WO2017217085A1 - Electrolytic copper foil, lithium ion secondary cell negative electrode, lithium ion secondary cell, and printed wiring board - Google Patents
Electrolytic copper foil, lithium ion secondary cell negative electrode, lithium ion secondary cell, and printed wiring board Download PDFInfo
- Publication number
- WO2017217085A1 WO2017217085A1 PCT/JP2017/014131 JP2017014131W WO2017217085A1 WO 2017217085 A1 WO2017217085 A1 WO 2017217085A1 JP 2017014131 W JP2017014131 W JP 2017014131W WO 2017217085 A1 WO2017217085 A1 WO 2017217085A1
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- Prior art keywords
- copper foil
- elongation
- electrolytic copper
- ion secondary
- lithium ion
- Prior art date
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 207
- 239000011889 copper foil Substances 0.000 title claims abstract description 196
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 33
- 239000011888 foil Substances 0.000 claims description 46
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 229910052799 carbon Inorganic materials 0.000 claims description 19
- 238000007788 roughening Methods 0.000 claims description 8
- 238000010030 laminating Methods 0.000 claims description 5
- 229910052802 copper Inorganic materials 0.000 abstract description 11
- 239000010949 copper Substances 0.000 abstract description 11
- 230000037303 wrinkles Effects 0.000 description 35
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- 238000005868 electrolysis reaction Methods 0.000 description 8
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- 239000000203 mixture Substances 0.000 description 7
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 6
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- 238000011156 evaluation Methods 0.000 description 6
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- 238000009864 tensile test Methods 0.000 description 5
- 239000010936 titanium Substances 0.000 description 5
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- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
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- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910012851 LiCoO 2 Inorganic materials 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000002202 Polyethylene glycol Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 2
- BQJTUDIVKSVBDU-UHFFFAOYSA-L copper;sulfuric acid;sulfate Chemical compound [Cu+2].OS(O)(=O)=O.[O-]S([O-])(=O)=O BQJTUDIVKSVBDU-UHFFFAOYSA-L 0.000 description 2
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- 239000007774 positive electrode material Substances 0.000 description 2
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 description 2
- 238000012935 Averaging Methods 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 1
- 229910001290 LiPF6 Inorganic materials 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
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- 229910052801 chlorine Inorganic materials 0.000 description 1
- 229910021446 cobalt carbonate Inorganic materials 0.000 description 1
- ZOTKGJBKKKVBJZ-UHFFFAOYSA-L cobalt(2+);carbonate Chemical compound [Co+2].[O-]C([O-])=O ZOTKGJBKKKVBJZ-UHFFFAOYSA-L 0.000 description 1
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- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
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- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
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Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C9/00—Alloys based on copper
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D1/00—Electroforming
- C25D1/04—Wires; Strips; Foils
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/66—Current collectors
- H01G11/70—Current collectors characterised by their structure
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/03—Use of materials for the substrate
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/03—Use of materials for the substrate
- H05K1/0313—Organic insulating material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to an electrolytic copper foil, a negative electrode for a lithium ion secondary battery, a lithium ion secondary battery, and a printed wiring board having the electrolytic copper foil.
- Conventional means for realizing thin copper foil include, for example, higher strength of electrolytic copper foil, and improvement of characteristics that do not easily cause characteristic deterioration such as softening even during heat treatment in the battery manufacturing process (high heat resistance) (For example, Patent Documents 1 to 4 etc.).
- the strength and heat resistance of the electrolytic copper foil are increased by adding additives to the electrolyte and incorporating the additive components into the crystal grains and grain boundaries of the matrix during electrodeposition. Generally, it is carried out by increasing the strength by the miniaturization effect or by the pinning effect.
- An object of the present invention is to provide an electrolytic copper foil, a negative electrode for a lithium ion secondary battery, a lithium ion secondary battery, and a printed wiring board having high strength, high heat resistance and low elongation anisotropy.
- the present inventors examined the development of a new electrolytic copper foil based on the above design guidelines, and found that an electrolytic copper foil having high strength and high heat resistance had an elongation anisotropy (elongation value depending on the direction in which the tensile test was performed). However, the details of this phenomenon will be described later, and the reduction in elongation anisotropy effectively reduces the occurrence of wrinkles and foil breaks after charging and discharging, and the occurrence of wrinkles and foil breaks after pressing. We found that it can be reduced.
- the electrolytic copper foil generally produces a long product (electrolytic copper foil) by depositing copper on the surface of the titanium cathode drum, continuously peeling it off and winding it.
- the rotation direction of the drum that is, the longitudinal direction of the long product is expressed as MD
- the direction orthogonal to the MD direction that is, the width direction of the copper foil is expressed as TD.
- Patent Documents 1 to 4 pays attention to the elongation anisotropy of the high-strength, high-heat-resistant electrolytic copper foil, and in such a configuration, wrinkles and foil breakage in the next-generation lithium ion secondary battery are not observed. The occurrence of this cannot be effectively suppressed.
- the conventional general electrolytic copper foil also has a slight elongation anisotropy of about 11.1%, which is due to surface irregularities caused by the transfer of buff lines present in the electrolytic drum. It is considered that the anisotropy of elongation is small, and it is difficult to cause wrinkles and foil breakage.
- next-generation lithium-ion secondary batteries will become full-scale in the future, it is considered essential to develop high-strength and high-heat-resistant foils, and it is important to reduce the anisotropy of the elongation that becomes apparent along with it. It can be said that it is a difficult task. That is, in the current collector application of a high-capacity lithium ion secondary battery, it is desired to develop a copper foil having high strength, high heat resistance, and low elongation anisotropy.
- the present inventors diligently studied, found a method for solving the above-mentioned problems, and completed the present invention. That is, the gist of the present invention is as follows. (1) An electrolytic copper foil containing 0.001 to 0.020% by mass of carbon, wherein the electrolytic copper foil has a ten-point average roughness (Rz) of 1.8 ⁇ m or less, and the electrolytic copper foil is heated at 150 ° C. for 1 hour.
- Rz ten-point average roughness
- the tensile strength of the copper foil is 400 MPa or more
- the elongation in the width direction (TD) of the copper foil is 2% or more
- the elongation in the longitudinal direction (MD) of the copper foil And an elongation anisotropy ⁇ [(MD elongation ⁇ TD elongation) / MD elongation] ⁇ 100 ⁇ which is a parameter representing a difference in elongation in the width direction (TD) is 50% or less.
- an electrolytic copper foil containing 0.001 to 0.020% by mass of carbon, the electrolytic copper foil having a ten-point average roughness (Rz) of 1.8 ⁇ m or less, and the electrolytic copper foil at 150 ° C.
- Tensile properties when measured at room temperature after heating for 1 hour are as follows: the tensile strength of the copper foil is 400 MPa or more, the elongation in the width direction (TD) of the copper foil is 2% or more, and the longitudinal direction of the copper foil (MD ) And elongation anisotropy ⁇ [(MD elongation ⁇ TD elongation) / MD elongation] ⁇ 100 ⁇ , which is a parameter representing the difference between the elongation in the width direction (TD), is 50% or less. It has become possible to provide an electrolytic copper foil with high heat resistance and low elongation anisotropy.
- the electrolytic copper foil of the present invention is used for, for example, a lithium ion secondary battery provided with a negative electrode for a lithium ion secondary battery having a current collector, the foil capacity and wrinkle at the time of charging / discharging are prevented, the battery capacity, Since cycle characteristics and safety can be improved, it is suitable for next-generation lithium ion secondary battery applications. Furthermore, if the electrolytic copper foil of the present invention is used for a printed wiring board formed by laminating with an insulating film, foil breakage and wrinkle generation during pressing can be prevented, and the dimensional stability can be improved.
- FIG. 1 shows test pieces cut in the MD and TD directions for a conventional general electrolytic copper foil and a conventional high-strength / high-heat-resistant electrolytic copper foil. It is a typical stress-strain curve (SS curve) obtained by measurement.
- FIG. 2 is a conceptual diagram for explaining a main part of a production apparatus for producing the electrolytic copper foil of the present invention.
- the electrolytic copper foil of the present invention is an electrolytic copper foil containing 0.001 to 0.020 mass% of carbon, and the electrolytic copper foil has a ten-point average roughness (Rz) of 1.8 ⁇ m or less.
- Rz ten-point average roughness
- Tensile properties when heated at room temperature for 1 hour and then measured at room temperature (20 ° C ⁇ 15 ° C) are as follows: The tensile strength of the copper foil is 400 MPa or more and the elongation in the width direction (TD) of the copper foil is 2% or more.
- the elongation anisotropy ⁇ [(MD elongation ⁇ TD elongation) / MD elongation] ⁇ 100 ⁇ which is a parameter representing the difference between the elongation in the longitudinal direction (MD) of the copper foil and the elongation in the width direction (TD) is 50. % Of the electrolytic copper foil.
- the carbon (C) content in the electrolytic copper foil needs to be 0.001 to 0.020 mass%. If the carbon content is less than 0.001% by mass, sufficient strength and heat resistance cannot be obtained, and if the carbon content exceeds 0.020% by mass, the ductility decreases and the foil breaks during handling or charge / discharge. It is easy to occur. Therefore, the carbon content is set to 0.001 to 0.020% by mass.
- the carbon content in the copper foil can be measured, for example, by using a carbon / sulfur analyzer EMIA-810W (manufactured by Horiba Seisakusho) in an oxygen stream combustion (tubular electric furnace method) -infrared absorption method. .
- the ten-point average roughness (Rz) of the electrolytic copper foil is 1.8 ⁇ m or less.
- the 10-point average roughness (Rz) of the electrolytic copper foil was set to 1.8 ⁇ m or less.
- the ten-point average roughness (Rz) of the electrolytic copper foil was measured according to JIS B0601: 1994.
- the electrolytic copper foil of the present invention satisfies the following characteristics in tensile properties when measured at room temperature after heating at 150 ° C. for 1 hour.
- the tensile strength of the copper foil is 400 MPa or more
- the elongation in the width direction (TD) of the copper foil is 2% or more
- the difference between the elongation in the longitudinal direction (MD) of the copper foil and the elongation in the width direction (TD) It is necessary to satisfy that the elongation anisotropy ⁇ [(MD elongation ⁇ TD elongation) / MD elongation] ⁇ 100 ⁇ , which is a parameter representing the value, is 50% or less.
- Patent Document 5 Conventional general electrolytic copper foils have few demands for high strength and high heat resistance, and high purity electrolytic copper foil (for example, Patent Document 5) that does not use an additive or for smoothing.
- an electrolytic copper foil for example, NC-WS manufactured by Furukawa Electric Co., Ltd.
- the additive is not so much incorporated into the copper foil during the electrodeposition process is added.
- the demand for electrolytic copper foil with high strength and high heat resistance has increased with the increase in capacity, size, and weight of batteries. Therefore, the additive species incorporated into the foil during the electrodeposition process are actively used. Increasing cases (for example, Patent Documents 1 to 4).
- the inventors have produced electrolytic copper foil using various additives on the premise that it has high strength and high heat resistance suitable for battery use or printed wiring board use, and Si-based active material is applied to the negative electrode.
- the copper foil wrinkle after charge / discharge was only improved by improving the properties that were required in the past, such as strength, elongation, and heat resistance. It turns out that it cannot suppress enough. Therefore, as a result of diligent studies for further suppression of wrinkles, it was found that elongation anisotropy becomes obvious in electrolytic copper foil with high strength and high heat resistance, and wrinkles are reduced by reducing the anisotropy of elongation. It was found that it can be effectively suppressed.
- the elongation anisotropy will be described.
- Elongation anisotropy refers to the property that the elongation value varies depending on the tensile direction in the tensile test.
- the present inventors investigated the anisotropy of elongation in a plurality of electrolytic copper foils having high strength and high heat resistance, and found that the elongation value when the copper foil was pulled in the longitudinal direction (MD direction) was the most. It was found that the elongation value was the smallest when the copper foil was pulled in the width direction (TD direction).
- the elongation anisotropy which is a parameter representing the difference between the elongation in the longitudinal direction (MD) of the copper foil and the width direction (TD) is ⁇ [(MD elongation ⁇ TD elongation) / MD elongation] ⁇ 100 ⁇ was calculated and evaluated.
- MD longitudinal direction
- TD width direction
- the electrolytic copper foil of the present invention has a high strength by suppressing the tensile strength when measured at room temperature after heating at 150 ° C. for 1 hour, and maintaining the tensile strength at 400 MPa or higher or lower than 400 MPa.
- the heat resistance is high
- the elongation in the width direction (TD) of the copper foil is 2% or more
- the elongation anisotropy of the copper foil is 50% or less, preferably 30% or less. This is because if the tensile strength after heating is less than 400 MPa, the strength of the thinned copper foil is insufficient and the foil breaks easily.
- the foil is likely to break. Furthermore, if the elongation anisotropy of the copper foil after heating exceeds 50%, the uniform deformation region and the non-uniform deformation region coexist, resulting in local strain bias, and the copper foil tends to wrinkle. It is.
- the electrolytic copper foil of the present invention has high strength and high heat resistance by suppressing that the tensile properties measured at room temperature after heating at 150 ° C. for 1 hour are maintained or lowered at a tensile strength of 400 MPa or more.
- the elongation in the width direction (TD) of the copper foil was 2% or more, and the elongation anisotropy of the copper foil was 50% or less.
- the tensile strength (initial strength) measured at room temperature before the heating is preferably in the range of 400 to 900 MPa. If the tensile strength is less than 400 MPa, the initial strength is insufficient, the tensile strength when measured at room temperature after heating at 150 ° C. can not be more than 400 MPa, the foil tends to break, In addition, if the tensile strength exceeds 900 MPa, the elongation is insufficient, and the elongation in the width direction (TD) of the copper foil when measured at room temperature after heating at 150 ° C. cannot be 2% or more. This is because cutting tends to occur easily.
- the electrolytic copper foil used for the formation of printed wiring boards is particularly rough plating as a post-treatment of the manufactured electrolytic copper foil (raw foil) for the purpose of ensuring adhesion with the resin constituting the printed wiring board.
- roughening is performed.
- Roughening plating generally forms granular copper particles on the order of 0.1 to 1 ⁇ m on the surface of electrolytic copper foil by electrolysis at a high current density in a sulfuric acid-copper sulfate plating solution for a relatively short time.
- the electrolytic copper foil of the present invention has a great feature in tensile properties when measured in a state of an untreated electrolytic copper foil (raw foil) in which no roughening treatment layer is formed on either side.
- the electrolytic copper foil does not include a roughening treatment layer by roughening plating.
- the tensile test was measured according to the IPC standard (IPC-TM-650). After measuring 10 times for each sample, values obtained by averaging their tensile strength and elongation were adopted as numerical values for strength and elongation. In addition, the numerical value of the tensile strength was not significant because no significant anisotropy was confirmed between the test piece cut out along the longitudinal direction of the copper foil and the test piece cut out along the width direction of the copper foil. In the invention, the tensile strength was measured with a test piece cut out along the longitudinal direction of the copper foil, and the tensile test speed was 50 mm / min.
- the electrolytic solution during the production of the electrolytic copper foil is The effect of the additive is somewhat different due to the fact that the copper foil flows at a high speed in the longitudinal direction of the copper foil, and it is assumed that the elongation anisotropy of the copper foil is expressed.
- FIG. 2 is a schematic view showing a main part of a typical production apparatus 1 used for producing the electrolytic copper foil M of the present invention, and an electrolytic cell 3 filled with an electrolytic solution 2 and a cylindrical surface.
- the cathode drum 4 is mainly composed of a cathode drum 4 having an anode and an anode 5 positioned opposite to the cathode drum 4.
- As the electrolytic solution 2 a sulfuric acid-copper sulfate aqueous solution is preferably used.
- the anode 5 is preferably an insoluble anode made of titanium coated with a white metal element or its oxide element.
- the electrolytic copper foil M rotates the cathode drum 4 at a constant speed in a state where the electrolytic solution 2 is filled between the insoluble anode 5 and the titanium cathode drum 4 provided to face the anode 5. Then, copper was deposited on the cathode drum surface 4 by applying a direct current between the electrodes 4 and 5, and the deposited copper was peeled off from the surface of the cathode drum 4 to form an electrolytic copper foil M.
- the electrolytic copper foil is manufactured by winding it with a winding roll 6.
- the flow rate direction of the electrolytic solution 2 flows from the distributor 7 to the overflow portions 8 provided on both upper sides of the electrolytic cell 3. It is a direction which goes to the same direction as the longitudinal direction of the copper foil formed on the surface of the cathode drum 4.
- the flow rate of the electrolyte 2 can be changed as appropriate depending on the pump output or the like, but so-called burnt plating occurs when it is manufactured under electrolysis conditions that are higher than the limit current density. It is necessary to appropriately adjust the electrolytic bath composition, bath temperature, current density, etc. so that the electrolysis conditions are lower than the density. Suitable electrolysis conditions for producing the electrolytic copper foil of the present invention are shown below.
- an additive In order to obtain an electrolytic copper foil having high strength and high heat resistance, it is essential to add an additive to the electrolytic solution.
- As a method for selecting the additive it is possible to appropriately select and use an effect of adsorbing on the copper surface and making the crystal grains fine and a heat resistance effect incorporated into the grains.
- there are no particular problems with the use of a plurality of additives it is preferable to use as few as possible in view of economy, production stability, and ease of concentration control.
- additives having the above-mentioned effects it is generally known that those having a functional group having an unshared electron pair such as S, N, and O are effective. In this example, S, N, and O are also effective.
- the additive for example, it is preferable to use, for example, polyethylene glycol (PEG), hydroxyethyl cellulose (HEC), thiourea and the like.
- the copper concentration and bath temperature are greatly increased, and the current density is decreased, so that the current density is less than the limit current density even at an extremely low flow rate, ideally even without stirring. It was devised to satisfy the electrolytic conditions.
- the flow rate of the electrolyte in the electrolytic cell was measured between the distributor 7 and the overflow part 8 of the electrolytic cell in a state before electrolysis using a small micro flow meter CM-1SX type (manufactured by Toho Denki Co., Ltd.). Measurement was performed with an anemometer attached at the position.
- the electrolytic copper foil of this invention can be manufactured by the method mentioned above.
- the electrolytic copper foil of the present invention is used for, for example, a lithium ion secondary battery provided with a negative electrode for a lithium ion secondary battery having a current collector, the foil capacity and wrinkle at the time of charging / discharging are prevented, the battery capacity, Cycle characteristics and safety can be improved. Furthermore, if the electrolytic copper foil of this invention is used for the printed wiring board formed by laminating
- Examples 1 to 7 and Comparative Examples 1 to 8 use the electrolytic copper foil manufacturing apparatus shown in FIG. 2 and between the insoluble anode 5 and the titanium cathode drum 4 provided to face the anode 5.
- copper is deposited on the cathode drum surface 4 by applying a direct current between the electrodes 4 and 5 while rotating the cathode drum 4 at a constant speed. It peeled off from the surface of the drum 4, and produced the electrolytic copper foil M of thickness 8 micrometers.
- Table 1 shows the electrolytic bath composition, additive type and amount, bath temperature, current density, and electrolytic flow rate.
- the reason why the flow rate is 0.02 m / s, not stirring, is to prevent concentration fluctuations due to stagnation of the bath during continuous foil production.
- the cathode drum 4 has a roughness Rz when measured in a direction perpendicular to the polishing direction (buffing direction) to the same value as the roughness Rz of the electrolytic copper foil (S surface) shown in Table 2. Until the surface was polished with a buff.
- Comparative Examples 9 to 13 electrolytic copper foils M having a thickness of 8 ⁇ m were prepared according to the conditions corresponding to those in Example 1 of Patent Documents 1 to 5, respectively. Since the flow rate was not particularly described, in Comparative Examples 9 to 13, the flow rate of the electrolytic solution was set to 0.5 m / s, which is a general flow rate condition range of the conventional electrolytic copper foil. Further, the cathode drum 4 has a roughness Rz when measured in a direction perpendicular to the polishing direction (buffing direction) to the same value as the roughness Rz of the electrolytic copper foil (S surface) shown in Table 2. Until the surface was polished with a buff.
- Comparative Example 14 Widely used as a copper foil for lithium ion secondary batteries. Although the additive is added to the electrolyte for smoothing, it is an electrolytic copper foil in which the additive is not taken into the copper foil during the electrodeposition process. “NC-WS” manufactured by Furukawa Electric Co., Ltd. was used.
- ⁇ Evaluation method> 1 Measurement of carbon content in copper foil The amount of carbon contained in copper foil was measured using a carbon / sulfur analyzer EMIA-810W (manufactured by Horiba Seisakusho) to burn a sample of about 0.5 g and burning in an oxygen stream ( Tubular electric furnace method)-measured by infrared absorption method. Table 2 shows the measured carbon content.
- the copper foil was handled with great care so as not to contaminate the surface, and pretreated such as acetone degreasing as necessary.
- the 10-point average roughness Rz was measured according to JIS B0601: 1994.
- the active material slurry was applied to both sides of a strip-shaped electrolytic copper foil (longitudinal direction parallel to the copper foil MD direction) having a thickness of 8 ⁇ m produced under the above conditions, and then dried, and this dried surface-treated electrolytic copper foil was heated at 150 ° C. for 1 hour and then compression molded with a roller press so that the film thickness of the molded negative electrode mixture was 120 ⁇ m on both sides to obtain a negative electrode for a lithium secondary battery.
- this slurry is uniformly applied to both surfaces of a positive electrode current collector made of a strip-shaped aluminum having a thickness of 20 ⁇ m, dried and compressed by a roller press so that the thickness of the positive electrode mixture after molding is 95 ⁇ m on both surfaces. It shape
- a lithium ion secondary battery was produced as a kind of nonaqueous electrolyte secondary battery.
- the positive electrode and negative electrode produced as described above and a separator made of a microporous polypropylene film were laminated to obtain a laminated electrode body.
- This laminated electrode body was wound many times in a spiral shape with the negative electrode inside along its length direction, and the final end of the separator was fixed to the outermost periphery with a tape to form a spiral electrode body.
- the prepared spiral electrode body is housed in a nickel-plated iron battery can with insulating plates on both upper and lower surfaces, and an aluminum positive electrode lead is used to collect the positive and negative electrodes.
- a negative electrode lead made of nickel was derived from the negative electrode current collector and connected to the battery can.
- a non-aqueous electrolyte solution in which LiPF6 was dissolved at a rate of 1 mol / L in an equal volume mixed solvent of propylene carbonate and diethyl carbonate was poured into a battery can containing the spiral electrode body.
- the battery can was caulked through an insulating sealing gasket whose surface was coated with asphalt to fix the battery lid, and the airtightness in the battery can was maintained.
- a cylindrical lithium secondary battery having a diameter of 18 mm and a height of 65 mm was produced.
- the battery in this lithium ion secondary battery was evaluated at a temperature of 25 ° C. by the following method.
- the surface-treated copper foil which gave the antirust process on the chromate conditions shown below to the electrolytic copper foil manufactured on the said conditions was used as a tension test, roughness measurement, a gas analysis, and a battery evaluation sample.
- the amount of carbon contained in the copper foil is 0.0015 to 0.018% by mass, which is an appropriate range of the present invention (0.001 to 0.020% by mass), and Rz is 1.0 to 1.7 ⁇ m, the proper range of the present invention (1.8 ⁇ m or less), and the tensile properties when measured at room temperature after heating at 150 ° C. for 1 hour, that is, the tensile strength is 420 to 653 MPa.
- the range (400 MPa or more), the width direction elongation (TD) value is 2.1 to 6.1%, which is an appropriate range of the present invention (2% or more), and the elongation anisotropy is 6.2 to 47.5%.
- Examples 1 to 4 had an elongation anisotropy of 30% or less, and wrinkles were not generated at all. There wasn't.
- Comparative Examples 1 to 4 the elongation anisotropy is 57.1 to 63.9%, which exceeds the upper limit (50%) of the appropriate range of the present invention, and significant wrinkles are confirmed in the copper foil after the charge / discharge test. It was done.
- Comparative Examples 3 and 4 have a copper foil widthwise elongation (TD) value of 1.3 to 1.8%, which is smaller than the lower limit (2%) of the proper range of the present invention, The foil breakage was also confirmed.
- the carbon content was 0.023% by mass, which is higher than the upper limit (0.02% by mass) of the appropriate range of the present invention, so that the copper foil after the charge / discharge test was confirmed to be broken.
- Comparative Example 6 the carbon content is less than 0.0008% by mass and the lower limit of the proper range of the present invention (0.001% by mass), so the tensile strength after heating at 150 ° C. is 370 MPa and the lower limit of the proper range of the present invention ( It was lower than 400 MPa), and it was remarkably softened by the heat treatment, and it was confirmed that the copper foil after the charge / discharge test was broken. Since Comparative Example 7 had a width direction (TD) elongation of the copper foil of 1.3%, which was smaller than the lower limit (2%) of the appropriate range of the present invention, the copper foil after the charge / discharge test was confirmed to be broken. .
- TD width direction
- carbon was contained at 0.001 to 0.020% by mass, the 10-point average roughness (Rz) of the electrolytic copper foil was 1.8 ⁇ m or less, and the electrolytic copper foil was measured at room temperature after heating at 150 ° C. for 1 hour.
- Tensile characteristics of the copper foil that is, the tensile strength of the copper foil is 400 MPa or more, the elongation in the width direction (TD) of the copper foil is 2% or more, and the elongation in the longitudinal direction (MD) of the copper foil and the width direction (
- fills the said characteristic is effective in suppression of wrinkles and foil breakage in the copper foil after a press.
- the strength and elongation anisotropy after heating are the characteristics of untreated electrolytic copper foil, and even if surface treatment such as rust prevention treatment or silane coupling treatment is applied, the above properties are affected. Absent.
- an electrolytic copper foil having high strength, high heat resistance, and low elongation anisotropy.
- the electrolytic copper foil of the present invention is used for, for example, a lithium ion secondary battery provided with a negative electrode for a lithium ion secondary battery having a current collector, the foil capacity and wrinkle at the time of charging / discharging are prevented, the battery capacity, Cycle characteristics and safety can be improved.
- the electrolytic copper foil of the present invention is used for a printed wiring board formed by laminating with an insulating film, foil breakage and wrinkle generation during pressing can be prevented, and dimensional stability can be improved.
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Abstract
Description
(1)炭素を0.001~0.020質量%含有する電解銅箔であって、該電解銅箔の十点平均粗さ(Rz)が1.8μm以下であり、前記電解銅箔を150℃で1時間加熱した後に常温で測定したときの引張特性は、前記銅箔の引張強度が400MPa以上、銅箔の幅方向(TD)の伸びが2%以上であり、かつ銅箔の長手方向(MD)の伸びと前記幅方向(TD)の伸びの差を表すパラメータである伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が50%以下であることを特徴とする電解銅箔。
(2)前記伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が30%以下である上記(1)に記載の電解銅箔。
(3)前記引張特性が、両面のいずれにも粗化処理層が形成されていない電解銅箔(原箔)の状態で得られる上記(1)または(2)に記載の電解銅箔。
(4)上記(1)~(3)のいずれか1項に記載の電解銅箔を集電体として有するリチウムイオン二次電池用負極電極。
(5)上記(1)~(3)のいずれか1項に記載の電解銅箔を集電体として有するリチウムイオン二次電池用負極電極を備えるリチウムイオン二次電池。
(6)上記(1)~(3)のいずれか1項に記載の電解銅箔と絶縁フィルムとを積層形成してなるプリント配線板。 Then, the present inventors diligently studied, found a method for solving the above-mentioned problems, and completed the present invention. That is, the gist of the present invention is as follows.
(1) An electrolytic copper foil containing 0.001 to 0.020% by mass of carbon, wherein the electrolytic copper foil has a ten-point average roughness (Rz) of 1.8 μm or less, and the electrolytic copper foil is heated at 150 ° C. for 1 hour. Tensile properties when measured at room temperature after that, the tensile strength of the copper foil is 400 MPa or more, the elongation in the width direction (TD) of the copper foil is 2% or more, and the elongation in the longitudinal direction (MD) of the copper foil And an elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100} which is a parameter representing a difference in elongation in the width direction (TD) is 50% or less. .
(2) The electrolytic copper foil according to (1), wherein the elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100} is 30% or less.
(3) The electrolytic copper foil according to (1) or (2), wherein the tensile properties are obtained in a state of an electrolytic copper foil (raw foil) in which a roughening treatment layer is not formed on either side.
(4) A negative electrode for a lithium ion secondary battery comprising the electrolytic copper foil according to any one of (1) to (3) as a current collector.
(5) A lithium ion secondary battery comprising a negative electrode for a lithium ion secondary battery having the electrolytic copper foil according to any one of (1) to (3) as a current collector.
(6) A printed wiring board formed by laminating the electrolytic copper foil according to any one of (1) to (3) above and an insulating film.
本発明の電解銅箔は、炭素を0.001~0.020質量%含有する電解銅箔であって、該電解銅箔の十点平均粗さ(Rz)が1.8μm以下であり、前記電解銅箔を150℃で1時間加熱した後に常温(20℃±15℃)で測定したときの引張特性は、前記銅箔の引張強度が400MPa以上、銅箔の幅方向(TD)の伸びが2%以上であり、かつ銅箔の長手方向(MD)の伸びと前記幅方向(TD)の伸びの差を表すパラメータである伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が50%以下であることを特徴とする電解銅箔である。 Next, embodiments of the present invention will be described below.
The electrolytic copper foil of the present invention is an electrolytic copper foil containing 0.001 to 0.020 mass% of carbon, and the electrolytic copper foil has a ten-point average roughness (Rz) of 1.8 μm or less. Tensile properties when heated at room temperature for 1 hour and then measured at room temperature (20 ° C ± 15 ° C) are as follows: The tensile strength of the copper foil is 400 MPa or more and the elongation in the width direction (TD) of the copper foil is 2% or more. The elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100} which is a parameter representing the difference between the elongation in the longitudinal direction (MD) of the copper foil and the elongation in the width direction (TD) is 50. % Of the electrolytic copper foil.
本発明では、電解銅箔中の炭素(C)含有量を0.001~0.020質量%とすることが必要である。炭素含有量が0.001質量%未満だと、十分な強度および耐熱性が得られず、また、炭素含有量が0.020質量%超えだと、延性が低下し、ハンドリング時、ないし充放電時に箔切れが生じやすいからである。このため、炭素含有量は0.001~0.020質量%とした。なお、銅箔中の炭素含有量の測定は、例えば炭素・硫黄分析装置EMIA-810W(堀場製作所製)を用いて、酸素気流中燃焼(管状電気炉方式)―赤外線吸収法で行うことができる。 <Carbon content in copper foil>
In the present invention, the carbon (C) content in the electrolytic copper foil needs to be 0.001 to 0.020 mass%. If the carbon content is less than 0.001% by mass, sufficient strength and heat resistance cannot be obtained, and if the carbon content exceeds 0.020% by mass, the ductility decreases and the foil breaks during handling or charge / discharge. It is easy to occur. Therefore, the carbon content is set to 0.001 to 0.020% by mass. The carbon content in the copper foil can be measured, for example, by using a carbon / sulfur analyzer EMIA-810W (manufactured by Horiba Seisakusho) in an oxygen stream combustion (tubular electric furnace method) -infrared absorption method. .
また、本発明では、電解銅箔の十点平均粗さ(Rz)が1.8μm以下であることが必要である。前記十点平均粗さ(Rz)が1.8μm超えだと、電解銅箔の表面凹凸に起因した伸び異方性が大きくなって顕在化し、充放電試験後の銅箔には、シワが顕著に発生しやすくなるからである。このため、電解銅箔の十点平均粗さ(Rz)は1.8μm以下とした。なお、電解銅箔の十点平均粗さ(Rz)の測定は、JIS B0601:1994に準じて行なった。また、測定面は、粗化処理層が形成されていない未処理の電解銅箔(原箔)のS面(陰極(Ti)ドラム側の表面)とし、測定方向は、バフスジ方向(=MD方向)に対し垂直な方向(=TD方向)とした。 <10-point average roughness of copper foil surface (Rz)>
In the present invention, it is necessary that the ten-point average roughness (Rz) of the electrolytic copper foil is 1.8 μm or less. When the ten-point average roughness (Rz) exceeds 1.8 μm, the elongation anisotropy due to the surface unevenness of the electrolytic copper foil becomes large and becomes apparent, and the copper foil after the charge / discharge test is noticeably wrinkled. This is because it tends to occur. For this reason, the 10-point average roughness (Rz) of the electrolytic copper foil was set to 1.8 μm or less. The ten-point average roughness (Rz) of the electrolytic copper foil was measured according to JIS B0601: 1994. The measurement surface is the S surface (surface on the cathode (Ti) drum side) of the untreated electrolytic copper foil (raw foil) on which the roughened layer is not formed, and the measurement direction is the buffing direction (= MD direction) ) Direction (= TD direction).
さらに、本発明の電解銅箔は、150℃で1時間加熱した後に常温で測定したときの引張特性が、以下の各特性を満足するものである。すなわち、銅箔の引張強度が400MPa以上、銅箔の幅方向(TD)の伸びが2%以上であり、かつ銅箔の長手方向(MD)の伸びと前記幅方向(TD)の伸びの差を表すパラメータである伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が50%以下であることを満足することが必要である。 <Tensile property of copper foil when measured at room temperature after heating at 150 ° C for 1 hour>
Furthermore, the electrolytic copper foil of the present invention satisfies the following characteristics in tensile properties when measured at room temperature after heating at 150 ° C. for 1 hour. That is, the tensile strength of the copper foil is 400 MPa or more, the elongation in the width direction (TD) of the copper foil is 2% or more, and the difference between the elongation in the longitudinal direction (MD) of the copper foil and the elongation in the width direction (TD) It is necessary to satisfy that the elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100}, which is a parameter representing the value, is 50% or less.
詳細なメカニズムは明らかでないが、それら複数の要因により、粗化めっき層を備えた電解銅箔は、粗化めっき層を備えない電解銅箔(原箔)に比較して、伸び異方性が見かけ上大きく見えたり、または小さく見えたりすることがある。そのため、本発明の電解銅箔は、上述した引張特性を正確に測定(評価)する際には、粗化めっきによる粗化処理層を備えていないことが好ましい。 In addition, the electrolytic copper foil used for the formation of printed wiring boards is particularly rough plating as a post-treatment of the manufactured electrolytic copper foil (raw foil) for the purpose of ensuring adhesion with the resin constituting the printed wiring board. In many cases, roughening is performed. Roughening plating generally forms granular copper particles on the order of 0.1 to 1 μm on the surface of electrolytic copper foil by electrolysis at a high current density in a sulfuric acid-copper sulfate plating solution for a relatively short time. To do. On the other hand, the electrolytic copper foil of the present invention has a great feature in tensile properties when measured in a state of an untreated electrolytic copper foil (raw foil) in which no roughening treatment layer is formed on either side. is there. Although depending on the thickness of the rough plating layer, generally, the rough plating layer is present on the surface of the electrolytic copper foil, so that the unevenness on the surface of the electrolytic copper foil becomes coarse. Moreover, generally the electrolysis conditions of roughening plating differ greatly from the electrolysis conditions which manufacture untreated electrolytic copper foil (raw foil). Therefore, the crystal structure and structure of the copper particles formed by the rough plating are different from the crystal structure and structure of the untreated electrolytic copper foil (original foil).
Although the detailed mechanism is not clear, due to these multiple factors, the electrolytic copper foil with the roughened plating layer has an elongation anisotropy compared to the electrolytic copper foil (raw foil) without the roughened plated layer. It may appear larger or smaller in appearance. Therefore, when the electrolytic copper foil of the present invention accurately measures (evaluates) the above-described tensile properties, it is preferable that the electrolytic copper foil does not include a roughening treatment layer by roughening plating.
本発明者らは、伸び異方性の低減方法について鋭意検討を行なった結果、銅電析中の電解液の流速を低減すること、理想的には無攪拌状態で製箔することで伸び異方性が大幅に低減されることを見出した。そのメカニズムについて各種解析を実施したが、伸び異方性の有無による金属組織上の明確な差異は確認されておらず、メカニズム解明には至っていない。しかしながら、伸び異方性は、従来箔のような添加剤の取り込みがほとんどない電解銅箔においては確認されず、高強度・高耐熱性を有する電解銅箔特有の現象と考えられる(図1参照)。添加剤成分の吸着及びその後の銅箔中への添加剤成分の取り込みについては、電解液の流速の影響を受けることは一般的に知られていることから、電解銅箔製造時の電解液が、銅箔長手方向に対して速い速度で流れていることに起因して、添加剤の効果が何らか異なり、銅箔の伸びの異方性が発現されたものと推察している。 [Method for producing electrolytic copper foil]
As a result of intensive investigations on methods for reducing elongation anisotropy, the inventors have reduced the flow rate of the electrolyte during copper electrodeposition, ideally by making the foil in an unstirred state. It was found that the directionality is greatly reduced. Although various analyzes have been conducted on the mechanism, no clear difference in the metal structure due to the presence or absence of elongation anisotropy has been confirmed, and the mechanism has not yet been elucidated. However, the elongation anisotropy is not confirmed in an electrolytic copper foil that hardly incorporates an additive such as a conventional foil, and is considered to be a phenomenon peculiar to an electrolytic copper foil having high strength and high heat resistance (see FIG. 1). ). Since it is generally known that the adsorption of the additive component and the subsequent incorporation of the additive component into the copper foil are affected by the flow rate of the electrolytic solution, the electrolytic solution during the production of the electrolytic copper foil is The effect of the additive is somewhat different due to the fact that the copper foil flows at a high speed in the longitudinal direction of the copper foil, and it is assumed that the elongation anisotropy of the copper foil is expressed.
図2は、本発明の電解銅箔Mを製造するために用いられる代表的な製造装置1の要部を示す概略図であって、電解液2を充填した電解槽3と、円筒状の表面をもつ陰極ドラム4と、この陰極ドラム4に対向して位置する陽極5とで主に構成されている。電解液2は、硫酸-硫酸銅水溶液を用いることが好ましい。陽極5は、白金属元素又はその酸化物元素で被覆したチタンからなる不溶性陽極を用いることが好ましい。 Next, the example of the typical manufacturing method of the electrolytic copper foil according to this invention is demonstrated below.
FIG. 2 is a schematic view showing a main part of a typical production apparatus 1 used for producing the electrolytic copper foil M of the present invention, and an
硫酸濃度: 30~100 g/L
塩素濃度: 60~140 mg/L
添加剤濃度:2~20mg/L
浴温 : 65~80℃
電流密度: 10~35A/dm2
流速 : 0.02~0.05m/s Copper concentration: 120-155 g / L
Sulfuric acid concentration: 30-100 g / L
Chlorine concentration: 60-140 mg / L
Additive concentration: 2-20mg / L
Bath temperature: 65-80 ℃
Current density: 10-35A / dm 2
Flow rate: 0.02 to 0.05m / s
実施例1~7および比較例1~8は、図2に示す電解銅箔の製造装置を用い、不溶性陽極5と、この陽極5に対向させて設けられたチタン製の陰極ドラム4との間に電解液2を満たした状態で、陰極ドラム4を 一定速度で回転させながら、両極4、5間に直流電流を通電することにより陰極ドラム表面4上に銅を析出させ、析出した銅を陰極ドラム4の表面から引き剥がして、厚さ8μmの電解銅箔Mを作製した。電解液の浴組成、添加剤の種類及び添加量、浴温、電流密度並びに電解液の流速を表1に示す。尚、実施例1~5および7において、無攪拌ではなく、流速を0.02m/sとしている理由は、連続製箔時にて浴の滞留による濃度変動を防止するためである。また、陰極ドラム4は、研磨方向(バフスジ方向)に対し垂直な方向に測定したときの粗さRzが、表2に示す電解銅箔(S面)の粗さRzの数値と同等程度になるまで、バフにて表面を研磨した。 (Examples 1 to 7 and Comparative Examples 1 to 8)
Examples 1 to 7 and Comparative Examples 1 to 8 use the electrolytic copper foil manufacturing apparatus shown in FIG. 2 and between the insoluble anode 5 and the
比較例9~13は、それぞれ特許文献1~5の実施例1に相当する条件に従って、厚さ8μmの電解銅箔Mを作製した。なお、流速については特に記載がなかったため、比較例9~13はいずれも、電解液の流速を、従来の電解銅箔の一般的な流速条件範囲である0.5m/sとした。また、陰極ドラム4は、研磨方向(バフスジ方向)に対し垂直な方向に測定したときの粗さRzが、表2に示す電解銅箔(S面)の粗さRzの数値と同等程度になるまで、バフにて表面を研磨した。 (Comparative Examples 9 to 13)
In Comparative Examples 9 to 13, electrolytic copper foils M having a thickness of 8 μm were prepared according to the conditions corresponding to those in Example 1 of Patent Documents 1 to 5, respectively. Since the flow rate was not particularly described, in Comparative Examples 9 to 13, the flow rate of the electrolytic solution was set to 0.5 m / s, which is a general flow rate condition range of the conventional electrolytic copper foil. Further, the
リチウムイオン二次電池用銅箔として広く用いられており、平滑化のために添加剤は電解液中に加えるものの、電析過程で銅箔中に添加剤がさほど取り込まれない電解銅箔である古河電気工業株式会社製の「NC-WS」を使用した。 (Comparative Example 14)
Widely used as a copper foil for lithium ion secondary batteries. Although the additive is added to the electrolyte for smoothing, it is an electrolytic copper foil in which the additive is not taken into the copper foil during the electrodeposition process. “NC-WS” manufactured by Furukawa Electric Co., Ltd. was used.
1.銅箔中の炭素含有量の測定
銅箔中に含有する炭素量は、炭素・硫黄分析装置EMIA-810W(堀場製作所製)を用い、0.5g程度のサンプルを燃焼させ、酸素気流中燃焼(管状電気炉方式)―赤外線吸収法で測定を行った。測定した炭素含有量を表2に示す。なお、測定する際には、銅箔は表面が汚染されないよう十分に注意して取扱い、必要に応じてアセトン脱脂等の前処理を行った。 <Evaluation method>
1. Measurement of carbon content in copper foil The amount of carbon contained in copper foil was measured using a carbon / sulfur analyzer EMIA-810W (manufactured by Horiba Seisakusho) to burn a sample of about 0.5 g and burning in an oxygen stream ( Tubular electric furnace method)-measured by infrared absorption method. Table 2 shows the measured carbon content. When measuring, the copper foil was handled with great care so as not to contaminate the surface, and pretreated such as acetone degreasing as necessary.
十点平均粗さRzは、JIS B0601:1994に準じて測定した。測定面は、銅箔のS面(陰極ドラム側の銅箔表面)、測定方向は、バフスジ方向(=MD方向)に対し垂直な方向(=TD方向)とした。 2. Measurement of 10-point average roughness Rz of copper foil surface The 10-point average roughness Rz was measured according to JIS B0601: 1994. The measurement surface was the S surface of the copper foil (the copper foil surface on the cathode drum side), and the measurement direction was the direction (= TD direction) perpendicular to the buffing direction (= MD direction).
(1)リチウム二次電池用負極電極の作製
カーボン系活物質(シリコン系合金活物質を20質量%含む。)と、アセチレンブラックとが、8:1の質量比になるようにボールミルを用いて粉砕混合し、負極材料を作製した。この負極材料を80質量%、結着剤としてポリフッ化ビニリデン(PVDF)を20質量%の割合で混合して負極合剤を調製し、この負極合剤をN-メチルピロリドン(溶剤)に分散させて活物質スラリーとした。次いで、上記の条件で作製した厚さ8μmの帯状(長手方向が銅箔MD方向に平行)の電解銅箔の両面に活物質スラリーを塗布した後、乾燥し、この乾燥した表面処理電解銅箔を150℃で1時間加熱した後、成形後の負極合剤の膜厚が両面共に120μmとなるようにローラープレス機で圧縮成形し、リチウム二次電池用負極電極を得た。 3. Battery performance test (1) Production of negative electrode for lithium secondary battery Ball mill so that carbon-based active material (containing 20% by mass of silicon-based alloy active material) and acetylene black are in a mass ratio of 8: 1. Was used for pulverization and mixing to prepare a negative electrode material. A negative electrode mixture was prepared by mixing 80% by mass of this negative electrode material and 20% by mass of polyvinylidene fluoride (PVDF) as a binder, and this negative electrode mixture was dispersed in N-methylpyrrolidone (solvent). Active material slurry. Next, the active material slurry was applied to both sides of a strip-shaped electrolytic copper foil (longitudinal direction parallel to the copper foil MD direction) having a thickness of 8 μm produced under the above conditions, and then dried, and this dried surface-treated electrolytic copper foil Was heated at 150 ° C. for 1 hour and then compression molded with a roller press so that the film thickness of the molded negative electrode mixture was 120 μm on both sides to obtain a negative electrode for a lithium secondary battery.
炭酸リチウム0.5モルと炭酸コバルト1モルとを混合し、空気中で900℃、5時間焼成して正極活物質(LiCoO2)とした。この正極活物質(LiCoO2)を91質量%、導電剤としてグラファイトを6質量%、結着剤としてPVDFを3質量%の割合で混合して正極合材を作製し、これをN-メチル-2ピロリドン(NMP)に分散してスラリー状とした。次に、このスラリーを厚み20μmの帯状のアルミニウムからなる正極集電体の両面に均一に塗布し、成形後の正極合剤の膜厚が表面共に95μmとなるように乾燥後ローラープレス機で圧縮成形し、リチウム二次電池用正極電極を得た。 (2) Preparation of positive electrode for lithium secondary battery 0.5 mol of lithium carbonate and 1 mol of cobalt carbonate were mixed and fired in air at 900 ° C. for 5 hours to obtain a positive electrode active material (LiCoO 2 ). This positive electrode active material (LiCoO 2 ) was mixed at a ratio of 91% by mass, graphite as a conductive agent at 6% by mass, and PVDF as a binder at a rate of 3% by mass to produce a positive electrode mixture, which was mixed with N-methyl- Dispersed in 2 pyrrolidone (NMP) to form a slurry. Next, this slurry is uniformly applied to both surfaces of a positive electrode current collector made of a strip-shaped aluminum having a thickness of 20 μm, dried and compressed by a roller press so that the thickness of the positive electrode mixture after molding is 95 μm on both surfaces. It shape | molded and the positive electrode for lithium secondary batteries was obtained.
非水電解質二次電池の一種として、リチウムイオン二次電池を作製した。上記のようにして作製した正極電極および負極電極と、微多孔性ポリプロピレンフィルムよりなるセパレータとを積層し、積層電極体とした。この積層電極体は、その長さ方向に沿って負極を内側にして渦巻型に多数回巻回し、最外周にセパレータの最終端部をテープで固定し、渦巻式電極体とした。作製した渦巻式電極体を、その上下両面に絶縁板を設置した状態で、ニッケルメッキが施された鉄製の電池缶に収納し、正極及び負極の集電を行うために、アルミニウム製の正極リードを正極集電体から導出して電池蓋に接続し、ニッケル製の負極リードを負極集電体から導出して電池缶に接続した。 (3) Production of lithium ion secondary battery A lithium ion secondary battery was produced as a kind of nonaqueous electrolyte secondary battery. The positive electrode and negative electrode produced as described above and a separator made of a microporous polypropylene film were laminated to obtain a laminated electrode body. This laminated electrode body was wound many times in a spiral shape with the negative electrode inside along its length direction, and the final end of the separator was fixed to the outermost periphery with a tape to form a spiral electrode body. The prepared spiral electrode body is housed in a nickel-plated iron battery can with insulating plates on both upper and lower surfaces, and an aluminum positive electrode lead is used to collect the positive and negative electrodes. Was extracted from the positive electrode current collector and connected to the battery lid, and a negative electrode lead made of nickel was derived from the negative electrode current collector and connected to the battery can.
充電:1C相当電流で定電流充電し、4.2Vに到達後、定電圧充電に切り換え、充電電流が0.05C相当に低下した時点で終了した。
放電:1C相当電流で定電流放電し、3.0Vになった時点で終了した。
なお、CはCレートであり、電池の全容量を1時間で放電させる電流量をいう。 (Conditions for charge / discharge test)
Charging: Constant current charging at a current equivalent to 1 C. After reaching 4.2 V, switching to constant voltage charging was completed when the charging current dropped to 0.05 C equivalent.
Discharge: A constant current was discharged at a current equivalent to 1 C, and was terminated when the voltage reached 3.0V.
C is a C rate, which means the amount of current that discharges the entire capacity of the battery in one hour.
充放電後の箔切れの評価は、上記条件にて1000サイクルまで充放電を繰り返し、サイクル試験終了後に電池を解体し、目視にて銅箔のシワ及び箔切れの有無を確認した。表2中のシワ及び箔切れの評価は、シワおよび箔切れが全く存在しない場合を「◎」とし、シワがわずかに発生している場合を「○」、そして、顕著なシワが発生している場合を「シワ」、箔切れが発生している場合を「箔切れ」、顕著なシワと箔切れが両方発生している場合を「シワ、箔切れ」と示す。 (Evaluation of wrinkles and foil breaks after charge / discharge)
Evaluation of the foil breakage after charging / discharging was repeated up to 1000 cycles under the above conditions, the battery was disassembled after the end of the cycle test, and the presence or absence of copper foil wrinkles and foil breakage was visually confirmed. The evaluation of wrinkles and foil breaks in Table 2 is “◎” when no wrinkles and foil breaks are present, “○” when slight wrinkles are generated, and significant wrinkles are generated. "Wrinkle" when the foil is cut, "Foil cut" when the foil is broken, and "Wrinkle, foil cut" when both the wrinkle and the foil are marked.
<クロメート処理条件>
重クロム酸カリウム1~10g/L
温度(℃) 25℃
浸漬処理時間 2~20秒
表2に評価結果を示す。 The surface-treated copper foil which gave the antirust process on the chromate conditions shown below to the electrolytic copper foil manufactured on the said conditions was used as a tension test, roughness measurement, a gas analysis, and a battery evaluation sample.
<Chromate treatment conditions>
Potassium dichromate 1-10g / L
Temperature (℃) 25 ℃
2 電解液
3 電解槽
4 陰極ドラム
5 陽極
6 巻取りロール
7 デストリビューター
8 オーバーフロー部 DESCRIPTION OF SYMBOLS 1 Electrolytic copper
Claims (6)
- 炭素を0.001~0.020質量%含有する電解銅箔であって、
該電解銅箔の十点平均粗さ(Rz)が1.8μm以下であり、
前記電解銅箔を150℃で1時間加熱した後に常温で測定したときの引張特性は、前記銅箔の引張強度が400MPa以上、銅箔の幅方向(TD)の伸びが2%以上であり、かつ銅箔の長手方向(MD)の伸びと前記幅方向(TD)の伸びの差を表すパラメータである伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が50%以下であることを特徴とする電解銅箔。 An electrolytic copper foil containing 0.001 to 0.020% by mass of carbon,
The electrolytic copper foil has a ten-point average roughness (Rz) of 1.8 μm or less,
Tensile properties when the electrolytic copper foil is heated at 150 ° C. for 1 hour and then measured at room temperature are as follows: the copper foil has a tensile strength of 400 MPa or more, and the copper foil has a width direction (TD) elongation of 2% or more. And the elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100} which is a parameter representing the difference between the elongation in the longitudinal direction (MD) of the copper foil and the elongation in the width direction (TD) is 50%. An electrolytic copper foil characterized by: - 前記伸び異方性{[(MD伸び-TD伸び)/MD伸び]×100}が30%以下である請求項1に記載の電解銅箔。 2. The electrolytic copper foil according to claim 1, wherein the elongation anisotropy {[(MD elongation−TD elongation) / MD elongation] × 100} is 30% or less.
- 前記引張特性が、両面のいずれにも粗化処理層が形成されていない電解銅箔(原箔)の状態で得られる請求項1または2に記載の電解銅箔。 The electrolytic copper foil according to claim 1 or 2, wherein the tensile properties are obtained in a state of an electrolytic copper foil (raw foil) in which a roughening treatment layer is not formed on either side.
- 請求項1~3のいずれか1項に記載の電解銅箔を集電体として有するリチウムイオン二次電池用負極電極。 A negative electrode for a lithium ion secondary battery comprising the electrolytic copper foil according to any one of claims 1 to 3 as a current collector.
- 請求項1~3のいずれか1項に記載の電解銅箔を集電体として有するリチウムイオン二次電池用負極電極を備えるリチウムイオン二次電池。 A lithium ion secondary battery comprising a negative electrode for a lithium ion secondary battery having the electrolytic copper foil according to any one of claims 1 to 3 as a current collector.
- 請求項1~3のいずれか1項に記載の電解銅箔と絶縁フィルムとを積層形成してなるプリント配線板。 A printed wiring board formed by laminating the electrolytic copper foil according to any one of claims 1 to 3 and an insulating film.
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US10781523B1 (en) | 2019-11-27 | 2020-09-22 | Chang Chun Petrochemicals Co., Ltd. | Electrolytic copper foil and electrode and lithium-ion battery comprising the same |
US10975487B1 (en) | 2019-12-09 | 2021-04-13 | Chang Chun Petrochemical Co., Ltd. | Electrolytic copper foil and electrode and copper-clad laminate comprising the same |
JP2021091949A (en) * | 2019-12-09 | 2021-06-17 | 長春石油化學股▲分▼有限公司 | Electrolytic copper foil, electrode including electrolytic copper foil, and copper-clad laminate including electrolytic copper foil |
Also Published As
Publication number | Publication date |
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TWI767910B (en) | 2022-06-21 |
KR102218889B1 (en) | 2021-02-22 |
CN108026653A (en) | 2018-05-11 |
TW201807260A (en) | 2018-03-01 |
KR20190003451A (en) | 2019-01-09 |
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