WO2024011536A1 - Copper composite current collector, preparation method therefor and application thereof - Google Patents
Copper composite current collector, preparation method therefor and application thereof Download PDFInfo
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- WO2024011536A1 WO2024011536A1 PCT/CN2022/105810 CN2022105810W WO2024011536A1 WO 2024011536 A1 WO2024011536 A1 WO 2024011536A1 CN 2022105810 W CN2022105810 W CN 2022105810W WO 2024011536 A1 WO2024011536 A1 WO 2024011536A1
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- C23C14/00—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
- C23C14/06—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the coating material
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- C23C14/00—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
- C23C14/22—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
- C23C14/24—Vacuum evaporation
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- C23C14/00—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
- C23C14/22—Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
- C23C14/56—Apparatus specially adapted for continuous coating; Arrangements for maintaining the vacuum, e.g. vacuum locks
- C23C14/562—Apparatus specially adapted for continuous coating; Arrangements for maintaining the vacuum, e.g. vacuum locks for coating elongated substrates
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- 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
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- H01M4/00—Electrodes
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- H01M4/04—Processes of manufacture in general
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- H01M4/0421—Methods of deposition of the material involving vapour deposition
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- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
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- H—ELECTRICITY
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- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
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- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
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- H01M4/66—Selection of materials
- H01M4/668—Composites of electroconductive material and synthetic resins
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- 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 the field of lithium-ion batteries, and specifically to a copper composite current collector and its preparation method and application.
- the surface of the copper metal layer on the surface of conventional copper composite current collectors is flat and very smooth.
- the surface roughness is low, the surface energy is low, and the specific surface area is also low.
- the following problems will occur: 1) The electrode slurry is prone to leakage, which reduces the product quality and limits the coating speed; 2) Due to the low specific surface area of the copper metal layer, the active material layer in the battery and the copper metal layer
- the bonding area is small, resulting in a low bonding force between the active material layer and the composite current collector in the battery, which is prone to powder falling off; at the same time, the small bonding area also leads to a conductive channel between the active material and the composite current collector. Small, increasing the interface resistance between the active material and the composite current collector copper metal layer interface.
- the present invention provides a preparation method of copper composite current collector, which includes the following steps:
- the polymer film is passed through a copper plating roller along the axial direction of the copper plating roller.
- the copper plating roller has a first temperature zone and a second temperature zone.
- the first temperature zone The temperature of the second temperature zone is 40°C to 50°C, and the temperature of the second temperature zone is 10°C to 20°C; and
- Metal copper is evaporated under vacuum conditions to plate copper metal layers on both sides of the polymer film.
- the lengths of the first temperature zone and the second temperature zone of the copper plating roller are independently 5 mm to 10 mm.
- the vacuum degree for evaporating the metallic copper is 10-4Pa to 10-5Pa, the temperature is 1600°C to 1800°C, and the concentration of copper vapor is maintained at 60mol/L to 80mol/L.
- the movement speed of the polymer film is 10 m/min to 100 m/min.
- the material of the polymer film is selected from the group consisting of a composite of an insulating polymer material and an inorganic non-conductive filler, a composite of an insulating polymer material and a conductive filler, an insulating polymer material or a conductive polymer.
- the insulating polymer material is selected from the group consisting of cellulose and its derivatives, starch and its derivatives, protein and its derivatives, polyvinyl alcohol and its cross-linked polymers, polyethylene glycol and its Cross-linked polymer, polyamide, polyterephthalate, polyimide, polyethylene, polypropylene, polystyrene, polyvinyl chloride, aramid, polyphenylenediamide, acrylonitrile-butan Diene-styrene copolymer, polyethylene terephthalate, polybutylene terephthalate, poly(p-phenylene terephthalamide), polypropylene, polyformaldehyde, epoxy resin, phenolic resin One or more of resin, polytetrafluoroethylene, polyvinylidene fluoride, silicone rubber and polycarbonate.
- the conductive polymer material is selected from doped polysulfide nitride and/or doped polyacetylene.
- the inorganic non-conductive filler is selected from one or more of ceramic materials, glass materials and ceramic composite materials.
- the conductive filler is selected from the group consisting of carbon black, carbon nanotubes, graphite, acetylene black, graphene, nickel, iron, copper, aluminum, alloys, nickel-coated graphite powder, and nickel-coated carbon fiber. one or more of them.
- the present invention also provides a copper composite current collector, which is prepared by the above-mentioned preparation method of a copper composite current collector.
- the copper composite current collector has at least one of the following properties:
- the present invention further provides a negative electrode, which includes the above-mentioned copper composite current collector and a negative electrode active material layer located on one or both sides of the copper composite current collector.
- the present invention provides a lithium ion battery, which includes the above-mentioned negative electrode.
- the present invention provides an electrical device that uses the above-mentioned lithium-ion battery as a power source.
- the preparation method of the above-mentioned copper composite current collector regulates the temperature of the copper plating roller so that it has different temperature zones, so that the copper metal layer can be plated on the surface of the polymer film at different speeds, thereby increasing the growth of copper crystals in the copper metal layer.
- the speed is different to form a hole structure on the surface of the copper metal layer.
- the formation of the pore structure increases the roughness and specific surface area of the copper composite current collector, thereby increasing the contact area between the active material and the copper composite current collector in the battery, increasing the coating amount of the active material, and reducing the internal temperature of the battery. resistance, improve battery capacity and energy density, and extend battery cycle life.
- Figure 1 is an SEM image of the copper composite current collector prepared in Example 1.
- the present invention provides a method for preparing a copper composite current collector.
- This method regulates the temperature of the copper plating roller so that it has different temperature zones, thereby increasing the plating speed of the copper metal layer on the surface of the polymer film.
- Different growth rates of copper crystals in the copper metal layer are different to form a hole structure on the surface of the copper metal layer.
- the formation of the pore structure increases the roughness and specific surface area of the copper composite current collector (at least an increase of 20% compared to traditional copper composite current collectors), thereby increasing the contact between the active material and the copper composite current collector in the battery. area, increases the coating amount of active materials (at least 5% increase compared to traditional copper composite current collectors), and can reduce the internal resistance of the battery, increase the battery capacity and energy density, and extend the cycle life of the battery.
- the present invention relates to a preparation method of a copper composite current collector, which includes the following steps:
- the above-mentioned polymer film is passed through a copper plating roller, wherein along the axial direction of the copper plating roller, the copper plating roller has a first temperature zone and a second temperature zone, and the temperature of the first temperature zone is 40 °C ⁇ 50°C, the temperature of the second temperature zone is 10°C ⁇ 20°C; and
- Metallic copper is evaporated under vacuum conditions to plate copper metal layers on both sides of the polymer film.
- the temperature of the first temperature zone can be any value between 40°C and 50°C, for example, it can also be 41°C, 42°C, 43°C, 44°C, 45°C, 46°C, or 47°C. , 48°C, 49°C.
- the temperature of the second temperature zone can be any value between 10°C and 20°C, for example, it can also be 11°C, 12°C, 13°C, 14°C, 15°C, 16°C, 17°C , 18°C, 19°C.
- the copper plating roller has a first temperature zone and a length of the second temperature zone that are independently any value between 5 mm and 10 mm, for example, they may also be 6 mm, 7 mm, 8 mm, or 9 mm.
- the vacuum degree of evaporating metallic copper can be 10 -4 Pa to 10 -5 Pa, the temperature can be 1600°C to 1800°C, and the concentration of copper vapor is maintained at 60 mol/L to 80 mol/L.
- the movement speed of the polymer film can be 10m/min ⁇ 100m/min, or can also be 20m/min, 30m/min, 40m/min, 50m/min, 60m/min, 70m/min, 80m/min, 90m/min.
- the copper metal layer has a purity of ⁇ 99.8%.
- the material of the polymer film is not limited, and any polymer material known in the art can be used, including, but not limited to, composites of insulating polymer materials and inorganic non-conductive fillers, insulating polymer materials and conductive fillers, insulating polymer materials or conductive polymer materials, wherein the mass percentage of insulating polymer materials in the composite formed of insulating polymer materials and inorganic non-conductive fillers is ⁇ 90%, insulating polymer materials and The mass percentage of the insulating polymer material in the composite formed by the conductive filler is ⁇ 90%.
- the insulating polymer material may be selected from cellulose and its derivatives, starch and its derivatives, proteins and its derivatives, polyvinyl alcohol and its cross-linked polymers, polyethylene glycol and its cross-linked Polymer, polyamide, polyterephthalate, polyimide, polyethylene, polypropylene, polystyrene, polyvinyl chloride, aramid, polyphenylenediamide, acrylonitrile-butadiene -Styrene copolymer, polyethylene terephthalate, polybutylene terephthalate, poly(p-phenylene terephthalamide), polypropylene, polyformaldehyde, epoxy resin, phenolic resin, One or more of polytetrafluoroethylene, polyvinylidene fluoride, silicone rubber and polycarbonate.
- the conductive polymer material may be selected from doped polysulfide nitride and/or doped polyacetylene.
- the inorganic non-conductive filler may be selected from one or more of ceramic materials, glass materials and ceramic composite materials.
- the conductive filler may be selected from the group consisting of carbon black, carbon nanotubes, graphite, acetylene black, graphene, nickel, iron, copper, aluminum, alloys, nickel-coated graphite powder, and nickel-coated carbon fiber. one or more.
- the alloy may include one or more of nickel, iron, copper and aluminum.
- a step of winding is further included;
- the winding tension may be 5N to 25N.
- the present invention also provides a copper composite current collector, which is prepared by the above-mentioned preparation method of a copper composite current collector.
- the copper composite current collector has at least one of the following properties:
- the specific surface area of the copper composite current collector can also be 25m 2 /g, 28m 2 /g, 30m 2 /g, 35m 2 /g, and the number of surface pores is >100/m 2 , for example, it can also be 150 pieces/m 2 , 200 pieces/m 2 , 300 pieces/m 2 , 400 pieces/m 2 , 500 pieces/m 2 .
- the thickness of the copper composite current collector may be 1.6 ⁇ m ⁇ 31 ⁇ m.
- the thickness of the polymer film may be 1 ⁇ m ⁇ 25 ⁇ m, and the thickness of the copper metal layer may be 0.3 ⁇ m ⁇ 3 ⁇ m. More preferably, the thickness of the polymer film is 2 ⁇ m to 8 ⁇ m. Regulating the thickness of the polymer film within this range can not only reduce the production cost of copper composite current collectors, but also avoid the problem of polymer film breakage during processing.
- the polymer film meets at least one of the following properties:
- the present invention further provides a negative electrode, which includes the above-mentioned copper composite current collector and a negative electrode active material layer located on one or both sides of the copper composite current collector.
- the material of the negative active material layer is not limited and can be composed of commonly used negative active materials, conductive agents, and negative binders; wherein the negative active material can be graphite, lithium titanate, or lithium,
- the negative electrode binder may be at least one of styrene-butadiene latex, acrylate, and sodium carboxymethyl cellulose, and the conductive agent may be at least one of carbon nanotubes and conductive carbon black.
- the present invention provides a lithium ion battery, which includes the above-mentioned negative electrode.
- a lithium-ion battery may also include a positive electrode and an electrolyte.
- the positive electrode includes a positive electrode current collector and a positive electrode active material layer located on the surface of the positive electrode current collector.
- the positive electrode current collector can be an aluminum current collector.
- the material of the positive electrode active material layer is not limited and can be made of commonly used positive electrode active materials, It is composed of conductive agent and positive electrode binder; among which, the positive electrode active material can be any positive electrode active material commonly used in this field, such as lithium cobalt oxide, lithium iron phosphate, NCA, NCM, lithium manganate, lithium nickelate, NCMA or cobalt-free Positive electrode; the positive electrode binder can be at least one of PVDF and acrylate, and the conductive agent can be at least one of carbon nanotubes and conductive carbon black;.
- the electrolyte can be a solid electrolyte, a semi-solid electrolyte or a liquid electrolyte, wherein the solid electrolyte and semi-solid electrolyte can be an oxide or sulfide electrolyte, and the solute in the liquid electrolyte can be lithium hexafluorophosphate.
- the above-mentioned lithium ion battery may further include a separator, wherein the separator may be any separator known in the art, such as a PE wet separator, a PP dry separator or a double-layer PE/PP coated separator.
- the separator may be any separator known in the art, such as a PE wet separator, a PP dry separator or a double-layer PE/PP coated separator.
- the shape of the lithium-ion battery is not limited, and may be cylindrical or square, for example.
- the present invention provides an electrical device that uses the above-mentioned lithium-ion battery as a power source.
- specific types of electrical devices include, but are not limited to, mobile terminals (mobile phones, mobile computers, etc.), smart wearables, power tools (electric drills, electric motors, etc.), electric vehicles, mobile power supplies, etc.
- a copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
- step 2) Evaporate copper metal with a purity of 99.9% in the evaporation boat at 1800°C, maintain the concentration of copper vapor at 70 mol/L, and evaporate a copper metal layer with a thickness of 1 ⁇ m on both sides of the BOPP film in step 1), where , During the evaporation process, the movement speed of the BOPP film is 30m/min.
- the BOPP film with a copper metal layer evaporated was then rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector.
- the measured surface morphology of the copper composite current collector is shown in Figure 1, and the measured related properties of the copper composite current collector are shown in Table 1.
- Positive electrode lithium iron phosphate
- Negative electrode composed of the copper composite current collector prepared in step 1 and a graphite layer located on the surface of the copper composite current collector;
- Electrolyte liquid electrolyte with lithium hexafluorophosphate as solute
- the preparation method of this embodiment is basically the same as that of Example 1, except that the temperature of the copper plating roller and the copper metal evaporation parameters are different. Specific steps are as follows:
- a copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
- step 2) Evaporate copper metal with a purity of 99.9% in the evaporation boat at 1600°C, maintain the concentration of copper vapor at 60 mol/L, and evaporate a copper metal layer with a thickness of 1 ⁇ m on both sides of the BOPP film in step 1), where , During the evaporation process, the movement speed of the BOPP film is 20m/min. The BOPP film with a copper metal layer evaporated was then rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector.
- the preparation method of this embodiment is basically the same as that of Example 1, except that the polymer film is a polyethylene terephthalate film, the thickness of the polymer film and the thickness of the copper metal layer are different, the temperature of the copper plating roller, Copper metal evaporation parameters are different. Specific steps are as follows:
- a copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a polyethylene terephthalate film. Specific steps are as follows:
- step 2) Evaporate the copper metal with a purity of 99.9% in the evaporation boat at 1800°C, and maintain the concentration of copper vapor at 80 mol/L to achieve the evaporation thickness on both sides of the polyethylene terephthalate film in step 1) It is a copper metal layer of 2 ⁇ m. During the evaporation process, the movement speed of the polyethylene terephthalate film is 80m/min. Then, the polyethylene terephthalate film evaporated with a copper metal layer was rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector.
- a copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
- Positive electrode lithium iron phosphate
- Negative electrode composed of the copper composite current collector prepared in step 1 and a graphite layer located on the surface of the copper composite current collector;
- Electrolyte liquid electrolyte with lithium hexafluorophosphate as solute
- the peeling force test, battery internal resistance test and charge and discharge cycle performance test refer to the national standard GB18287_2000, and the test results are shown in Table 2.
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Abstract
Description
本发明涉及锂离子电池领域,具体而言,涉及一种铜复合集流体及其制备方法和应用。The present invention relates to the field of lithium-ion batteries, and specifically to a copper composite current collector and its preparation method and application.
目前常规的铜复合集流体表面的铜金属层表面都是平整且非常光滑的,表面的粗糙度低、表面能低、比表面积也低,这就导致铜复合集流体在涂覆电极浆料时会出现以下几个问题:1)电极浆料比较容易出现漏涂,降低了产品品质且限制了涂布速度;2)由于铜金属层的比表面积低,电池内的活性物质层与铜金属层的粘接面积较小,导致电池内活性物质层与复合集流体的粘接力较低,易产生掉粉现象;同时,粘接面积小也导致了活性物质与复合集流体之间的导电通道小,增加了活性物质与复合集流体铜金属层界面之间的界面电阻。At present, the surface of the copper metal layer on the surface of conventional copper composite current collectors is flat and very smooth. The surface roughness is low, the surface energy is low, and the specific surface area is also low. This causes the copper composite current collector to have difficulty in coating electrode slurry. The following problems will occur: 1) The electrode slurry is prone to leakage, which reduces the product quality and limits the coating speed; 2) Due to the low specific surface area of the copper metal layer, the active material layer in the battery and the copper metal layer The bonding area is small, resulting in a low bonding force between the active material layer and the composite current collector in the battery, which is prone to powder falling off; at the same time, the small bonding area also leads to a conductive channel between the active material and the composite current collector. Small, increasing the interface resistance between the active material and the composite current collector copper metal layer interface.
发明内容Contents of the invention
基于此,有必要提供一种能够提高比表面积同时降低界面电阻的铜复合集流体及其制备方法和应用。Based on this, it is necessary to provide a copper composite current collector that can increase the specific surface area while reducing the interface resistance and its preparation method and application.
本发明一方面,提供一种铜复合集流体的制备方法,其包括以下步骤:On the one hand, the present invention provides a preparation method of copper composite current collector, which includes the following steps:
提供聚合物薄膜;Provide polymer films;
采用真空蒸镀技术,将所述聚合物薄膜穿过镀铜辊,沿所述镀铜辊的轴向,所述镀铜辊具有第一温区和第二温区,所述第一温区的温度为40℃~50℃,所述第二温区的温度为10℃~20℃;以及Using vacuum evaporation technology, the polymer film is passed through a copper plating roller along the axial direction of the copper plating roller. The copper plating roller has a first temperature zone and a second temperature zone. The first temperature zone The temperature of the second temperature zone is 40°C to 50°C, and the temperature of the second temperature zone is 10°C to 20°C; and
在真空条件下蒸发金属铜,以在所述聚合物薄膜的两面镀覆铜金属层。Metal copper is evaporated under vacuum conditions to plate copper metal layers on both sides of the polymer film.
在其中一个实施例中,所述镀铜辊具有所述第一温区和所述第二温区的长度分别独立地为5mm~10mm。In one embodiment, the lengths of the first temperature zone and the second temperature zone of the copper plating roller are independently 5 mm to 10 mm.
在其中一个实施例中,蒸发所述金属铜的真空度为10-4Pa~10-5Pa,温度为1600℃~1800℃,铜蒸汽的浓度维持为60mol/L~80mol/L。In one embodiment, the vacuum degree for evaporating the metallic copper is 10-4Pa to 10-5Pa, the temperature is 1600°C to 1800°C, and the concentration of copper vapor is maintained at 60mol/L to 80mol/L.
在其中一个实施例中,镀覆所述铜金属层的过程中,所述聚合物薄膜的运动速度为10m/min~100m/min。In one embodiment, during the process of plating the copper metal layer, the movement speed of the polymer film is 10 m/min to 100 m/min.
在其中一个实施例中,所述聚合物薄膜的材质选自绝缘聚合物材料和无机非导电填料形成的复合物、绝缘聚合物材料和导电填料形成的复合物、绝缘聚合物材料或导电聚合物材料,其中,所述绝缘聚合物材料和无机非导电填料形成的复合物中所述绝缘聚合物材料的质量百分比≥90%,所述绝缘聚合物材料和导电填料形成的复合物中所述绝缘聚合物材料的质量百分比≥90%。In one embodiment, the material of the polymer film is selected from the group consisting of a composite of an insulating polymer material and an inorganic non-conductive filler, a composite of an insulating polymer material and a conductive filler, an insulating polymer material or a conductive polymer. Material, wherein the mass percentage of the insulating polymer material in the composite formed by the insulating polymer material and the inorganic non-conductive filler is ≥90%, and the insulation in the composite formed by the insulating polymer material and the conductive filler The mass percentage of polymer material is ≥90%.
在其中一个实施例中,所述绝缘聚合物材料选自纤维素及其衍生物、淀粉及其衍生物、蛋白质及其衍生物、聚乙烯醇及其交联聚合物、聚乙二醇及其交联聚合物、聚酰胺、聚对苯二甲酸酯、聚酰亚胺、聚乙烯、聚丙烯、聚苯乙烯、聚氯乙烯、芳纶、聚二甲酰苯二胺、丙烯腈-丁二烯-苯乙烯共聚物、聚对苯二甲酸乙二醇酯、聚对苯二甲酸丁二醇酯、聚对苯二甲酰对苯二胺、聚丙乙烯、聚甲醛、环氧树脂、酚醛树脂、聚四氟乙烯、聚偏氟乙烯、硅橡胶及聚碳酸酯中的一种或多种。In one embodiment, the insulating polymer material is selected from the group consisting of cellulose and its derivatives, starch and its derivatives, protein and its derivatives, polyvinyl alcohol and its cross-linked polymers, polyethylene glycol and its Cross-linked polymer, polyamide, polyterephthalate, polyimide, polyethylene, polypropylene, polystyrene, polyvinyl chloride, aramid, polyphenylenediamide, acrylonitrile-butan Diene-styrene copolymer, polyethylene terephthalate, polybutylene terephthalate, poly(p-phenylene terephthalamide), polypropylene, polyformaldehyde, epoxy resin, phenolic resin One or more of resin, polytetrafluoroethylene, polyvinylidene fluoride, silicone rubber and polycarbonate.
在其中一个实施例中,所述导电聚合物材料选自掺杂聚氮化硫和/或掺杂聚乙炔。In one embodiment, the conductive polymer material is selected from doped polysulfide nitride and/or doped polyacetylene.
在其中一个实施例中,所述无机非导电填料选自陶瓷材料、玻璃材料及陶瓷复合材料中的一种或多种。In one embodiment, the inorganic non-conductive filler is selected from one or more of ceramic materials, glass materials and ceramic composite materials.
在其中一个实施例中,所述导电填料选自碳黑、碳纳米管、石墨、乙炔黑、石墨烯、镍、铁、铜、铝、合金、镍包覆的石墨粉及镍包覆的碳纤维中的一种或多种。In one embodiment, the conductive filler is selected from the group consisting of carbon black, carbon nanotubes, graphite, acetylene black, graphene, nickel, iron, copper, aluminum, alloys, nickel-coated graphite powder, and nickel-coated carbon fiber. one or more of them.
本发明一方面,还提供一种铜复合集流体,其采用如上述所述的铜复合集流体的制备方法制得。In one aspect, the present invention also provides a copper composite current collector, which is prepared by the above-mentioned preparation method of a copper composite current collector.
在其中一个实施例中,所述铜复合集流体具有以下性能中的至少一种:In one embodiment, the copper composite current collector has at least one of the following properties:
(1)表面粗糙度>0.2μm;(1) Surface roughness>0.2μm;
(2)比表面积>20m 2/g; (2) Specific surface area >20m 2 /g;
(3)表面孔数量>10个/m 2,孔径≥10nm; (3) The number of surface pores is >10/m 2 and the pore diameter is ≥10nm;
(4)穿刺强度≥200gf;(4) Puncture strength ≥200gf;
(5)纵向拉伸强度≥150MPa,纵向延伸率≥10%,横向拉伸强度≥150Mpa,横向延伸率≥10%。(5) Longitudinal tensile strength ≥ 150MPa, longitudinal elongation ≥ 10%, transverse tensile strength ≥ 150Mpa, transverse elongation ≥ 10%.
本发明另一方面,进一步提供一种负极,其包括上述所述的铜复合集流体及位于所述铜复合集流体一面或两面的负极活性材料层。In another aspect, the present invention further provides a negative electrode, which includes the above-mentioned copper composite current collector and a negative electrode active material layer located on one or both sides of the copper composite current collector.
本发明再一方面,提供一种锂离子电池,其包括上述所述的负极。In yet another aspect, the present invention provides a lithium ion battery, which includes the above-mentioned negative electrode.
本发明又一方面,提供一种用电装置,其采用上述所述的锂离子电池作为电源。In another aspect, the present invention provides an electrical device that uses the above-mentioned lithium-ion battery as a power source.
上述铜复合集流体的制备方法通过调控镀铜辊的温度,使其具有不同的温区,从而可以使得铜金属层在聚合物薄膜表面镀覆的速度不同,使铜金属层中铜晶体的生长速度不同,以在铜金属层表面构造形成孔结构。孔结构的形成实现了铜复合集流体粗糙度、比表面积的增加,从而增加了电池内活性物质和铜复合集流体之间的接触面积,提升了活性物质的涂覆量,且能够降低电池内阻,提高电池容量和能量密度,并延长了电池的循环寿命。The preparation method of the above-mentioned copper composite current collector regulates the temperature of the copper plating roller so that it has different temperature zones, so that the copper metal layer can be plated on the surface of the polymer film at different speeds, thereby increasing the growth of copper crystals in the copper metal layer. The speed is different to form a hole structure on the surface of the copper metal layer. The formation of the pore structure increases the roughness and specific surface area of the copper composite current collector, thereby increasing the contact area between the active material and the copper composite current collector in the battery, increasing the coating amount of the active material, and reducing the internal temperature of the battery. resistance, improve battery capacity and energy density, and extend battery cycle life.
为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly explain the specific embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings that need to be used in the description of the specific embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description The drawings illustrate some embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on these drawings without exerting any creative effort.
图1为实施例1中制得的铜复合集流体的SEM图。Figure 1 is an SEM image of the copper composite current collector prepared in Example 1.
现将详细地提供本发明实施方式的参考,其一个或多个实例描述于下文。提供每一实例作为解释而非限制本发明。实际上,对本领域技术人员而言,显而易见的是,可以对本发明进行多种修改和变化而不背离本发明的范围或精神。例如,作为一个实施方式的部分而说明或描述的特征可以用于另一实施方式中,来产生更进一步的实施方式。Reference will now be made in detail to embodiments of the invention, one or more examples of which are described below. Each example is provided by way of explanation, not limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the scope or spirit of the invention. For example, features illustrated or described as part of one embodiment can be used in another embodiment, to yield still further embodiments.
因此,旨在本发明覆盖落入所附权利要求的范围及其等同范围中的此类修改和变化。本发明的其它对象、特征和方面公开于以下详细描述中或从中是显而易见的。本领域普通技术人员应理解本讨论仅是示例性实施方式的描述,而非意在限制本发明更广阔的方面。Thus, it is intended that the present invention cover such modifications and variations as come within the scope of the appended claims and their equivalents. Other objects, features, and aspects of the invention are disclosed in, or are apparent from, the following detailed description. Those of ordinary skill in the art will appreciate that this discussion is merely a description of exemplary embodiments and is not intended to limit the broader aspects of the invention.
除非另有定义,本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同。本文中在本发明的说明书中所使用的术语只是为了描述具体的实施例的目的,不是旨在于限制本发明。本文所使用的术语“和/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the technical field to which the invention belongs. The terminology used herein in the description of the invention is for the purpose of describing specific embodiments only and is not intended to limit the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
除了在操作实施例中所示以外或另外表明之外,所有在说明书和权利要求中表示成分的量、物化性质等所使用的数字理解为在所有情况下通过术语“约” 来调整。例如,因此,除非有相反的说明,否则上述说明书和所附权利要求书中列出的数值参数均是近似值,本领域的技术人员能够利用本文所公开的教导内容寻求获得的所需特性,适当改变这些近似值。用端点表示的数值范围的使用包括该范围内的所有数字以及该范围内的任何范围,例如,1至5包括1、1.1、1.3、1.5、2、2.75、3、3.80、4和5等等。Except as shown in the operating examples or otherwise indicated, all numbers used in the specification and claims to express amounts, physicochemical properties, etc. of ingredients are to be understood to be adjusted in all cases by the term "about." For example, therefore, unless stated to the contrary, the numerical parameters set forth in the foregoing specification and appended claims are approximations, and those skilled in the art will be able to seek to obtain the desired properties using the teachings disclosed herein, as appropriate. Change these approximations. The use of numerical ranges expressed by endpoints includes all numbers within that range and any range within that range, for example, 1 to 5 includes 1, 1.1, 1.3, 1.5, 2, 2.75, 3, 3.80, 4, and 5, etc. .
可以理解,传统的铜复合集流体的表面较为平整光滑,难以在其表面涂覆较多的电池活性物质,且涂覆质量较差。为此,本发明提供了一种铜复合集流体的制备方法,该方法通过调控镀铜辊的温度,使其具有不同的温区,从而可以使得铜金属层在聚合物薄膜表面镀覆的速度不同,使铜金属层中铜晶体的生长速度不同,以在铜金属层表面构造形成孔结构。孔结构的形成实现了铜复合集流体粗糙度、比表面积的增加(相较于传统的铜复合集流体至少提升了20%),从而增加了电池内活性物质和铜复合集流体之间的接触面积,提升了活性物质的涂覆量(相较于传统的铜复合集流体至少提升了5%),且能够降低电池内阻,提高电池容量和能量密度,并延长了电池的循环寿命。It can be understood that the surface of traditional copper composite current collectors is relatively flat and smooth, making it difficult to coat more battery active materials on the surface, and the coating quality is poor. To this end, the present invention provides a method for preparing a copper composite current collector. This method regulates the temperature of the copper plating roller so that it has different temperature zones, thereby increasing the plating speed of the copper metal layer on the surface of the polymer film. Different growth rates of copper crystals in the copper metal layer are different to form a hole structure on the surface of the copper metal layer. The formation of the pore structure increases the roughness and specific surface area of the copper composite current collector (at least an increase of 20% compared to traditional copper composite current collectors), thereby increasing the contact between the active material and the copper composite current collector in the battery. area, increases the coating amount of active materials (at least 5% increase compared to traditional copper composite current collectors), and can reduce the internal resistance of the battery, increase the battery capacity and energy density, and extend the cycle life of the battery.
本发明一方面,涉及一种铜复合集流体的制备方法,其包括以下步骤:On the one hand, the present invention relates to a preparation method of a copper composite current collector, which includes the following steps:
提供聚合物薄膜;Provide polymer films;
采用真空蒸镀技术,将上述聚合物薄膜穿过镀铜辊,其中沿所述镀铜辊的轴向,镀铜辊具有第一温区和第二温区,第一温区的温度为40℃~50℃,第二温区的温度为10℃~20℃;以及Using vacuum evaporation technology, the above-mentioned polymer film is passed through a copper plating roller, wherein along the axial direction of the copper plating roller, the copper plating roller has a first temperature zone and a second temperature zone, and the temperature of the first temperature zone is 40 ℃~50℃, the temperature of the second temperature zone is 10℃~20℃; and
在真空条件下蒸发金属铜,以在聚合物薄膜的两面镀覆铜金属层。Metallic copper is evaporated under vacuum conditions to plate copper metal layers on both sides of the polymer film.
在一些实施方式中,第一温区的温度可以为40℃~50℃之间的任意值,例如,还可以为41℃、42℃、43℃、44℃、45℃、46℃、47℃、48℃、49℃。In some embodiments, the temperature of the first temperature zone can be any value between 40°C and 50°C, for example, it can also be 41°C, 42°C, 43°C, 44°C, 45°C, 46°C, or 47°C. , 48℃, 49℃.
在一些实施方式中,第二温区的温度可以为10℃~20℃之间的任意值,例如, 还可以为11℃、12℃、13℃、14℃、15℃、16℃、17℃、18℃、19℃。In some embodiments, the temperature of the second temperature zone can be any value between 10°C and 20°C, for example, it can also be 11°C, 12°C, 13°C, 14°C, 15°C, 16°C, 17°C , 18℃, 19℃.
在一些实施方式中,镀铜辊具有第一温区和第二温区的长度分别独立地为5mm~10mm之间的任意值,例如,还可以为6mm、7mm、8mm、9mm。In some embodiments, the copper plating roller has a first temperature zone and a length of the second temperature zone that are independently any value between 5 mm and 10 mm, for example, they may also be 6 mm, 7 mm, 8 mm, or 9 mm.
在一些实施方式中,蒸发金属铜的真空度可以为10 -4Pa~10 -5Pa,温度可以为1600℃~1800℃,铜蒸汽的浓度维持为60mol/L~80mol/L。 In some embodiments, the vacuum degree of evaporating metallic copper can be 10 -4 Pa to 10 -5 Pa, the temperature can be 1600°C to 1800°C, and the concentration of copper vapor is maintained at 60 mol/L to 80 mol/L.
在一些实施方式中,镀覆铜金属层的过程中,聚合物薄膜的运动速度可以为10m/min~100m/min,还可以为20m/min、30m/min、40m/min、50m/min、60m/min、70m/min、80m/min、90m/min。In some embodiments, during the process of plating the copper metal layer, the movement speed of the polymer film can be 10m/min~100m/min, or can also be 20m/min, 30m/min, 40m/min, 50m/min, 60m/min, 70m/min, 80m/min, 90m/min.
在一些实施方式中,铜金属层的纯度≥99.8%。In some embodiments, the copper metal layer has a purity of ≥99.8%.
在一些实施方式中,聚合物薄膜的材质不做限制,选用本领域任意公知的聚合物材料即可,包括,但不限于绝缘聚合物材料和无机非导电填料形成的复合物、绝缘聚合物材料和导电填料形成的复合物、绝缘聚合物材料或导电聚合物材料,其中,绝缘聚合物材料和无机非导电填料形成的复合物中绝缘聚合物材料的质量百分比≥90%,绝缘聚合物材料和导电填料形成的复合物中绝缘聚合物材料的质量百分比≥90%。In some embodiments, the material of the polymer film is not limited, and any polymer material known in the art can be used, including, but not limited to, composites of insulating polymer materials and inorganic non-conductive fillers, insulating polymer materials and conductive fillers, insulating polymer materials or conductive polymer materials, wherein the mass percentage of insulating polymer materials in the composite formed of insulating polymer materials and inorganic non-conductive fillers is ≥90%, insulating polymer materials and The mass percentage of the insulating polymer material in the composite formed by the conductive filler is ≥90%.
在一些实施方式中,绝缘聚合物材料可以选自纤维素及其衍生物、淀粉及其衍生物、蛋白质及其衍生物、聚乙烯醇及其交联聚合物、聚乙二醇及其交联聚合物、聚酰胺、聚对苯二甲酸酯、聚酰亚胺、聚乙烯、聚丙烯、聚苯乙烯、聚氯乙烯、芳纶、聚二甲酰苯二胺、丙烯腈-丁二烯-苯乙烯共聚物、聚对苯二甲酸乙二醇酯、聚对苯二甲酸丁二醇酯、聚对苯二甲酰对苯二胺、聚丙乙烯、聚甲醛、环氧树脂、酚醛树脂、聚四氟乙烯、聚偏氟乙烯、硅橡胶及聚碳酸酯中的一种或多种。In some embodiments, the insulating polymer material may be selected from cellulose and its derivatives, starch and its derivatives, proteins and its derivatives, polyvinyl alcohol and its cross-linked polymers, polyethylene glycol and its cross-linked Polymer, polyamide, polyterephthalate, polyimide, polyethylene, polypropylene, polystyrene, polyvinyl chloride, aramid, polyphenylenediamide, acrylonitrile-butadiene -Styrene copolymer, polyethylene terephthalate, polybutylene terephthalate, poly(p-phenylene terephthalamide), polypropylene, polyformaldehyde, epoxy resin, phenolic resin, One or more of polytetrafluoroethylene, polyvinylidene fluoride, silicone rubber and polycarbonate.
在一些实施方式中,导电聚合物材料可以选自掺杂聚氮化硫和/或掺杂聚乙 炔。In some embodiments, the conductive polymer material may be selected from doped polysulfide nitride and/or doped polyacetylene.
在一些实施方式中,无机非导电填料可以选自陶瓷材料、玻璃材料及陶瓷复合材料中的一种或多种。In some embodiments, the inorganic non-conductive filler may be selected from one or more of ceramic materials, glass materials and ceramic composite materials.
在一些实施方式中,导电填料可以选自碳黑、碳纳米管、石墨、乙炔黑、石墨烯、镍、铁、铜、铝、合金、镍包覆的石墨粉及镍包覆的碳纤维中的一种或多种。其中,合金可以包括镍、铁、铜及铝中的一种或多种。In some embodiments, the conductive filler may be selected from the group consisting of carbon black, carbon nanotubes, graphite, acetylene black, graphene, nickel, iron, copper, aluminum, alloys, nickel-coated graphite powder, and nickel-coated carbon fiber. one or more. The alloy may include one or more of nickel, iron, copper and aluminum.
在一些实施方式中,在聚合物薄膜的两面镀覆铜金属层后,还包括收卷的步骤;In some embodiments, after plating copper metal layers on both sides of the polymer film, a step of winding is further included;
可选地,收卷的张力可以为5N~25N。Optionally, the winding tension may be 5N to 25N.
本发明一方面,还提供一种铜复合集流体,其采用如上述所述的铜复合集流体的制备方法制得。In one aspect, the present invention also provides a copper composite current collector, which is prepared by the above-mentioned preparation method of a copper composite current collector.
在一些实施方式中,铜复合集流体具有以下性能中的至少一种:In some embodiments, the copper composite current collector has at least one of the following properties:
(1)表面粗糙度>0.2μm;(1) Surface roughness>0.2μm;
(2)比表面积>20m 2/g; (2) Specific surface area >20m 2 /g;
(3)表面孔数量>10个/m 2,孔径≥10nm; (3) The number of surface pores is >10/m 2 and the pore diameter is ≥10nm;
(4)穿刺强度≥200gf;(4) Puncture strength ≥200gf;
(5)纵向(MD)拉伸强度≥150MPa,纵向(MD)延伸率≥10%,横向(TD)拉伸强度≥150Mpa,横向(TD)延伸率≥10%。(5) Longitudinal (MD) tensile strength ≥ 150MPa, longitudinal (MD) elongation ≥ 10%, transverse (TD) tensile strength ≥ 150Mpa, transverse (TD) elongation ≥ 10%.
在一些实施方式中,铜复合集流体的比表面积还可以为25m 2/g、28m 2/g、30m 2/g、35m 2/g,表面孔数量>100个/m 2,例如还可以为150个/m 2、200个/m 2、300个/m 2、400个/m 2、500个/m 2。 In some embodiments, the specific surface area of the copper composite current collector can also be 25m 2 /g, 28m 2 /g, 30m 2 /g, 35m 2 /g, and the number of surface pores is >100/m 2 , for example, it can also be 150 pieces/m 2 , 200 pieces/m 2 , 300 pieces/m 2 , 400 pieces/m 2 , 500 pieces/m 2 .
在一些实施方式中,铜复合集流体的厚度可以为1.6μm~31μm,优选地,聚合物薄膜的厚度可以为1μm~25μm,铜金属层的厚度可以为0.3μm~3μm。 更优选地,聚合物薄膜的厚度为2μm~8μm。将聚合物薄膜的厚度调控在此范围内,既可以降低铜复合集流体生产成本,又可以避免加工过程中聚合物薄膜出现断带问题。In some embodiments, the thickness of the copper composite current collector may be 1.6 μm ~ 31 μm. Preferably, the thickness of the polymer film may be 1 μm ~ 25 μm, and the thickness of the copper metal layer may be 0.3 μm ~ 3 μm. More preferably, the thickness of the polymer film is 2 μm to 8 μm. Regulating the thickness of the polymer film within this range can not only reduce the production cost of copper composite current collectors, but also avoid the problem of polymer film breakage during processing.
在一些实施方式中,聚合物薄膜满足以下性能中的至少一种:In some embodiments, the polymer film meets at least one of the following properties:
(1)穿刺强度≥200gf;(1)Puncture strength ≥200gf;
(2)纵向(MD)拉伸强度≥160MPa,纵向(MD)延伸率≥30%,横向(TD)拉伸强度≥160Mpa,横向(TD)延伸率≥30%。(2) Longitudinal (MD) tensile strength ≥ 160MPa, longitudinal (MD) elongation ≥ 30%, transverse (TD) tensile strength ≥ 160Mpa, transverse (TD) elongation ≥ 30%.
本发明另一方面,进一步提供一种负极,其包括上述所述的铜复合集流体及位于所述铜复合集流体一面或两面的负极活性材料层。In another aspect, the present invention further provides a negative electrode, which includes the above-mentioned copper composite current collector and a negative electrode active material layer located on one or both sides of the copper composite current collector.
在一些实施方式中,负极活性材料层的材质不做限制,可以由常用的负极活性材料、导电剂及负极粘结剂组成;其中,所述负极活性材料可以为石墨、钛酸锂、锂,所述负极粘结剂可以为丁苯乳胶、丙烯酸酯及羧甲基纤维素钠中的至少一种,所述导电剂可以为碳纳米管及导电碳黑中的至少一种。In some embodiments, the material of the negative active material layer is not limited and can be composed of commonly used negative active materials, conductive agents, and negative binders; wherein the negative active material can be graphite, lithium titanate, or lithium, The negative electrode binder may be at least one of styrene-butadiene latex, acrylate, and sodium carboxymethyl cellulose, and the conductive agent may be at least one of carbon nanotubes and conductive carbon black.
本发明再一方面,提供一种锂离子电池,其包括上述所述的负极。In yet another aspect, the present invention provides a lithium ion battery, which includes the above-mentioned negative electrode.
在一些实施方式中,锂离子电池还可以包括正极和电解质。In some embodiments, a lithium-ion battery may also include a positive electrode and an electrolyte.
所述正极包括正极集流体及位于所述正极集流体表面的正极活性材料层,其中,正极集流体可以为铝集流体,正极活性材料层材质也不做限制,可以由常用的正极活性材料、导电剂及正极粘结剂组成;其中,正极活性材料可以为本领域常用的任意正极活性材料,比如钴酸锂、磷酸铁锂、NCA、NCM、锰酸锂、镍酸锂、NCMA或无钴正极;正极粘结剂可以为PVDF及丙烯酸酯中的至少一种,所述导电剂可以为碳纳米管及导电碳黑中的至少一种;。The positive electrode includes a positive electrode current collector and a positive electrode active material layer located on the surface of the positive electrode current collector. The positive electrode current collector can be an aluminum current collector. The material of the positive electrode active material layer is not limited and can be made of commonly used positive electrode active materials, It is composed of conductive agent and positive electrode binder; among which, the positive electrode active material can be any positive electrode active material commonly used in this field, such as lithium cobalt oxide, lithium iron phosphate, NCA, NCM, lithium manganate, lithium nickelate, NCMA or cobalt-free Positive electrode; the positive electrode binder can be at least one of PVDF and acrylate, and the conductive agent can be at least one of carbon nanotubes and conductive carbon black;.
在一些实施方式中,电解质可以为固态电解质、半固态电解质或液态电解液,其中固态电解质和半固态电解质可以为氧化物或硫化物电解质,液态电解 液中的溶质可以为六氟磷酸锂。In some embodiments, the electrolyte can be a solid electrolyte, a semi-solid electrolyte or a liquid electrolyte, wherein the solid electrolyte and semi-solid electrolyte can be an oxide or sulfide electrolyte, and the solute in the liquid electrolyte can be lithium hexafluorophosphate.
在一些实施方式中,上述锂离子电池还可以包括隔膜,其中隔膜可以本领域公知的任意隔膜,比如,PE湿法隔膜、PP干法隔膜或双层PE/PP涂覆隔膜。In some embodiments, the above-mentioned lithium ion battery may further include a separator, wherein the separator may be any separator known in the art, such as a PE wet separator, a PP dry separator or a double-layer PE/PP coated separator.
所述锂离子电池的形状不做限制,例如可以为圆柱形、方形。The shape of the lithium-ion battery is not limited, and may be cylindrical or square, for example.
本发明又一方面,提供一种用电装置,其采用上述所述的锂离子电池作为电源。In another aspect, the present invention provides an electrical device that uses the above-mentioned lithium-ion battery as a power source.
在一些实施方式中,用电装置的具体类型包括,但不限于移动终端(手机、移动电脑等)、智能穿戴、电动工具(电钻、电动机等)、电动汽车、移动电源等。In some embodiments, specific types of electrical devices include, but are not limited to, mobile terminals (mobile phones, mobile computers, etc.), smart wearables, power tools (electric drills, electric motors, etc.), electric vehicles, mobile power supplies, etc.
以下结合具体实施例和对比例对本发明作进一步详细的说明。The present invention will be further described in detail below with reference to specific examples and comparative examples.
实施例1Example 1
1、铜复合集流体的制备1. Preparation of copper composite current collector
采用真空蒸镀工艺制备铜复合集流体,聚合物薄膜为双向拉伸的聚丙烯(BOPP)薄膜。具体步骤如下:A copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
1)将真空离子蒸镀设备的蒸镀舱室抽真空至真空度为10 -5Pa后,将厚度为4μm的BOPP薄膜穿过镀铜辊,其中镀铜辊具有温度为45℃的第一温区和温度为15℃的第二温区,且具有第一温区和具有第二温区的镀铜辊的长度均为6mm; 1) After evacuating the evaporation chamber of the vacuum ion evaporation equipment to a vacuum degree of 10 -5 Pa, pass the BOPP film with a thickness of 4 μm through a copper plating roller, where the copper plating roller has a first temperature of 45°C. zone and a second temperature zone with a temperature of 15°C, and the lengths of the copper plating rollers with the first temperature zone and the second temperature zone are both 6 mm;
2)在1800℃下蒸发蒸发舟中的纯度为99.9%的铜金属,维持铜蒸汽的浓度为70mol/L,以在步骤1)中BOPP薄膜的两面蒸镀厚度为1μm的铜金属层,其中,蒸镀过程中,BOPP薄膜的运动速度为30m/min。随后在张力为5N作用力下收卷,并于20N下放卷蒸镀有铜金属层的BOPP薄膜,制得铜复合集流体。测得铜复合集流体的表面形貌如图1所示,测得铜复合集流体的相关性能如表1 所示。2) Evaporate copper metal with a purity of 99.9% in the evaporation boat at 1800°C, maintain the concentration of copper vapor at 70 mol/L, and evaporate a copper metal layer with a thickness of 1 μm on both sides of the BOPP film in step 1), where , During the evaporation process, the movement speed of the BOPP film is 30m/min. The BOPP film with a copper metal layer evaporated was then rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector. The measured surface morphology of the copper composite current collector is shown in Figure 1, and the measured related properties of the copper composite current collector are shown in Table 1.
2、电池装配2. Battery assembly
正极:磷酸铁锂;Positive electrode: lithium iron phosphate;
负极:由步骤1中制得的铜复合集流体及位于铜复合集流体表面的石墨层组成;Negative electrode: composed of the copper composite current collector prepared in step 1 and a graphite layer located on the surface of the copper composite current collector;
电解液:以六氟磷酸锂为溶质的液态电解液;Electrolyte: liquid electrolyte with lithium hexafluorophosphate as solute;
隔膜:聚乙烯(PE)微孔隔膜;Separator: polyethylene (PE) microporous separator;
将上述各个部件装配成型号为100Ah的三元锂离子电池,并进行相关性能测试,测试结果如表2所示。Assemble the above components into a 100Ah ternary lithium-ion battery, and conduct relevant performance tests. The test results are shown in Table 2.
实施例2Example 2
本实施例与实施例1的制备方法基本相同,不同之处在于:镀铜辊的温度、铜金属蒸镀参数不同。具体步骤如下:The preparation method of this embodiment is basically the same as that of Example 1, except that the temperature of the copper plating roller and the copper metal evaporation parameters are different. Specific steps are as follows:
采用真空蒸镀工艺制备铜复合集流体,聚合物薄膜为双向拉伸的聚丙烯(BOPP)薄膜。具体步骤如下:A copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
1)将真空离子蒸镀设备的蒸镀舱室抽真空至真空度为10 -5Pa后,将厚度为4μm的BOPP薄膜穿过镀铜辊,其中镀铜辊具有温度为40℃的第一温区和温度为10℃的第二温区,且具有第一温区和具有第二温区的镀铜辊的长度均为8mm; 1) After evacuating the evaporation chamber of the vacuum ion evaporation equipment to a vacuum degree of 10 -5 Pa, pass the BOPP film with a thickness of 4 μm through a copper plating roller, where the copper plating roller has a first temperature of 40°C. zone and a second temperature zone with a temperature of 10°C, and the lengths of the copper plating rollers with the first temperature zone and the second temperature zone are both 8 mm;
2)在1600℃下蒸发蒸发舟中的纯度为99.9%的铜金属,维持铜蒸汽的浓度为60mol/L,以在步骤1)中BOPP薄膜的两面蒸镀厚度为1μm的铜金属层,其中,蒸镀过程中,BOPP薄膜的运动速度为20m/min。随后在张力为5N作用力下收卷,并于20N下放卷蒸镀有铜金属层的BOPP薄膜,制得铜复合集流体。2) Evaporate copper metal with a purity of 99.9% in the evaporation boat at 1600°C, maintain the concentration of copper vapor at 60 mol/L, and evaporate a copper metal layer with a thickness of 1 μm on both sides of the BOPP film in step 1), where , During the evaporation process, the movement speed of the BOPP film is 20m/min. The BOPP film with a copper metal layer evaporated was then rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector.
实施例3Example 3
本实施例与实施例1的制备方法基本相同,不同之处在于:聚合物薄膜为聚对苯二甲酸乙二醇酯薄膜,聚合物薄膜厚度及铜金属层厚度不同、镀铜辊的温度、铜金属蒸镀参数不同。具体步骤如下:The preparation method of this embodiment is basically the same as that of Example 1, except that the polymer film is a polyethylene terephthalate film, the thickness of the polymer film and the thickness of the copper metal layer are different, the temperature of the copper plating roller, Copper metal evaporation parameters are different. Specific steps are as follows:
采用真空蒸镀工艺制备铜复合集流体,聚合物薄膜为聚对苯二甲酸乙二醇酯薄膜。具体步骤如下:A copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a polyethylene terephthalate film. Specific steps are as follows:
1)将真空离子蒸镀设备的蒸镀舱室抽真空至真空度为10-5Pa后,将厚度为6μm的聚对苯二甲酸乙二醇酯薄膜穿过镀铜辊,其中镀铜辊具有温度为50℃的第一温区和温度为20℃的第二温区,且具有第一温区和具有第二温区的镀铜辊的长度均为10mm;1) After evacuating the evaporation chamber of the vacuum ion evaporation equipment to a vacuum degree of 10-5Pa, pass a polyethylene terephthalate film with a thickness of 6 μm through a copper plating roller, where the copper plating roller has a temperature The first temperature zone is 50°C and the second temperature zone is 20°C, and the lengths of the copper plating rollers with the first temperature zone and the second temperature zone are both 10 mm;
2)在1800℃下蒸发蒸发舟中的纯度为99.9%的铜金属,维持铜蒸汽的浓度为80mol/L,以在步骤1)中聚对苯二甲酸乙二醇酯薄膜的两面蒸镀厚度为2μm的铜金属层,其中,蒸镀过程中,聚对苯二甲酸乙二醇酯薄膜的运动速度为80m/min。随后在张力为5N作用力下收卷,并于20N下放卷蒸镀有铜金属层的聚对苯二甲酸乙二醇酯薄膜,制得铜复合集流体。2) Evaporate the copper metal with a purity of 99.9% in the evaporation boat at 1800°C, and maintain the concentration of copper vapor at 80 mol/L to achieve the evaporation thickness on both sides of the polyethylene terephthalate film in step 1) It is a copper metal layer of 2 μm. During the evaporation process, the movement speed of the polyethylene terephthalate film is 80m/min. Then, the polyethylene terephthalate film evaporated with a copper metal layer was rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector.
对比例1Comparative example 1
1、铜复合集流体的制备1. Preparation of copper composite current collector
采用真空蒸镀工艺制备铜复合集流体,聚合物薄膜为双向拉伸的聚丙烯(BOPP)薄膜。具体步骤如下:A copper composite current collector was prepared using a vacuum evaporation process, and the polymer film was a biaxially oriented polypropylene (BOPP) film. Specific steps are as follows:
1)将真空离子蒸镀设备的蒸镀舱室抽真空至真空度为10 -5Pa后,将厚度为4μm的BOPP薄膜穿过镀铜辊,其中镀铜辊的温度为30℃; 1) After evacuating the evaporation chamber of the vacuum ion evaporation equipment to a vacuum degree of 10 -5 Pa, pass the BOPP film with a thickness of 4 μm through a copper plating roller, where the temperature of the copper plating roller is 30°C;
2)在1700℃下蒸发蒸发舟中的纯度为99.9%的铜金属,维持铜蒸汽的浓度为150mol/L,以在步骤1)中BOPP薄膜的两面蒸镀厚度为1μm的铜金属层,其中,蒸镀过程中,BOPP薄膜的运动速度为50m/min。随后在张力为5N作用 力下收卷,并于20N下放卷蒸镀有铜金属层的BOPP薄膜,制得铜复合集流体。测得铜复合集流体的相关性能如表1所示。2) Evaporate copper metal with a purity of 99.9% in the evaporation boat at 1700°C, maintain the concentration of copper vapor at 150 mol/L, and evaporate a copper metal layer with a thickness of 1 μm on both sides of the BOPP film in step 1), where , During the evaporation process, the movement speed of the BOPP film is 50m/min. The BOPP film with a copper metal layer evaporated was then rolled up under a tension of 5N and unrolled under 20N to prepare a copper composite current collector. The measured relevant properties of the copper composite current collector are shown in Table 1.
2、电池装配2. Battery assembly
正极:磷酸铁锂;Positive electrode: lithium iron phosphate;
负极:由步骤1中制得的铜复合集流体及位于铜复合集流体表面的石墨层组成;Negative electrode: composed of the copper composite current collector prepared in step 1 and a graphite layer located on the surface of the copper composite current collector;
电解液:以六氟磷酸锂为溶质的液态电解液;Electrolyte: liquid electrolyte with lithium hexafluorophosphate as solute;
隔膜:聚乙烯(PE)微孔隔膜;Separator: polyethylene (PE) microporous separator;
将上述各个部件装配成型号为100Ah的三元锂离子电池,并进行相关性能测试,测试结果如表2所示。Assemble the above components into a 100Ah ternary lithium-ion battery, and conduct relevant performance tests. The test results are shown in Table 2.
表1Table 1
三元锂离子电池的相关性能测试:Relevant performance tests of ternary lithium-ion batteries:
剥离力测试、电池内阻测试以及充放电循环性能测试参见国标GB18287_2000,测试结果如表2所示。The peeling force test, battery internal resistance test and charge and discharge cycle performance test refer to the national standard GB18287_2000, and the test results are shown in Table 2.
1)剥离力测试:分别各测试10PCS实施例1和对比例1~3所装配的磷酸铁锂电池中铝复合集流体及正极活性材料层之间的剥离力,并取均值;1) Peeling force test: Test the peeling force between the aluminum composite current collector and the cathode active material layer in the lithium iron phosphate batteries assembled in 10 PCS Example 1 and Comparative Examples 1 to 3 respectively, and take the average value;
2)电池内阻测试:分别各测试10PCS实施例1和对比例1~3所装配的磷酸铁锂电池的内阻,并取均值;2) Battery internal resistance test: Test the internal resistance of 10 PCS lithium iron phosphate batteries assembled in Example 1 and Comparative Examples 1 to 3 respectively, and take the average value;
3)充放电循环性能测试:在容量保持率为80%时,以1C倍率充电和1C倍率放电(1C/1C)分别各测试10PCS实施例1和对比例1~3所装配的磷酸铁 锂电池的循环性能,并取均值。3) Charge and discharge cycle performance test: When the capacity retention rate is 80%, test 10 PCS lithium iron phosphate batteries assembled in Example 1 and Comparative Examples 1 to 3 at 1C rate charging and 1C rate discharge (1C/1C) respectively. cycle performance and take the average value.
表2Table 2
以上所述实施例的各技术特征可以进行任意的组合,为使描述简洁,未对上述实施例中的各个技术特征所有可能的组合都进行描述,然而,只要这些技术特征的组合不存在矛盾,都应当认为是本说明书记载的范围。The technical features of the above embodiments can be combined in any way. To simplify the description, not all possible combinations of the technical features in the above embodiments are described. However, as long as there is no contradiction in the combination of these technical features, All should be considered to be within the scope of this manual.
以上所述实施例仅表达了本发明的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only express several implementation modes of the present invention, and their descriptions are relatively specific and detailed, but they should not be construed as limiting the scope of the invention. It should be noted that, for those of ordinary skill in the art, several modifications and improvements can be made without departing from the concept of the present invention, and these all belong to the protection scope of the present invention. Therefore, the scope of protection of the patent of the present invention should be determined by the appended claims.
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000017426A (en) * | 1998-07-02 | 2000-01-18 | Sumitomo Heavy Ind Ltd | Deposition apparatus |
CN107177820A (en) * | 2017-06-12 | 2017-09-19 | 哈尔滨光宇电源股份有限公司 | High-speed and continuous type vacuum vapor deposition lithium equipment and the method that base material evaporation lithium is realized using it |
CN109355634A (en) * | 2018-12-12 | 2019-02-19 | 安徽金美新材料科技有限公司 | The vacuum deposition apparatus of two-sided continuous coating |
CN113748546A (en) * | 2020-04-17 | 2021-12-03 | 宁德时代新能源科技股份有限公司 | Negative pole piece, secondary battery and device thereof |
US20220056575A1 (en) * | 2020-08-20 | 2022-02-24 | Applied Materials, Inc. | Material deposition apparatus having at least one heating assembly and method for pre- and/or post-heating a substrate |
-
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000017426A (en) * | 1998-07-02 | 2000-01-18 | Sumitomo Heavy Ind Ltd | Deposition apparatus |
CN107177820A (en) * | 2017-06-12 | 2017-09-19 | 哈尔滨光宇电源股份有限公司 | High-speed and continuous type vacuum vapor deposition lithium equipment and the method that base material evaporation lithium is realized using it |
CN109355634A (en) * | 2018-12-12 | 2019-02-19 | 安徽金美新材料科技有限公司 | The vacuum deposition apparatus of two-sided continuous coating |
CN113748546A (en) * | 2020-04-17 | 2021-12-03 | 宁德时代新能源科技股份有限公司 | Negative pole piece, secondary battery and device thereof |
US20220056575A1 (en) * | 2020-08-20 | 2022-02-24 | Applied Materials, Inc. | Material deposition apparatus having at least one heating assembly and method for pre- and/or post-heating a substrate |
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