side of the container via a urethane-based adhesive by a dry laminating method, whereby a metal plate 10 for a battery container was obtained. The lamination temperature (base temperature) at this time was 250 ° C.

(成形性の評価)
 上記で得られた電池容器用金属板10に対し、実施例1と同様の手法にてプレス加工を施した後に、成形性の評価を行った。
(Evaluation of moldability)
After performing press working on the metal plate 10 for a battery container obtained as described above in the same manner as in Example 1, the moldability was evaluated.

(耐内容物性の評価その2)
 耐内容物性に用いる電解液としては、上記した実施例1と同じ電解液を用いた。この電解液に、上記のプレス加工を施した電池容器用金属板10を浸漬し、85℃の環境下で浸漬ラミネート材として所定の日数(一例として14日間)だけ保管した。
 そしてこの浸漬ラミネート材に対し、それぞれ所定の日数(1日、7日又は14日)が経過した時点において常温に戻し、ORIENTEC社製 TENSILON RTC-1210A基材1と接着剤(酸変性ポリプロピレン)間のラミネート強度を測定した。測定の方法としては、T型剥離で、引張速度100mm/分の条件で行った。
 そして、基材がアルミニウムの場合(比較例12)における初日時点でのラミネート強度の値を100%とした場合の、各サンプルでそれぞれ上記日数経過時点でのラミネート強度の割合を算出し、ピール強度残存率とした。
(Evaluation of content resistance 2)
As the electrolytic solution used for the content resistance, the same electrolytic solution as in Example 1 described above was used. The above-described pressed metal plate 10 for a battery container was immersed in the electrolytic solution, and stored as an immersion laminate material for a predetermined number of days (for example, 14 days) in an environment of 85 ° C.
After a predetermined number of days (1 day, 7 days or 14 days) has elapsed, the temperature of the immersion laminate material is returned to room temperature, and the temperature of the immersion laminate material between the TENSILON RTC-1210A substrate 1 made by ORIENTEC and the adhesive (acid-modified polypropylene) Was measured for laminate strength. As a measurement method, T-peeling was performed under the condition of a tensile speed of 100 mm / min.
Then, when the value of the lamination strength at the first day in the case where the base material was aluminum (Comparative Example 12) was set to 100%, the ratio of the lamination strength after the number of days described above was calculated for each sample, and the peel strength was calculated. The residual rate was used.

 なお浸漬ラミネート材に対する耐内容物性評価は、上記ピール強度残存率を用いて以下の基準で行った。
[評価基準]
 ○:浸漬試験後のピール強度残存率100~60%
 △:浸漬試験後のピール強度残存率60~40%
 ×:浸漬試験後のピール強度残存率40~0%
The evaluation of the content resistance of the immersion laminate material was performed using the above-described residual peel strength according to the following criteria.
[Evaluation criteria]
:: Peel strength residual ratio after immersion test 100 to 60%
Δ: Peel strength residual rate after immersion test 60 to 40%
×: Persistence of peel strength after immersion test 40 to 0%

<実施例11>
 上記した実施例1と同じ基材を用いた。
 表面処理層2(電気めっき層)として実施例6と同様のCrめっき浴を用いてCrめっき量が0.1g/mのCrめっき層とした点以外は、上記した実施例10と同様に行った。
<Example 11>
The same substrate as in Example 1 was used.
As in Example 10 described above, except that a Cr plating layer having a Cr plating amount of 0.1 g / m 2 was used as the surface treatment layer 2 (electroplating layer) using the same Cr plating bath as in Example 6. went.

<比較例9>
 上記した比較例8と同じ厚み(50μm)として焼鈍を行わない硬質の基材を用いた。
 この基材に対して比較例2で示したZnめっき浴を用いてZnめっき量が5.0g/mのZnめっき層を表面処理層2(電気めっき層)とした点以外は、上記した実施例10と同様に行った。
 なお、結晶粒径は、図5に示すように、走査型電子顕微鏡(SEM)で電池容器用金属板10の断面写真の撮影を行った上でJIS G0551(附属書C)に準拠して、平面方向及び厚み方向のそれぞれについて測定した。
<Comparative Example 9>
A hard base material having the same thickness as that of Comparative Example 8 (50 μm) and not subjected to annealing was used.
Using the Zn plating bath shown in Comparative Example 2 for this substrate, the Zn plating layer having a Zn plating amount of 5.0 g / m 2 was used as the surface treatment layer 2 (electroplating layer) as described above. Performed in the same manner as in Example 10.
As shown in FIG. 5, the crystal grain size was determined by taking a cross-sectional photograph of the battery container metal plate 10 with a scanning electron microscope (SEM) and then conforming to JIS G0551 (Annex C). The measurement was performed in each of the plane direction and the thickness direction.

<比較例10>
 板厚が80μmと変更した以外は比較例9と同じ硬質の基材を用いた。
 この基材に対して比較例9と同様の手法でZnめっきを形成し、さらにこのZnめっき層上に以下の条件でCrめっき量が0.01g/mとなるようにクロメート処理を行って表面処理層2(電気めっき層)を形成した。
(クロメート処理の浴組成、条件)
 無水クロム酸:25g/l
 全クロム量:5mg/m
 上記のようにして得られた電池容器用金属板10に対し、実施例10と同様の手法にて成形性の評価と耐内容物性の評価をそれぞれ行った。
<Comparative Example 10>
The same hard substrate as in Comparative Example 9 was used except that the plate thickness was changed to 80 μm.
Zn plating was formed on this base material in the same manner as in Comparative Example 9, and chromate treatment was further performed on this Zn plating layer under the following conditions so that the Cr plating amount was 0.01 g / m 2. Surface treatment layer 2 (electroplating layer) was formed.
(Bath composition and conditions for chromate treatment)
Chromic anhydride: 25 g / l
Total chromium amount: 5 mg / m 2
With respect to the metal plate 10 for a battery container obtained as described above, the evaluation of the formability and the evaluation of the content resistance were performed in the same manner as in Example 10.

<比較例11>
 実施例1と同様の基材を用い、表面処理層2を形成する前に基材に対して焼鈍を行ったこと以外は、比較例10と同様にして行った。
<Comparative Example 11>
The procedure was performed in the same manner as in Comparative Example 10 except that the same substrate as in Example 1 was used and annealing was performed on the substrate before forming the surface treatment layer 2.

<比較例12>
 基材として厚さ40μmのアルミニウムの冷間圧延板(O材)を準備した。
 この基材に対し、実施例10と同様に、容器内面側となる一方の面には溶融した酸変性ポリプロピレンを介してポリプロピレンフィルムを押し出しラミネート法で形成するとともに、容器外面側となる一方の面にはウレタン系接着剤を介して延伸ポリアミドフィルムをドライラミネート法でそれぞれ形成して電池容器用金属板10を得た。なお、表面処理層2は形成しなかった。
 上記で得られた電池容器用金属板10に対し、実施例10と同様の手法にて成形性の評価と耐内容物性の評価をそれぞれ行った。
<Comparative Example 12>
A 40 μm-thick cold-rolled aluminum plate (O-material) was prepared as a substrate.
On this base material, as in Example 10, a polypropylene film was formed by extrusion lamination on one surface on the inner surface side of the container via a molten acid-modified polypropylene, and one surface on the outer surface side of the container. Then, a stretched polyamide film was formed by a dry lamination method via a urethane-based adhesive to obtain a metal plate 10 for a battery container. In addition, the surface treatment layer 2 was not formed.
With respect to the metal plate 10 for a battery container obtained above, the evaluation of the moldability and the evaluation of the content resistance were performed in the same manner as in Example 10.

<実施例12>
 上記した実施例1と同じ基材を用いた。
 この基材の一方の面に対して、上記した実施例4と同様の手法でNi-Fe拡散層(Niめっき層)からなる表面処理層2を形成した。
 次いで、この基材の他方の面に、上記した比較例11と同様の手法でZnめっき層及びクロメート処理からなる表面処理層2を形成した。
<Example 12>
The same substrate as in Example 1 was used.
On one surface of the substrate, a surface treatment layer 2 composed of a Ni—Fe diffusion layer (Ni plating layer) was formed in the same manner as in Example 4 described above.
Next, on the other surface of the base material, a Zn plating layer and a surface treatment layer 2 formed by a chromate treatment were formed in the same manner as in Comparative Example 11 described above.

 このように表面処理して得られた基材に対し、Ni-Fe拡散層からなる面を内面側に、Znめっき層及びクロメート処理からなる面を外面側になるようにして、上記した実施例10と同様に、内面側となる面にポリプロピレンフィルムを、外面側となる面に延伸ポリアミドフィルムをラミネートし、これにより電池容器用金属板10を得た。そしてこの電池容器用金属板10に対し、プレス加工を施した後、上記した成形性及び耐内容物性の評価を行った。
 上記した評価の結果、内面側および外面側ともに成形性は問題なく、耐内容物性に関しても14日目まで「○」であった。
The substrate obtained by performing the surface treatment in this manner is configured such that the surface composed of the Ni—Fe diffusion layer is on the inner surface side and the surface composed of the Zn plating layer and the chromate treatment is the outer surface side. Similarly to 10, a polypropylene film was laminated on the inner surface and a stretched polyamide film was laminated on the outer surface, whereby a metal plate 10 for a battery container was obtained. Then, after performing press working on the metal plate 10 for a battery container, the above-described moldability and content resistance were evaluated.
As a result of the evaluation described above, there was no problem in the moldability on both the inner surface and the outer surface, and the content resistance was also “○” until the 14th day.

 上記した実施例1~11及び比較例で用いた各サンプルの材料仕様を表1に示す。さらに、各実施例1~9及び比較例1~12で用いたサンプルに対する表面処理の仕様と各めっき量、並びに耐内容物性1と成形性の評価を表2に示す。さらに実施例10~11および比較例9~12で用いたサンプルに対する表面処理の仕様と各めっき量、並びに耐内容物性2と成形性の評価を表3に示す。 Table 1 shows the material specifications of each sample used in the above Examples 1 to 11 and Comparative Example. In addition, Table 2 shows the surface treatment specifications and the plating amounts for the samples used in Examples 1 to 9 and Comparative Examples 1 to 12, and evaluations of the content resistance 1 and the moldability. Further, Table 3 shows the specifications of the surface treatment and the respective plating amounts, and the evaluation of the physical property resistance 2 and the moldability of the samples used in Examples 10 to 11 and Comparative Examples 9 to 12.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002

Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003

 表2に示した各種の電池容器用金属板(熱可塑性樹脂3の被覆ナシ)に対する評価において、実施例1~9では電池缶用途として耐え得る耐内容物性と成形性を兼ね備えた結果を得ることができた。これは鉄又は鉄の合金がベースとなった本実施形態における電池容器用金属板において、電池容器としての加工性(成形性)に適した空間を確保するに留まらず電解液に対する耐食性(耐内容物性)をも兼ね備えていることを意味する。一方で比較例1~8ではそもそも電池容器としての使用に耐え得るだけの充分な耐内容物性を具備していないことが判明した。 In the evaluation of various types of metal plates for battery containers (pear coated with the thermoplastic resin 3) shown in Table 2, in Examples 1 to 9, obtaining a result having both the content resistance and the moldability that can withstand the use for battery cans. Was completed. This is because, in the metal plate for a battery container according to the present embodiment based on iron or an alloy of iron, not only a space suitable for workability (formability) as a battery container is ensured, but also a corrosion resistance against an electrolytic solution (content resistance). Physical properties). On the other hand, it was found that Comparative Examples 1 to 8 did not have sufficient content resistance enough to withstand use as a battery container in the first place.

 また、表3に示すように、表面処理層2上に熱可塑性樹脂3(オレフィン系樹脂の一例としてのポリプロピレン樹脂)が被覆された実施例10及び11においても、アルミニウムを用いた比較例12と同等程度に、電池缶用途として耐え得る耐内容物性と成形性を兼ね備えた結果を得ることができた。一方で比較例10及び11ではやはり電池容器としての使用に耐え得る耐内容物性を具備していないことが判明した。 Further, as shown in Table 3, in Examples 10 and 11 in which the surface treatment layer 2 was coated with the thermoplastic resin 3 (a polypropylene resin as an example of an olefin resin), Comparative Examples 12 and 11 using aluminum were also used. As a result, it was possible to obtain a result having both the content resistance and the moldability that can withstand the use of a battery can. On the other hand, it was found that Comparative Examples 10 and 11 did not have the content resistance enough to withstand use as a battery container.

 本発明の電池容器用金属板およびその製造方法は、リチウムイオン二次電池などの電池容器の用途として充分な成形性と耐内容物性を示すことができ、電池を使用する幅広い分野の産業への適用が可能である。 INDUSTRIAL APPLICABILITY The metal plate for a battery container of the present invention and the method for producing the same can exhibit sufficient moldability and content resistance for use in a battery container such as a lithium ion secondary battery, and can be used in a wide range of industries using batteries. Applicable.

1 基材
2 表面処理層
3 熱可塑性樹脂
10 電池容器用金属板
DESCRIPTION OF SYMBOLS 1 Base material 2 Surface treatment layer 3 Thermoplastic resin 10 Metal plate for battery containers

Claims (10)

 電池容器として用いられる電池容器用金属板であって、
 鉄又は鉄の合金からなり、厚みが10~100μmである基材と、
 前記基材の少なくとも片方の面上に形成される、0.5~50.0g/mのNiめっき層および0.05~10.0g/mのCrめっき層の少なくとも1つを含有する電気めっき層と、
 を有することを特徴とする電池容器用金属板。
A metal plate for a battery container used as a battery container,
A base material made of iron or an alloy of iron and having a thickness of 10 to 100 μm;
Is formed on at least one surface of the base material, contains at least one of 0.5 Ni plating layer ~ 50.0 g / m 2 and 0.05 ~ 10.0g / m 2 of Cr plating layer An electroplating layer,
A metal plate for a battery container, comprising:
 前記電気Crめっき層は、Cr水和酸化物の割合よりも金属Crの割合が大である請求項1に記載の電池容器用金属板。 The metal plate for a battery container according to claim 1, wherein the ratio of the metal Cr in the electrochromic plating layer is higher than the ratio of the hydrated Cr oxide.  前記電気Niめっき層は、Niのみで構成されるNiめっき層、Feが拡散したFe-Ni拡散層、及びFeとNiとが共に電析したFe-Ni合金めっき層の中から選択される1つを含む請求項1又は2に記載の電池容器用金属板。 The electric Ni plating layer is selected from a Ni plating layer composed of only Ni, an Fe—Ni diffusion layer in which Fe is diffused, and an Fe—Ni alloy plating layer in which both Fe and Ni are electrodeposited. The metal plate for a battery container according to claim 1, comprising:  前記基材のうち前記電池容器の内面側となる面は、ポリオレフィン系樹脂で被覆されている請求項1~3のいずれか一項に記載の電池容器用金属板。 The metal plate for a battery container according to any one of claims 1 to 3, wherein a surface of the base material on the inner surface side of the battery container is coated with a polyolefin-based resin.  前記ポリオレフィン系樹脂はポリプロピレン樹脂であって、
 前記基材と前記ポリプロピレン樹脂との間には酸変性ポリオレフィン層が介在する請求項4に記載の電池容器用金属板。
The polyolefin resin is a polypropylene resin,
The metal plate for a battery container according to claim 4, wherein an acid-modified polyolefin layer is interposed between the base material and the polypropylene resin.
 前記基材のうち前記電池容器の外面側となる面は、ポリエステル樹脂、ポリアミド樹脂、ポリオレフィン樹脂のいずれかで被覆されている請求項1~5のいずれか一項に記載の電池容器用金属板。 The metal plate for a battery container according to any one of claims 1 to 5, wherein a surface of the base material on an outer surface side of the battery container is coated with any of a polyester resin, a polyamide resin, and a polyolefin resin. .  前記基材の引張強度が260~700MPaであり、
 前記基材の伸びが5~55%である請求項1~6のいずれか一項に記載の電池容器用金属板。
The substrate has a tensile strength of 260 to 700 MPa,
The metal plate for a battery container according to any one of claims 1 to 6, wherein the elongation of the base material is 5 to 55%.
 前記基材の平面方向と厚み方向における結晶粒径の比が0.8~8である請求項1~7のいずれか一項に記載の電池容器用金属板。 The metal plate for a battery container according to any one of claims 1 to 7, wherein the ratio of the crystal grain size in the plane direction and the thickness direction of the base material is 0.8 to 8.  前記基材のうち前記電池容器の内面側となる面には、前記Niめっき層および前記Crめっき層の少なくとも1つを含有する電気めっき層が形成されているとともに、
 前記基材のうち前記電池容器の外面側となる面には、3~30g/mのZnめっき層又はZn合金めっき層を含有する電気めっき層が形成されている請求項1~8のいずれか一項に記載の電池容器用金属板。
An electroplating layer containing at least one of the Ni plating layer and the Cr plating layer is formed on a surface of the base material on the inner surface side of the battery container,
The electroplating layer containing a Zn plating layer or a Zn alloy plating layer of 3 to 30 g / m 2 is formed on a surface of the base material on the outer surface side of the battery container. The metal plate for a battery container according to claim 1.
 鉄又は鉄の合金の基材からなる電池容器用金属板の製造方法であって、
 前記基材を冷間圧延してその厚みを10~100μmとする工程と、
 前記基材の少なくとも片方の面上に、0.5~50.0g/mのNiめっき層および0.05~10.0g/mのCrめっき層の少なくとも1つを含有する電気めっき層を形成する工程と、
 を有することを特徴とする電池容器用金属板の製造方法。
A method for producing a metal plate for a battery container comprising a base material of iron or an alloy of iron,
Cold rolling the substrate to a thickness of 10 to 100 μm;
On at least one surface of said substrate, electroplated layer containing at least one of 0.5 Ni plating layer ~ 50.0 g / m 2 and 0.05 ~ 10.0g / m 2 of Cr plating layer Forming a;
A method for producing a metal plate for a battery container, comprising:
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