TW201320454A - Metal foil with coating layer and method for producing same, secondary cell electrode and method for producing same, and lithium ion secondary cell - Google Patents

Metal foil with coating layer and method for producing same, secondary cell electrode and method for producing same, and lithium ion secondary cell Download PDF

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TW201320454A
TW201320454A TW101123840A TW101123840A TW201320454A TW 201320454 A TW201320454 A TW 201320454A TW 101123840 A TW101123840 A TW 101123840A TW 101123840 A TW101123840 A TW 101123840A TW 201320454 A TW201320454 A TW 201320454A
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layer
active material
metal foil
coating layer
resin composition
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Ryoichi Oguro
Naofumi Tokuhara
Isamu Sou
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Furukawa Electric Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D15/00Electrolytic or electrophoretic production of coatings containing embedded materials, e.g. particles, whiskers, wires
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/48After-treatment of electroplated surfaces
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/60Electroplating characterised by the structure or texture of the layers
    • C25D5/605Surface topography of the layers, e.g. rough, dendritic or nodular layers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/60Electroplating characterised by the structure or texture of the layers
    • C25D5/615Microstructure of the layers, e.g. mixed structure
    • C25D5/617Crystalline layers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00Electroplating characterised by the article coated
    • C25D7/06Wires; Strips; Foils
    • C25D7/0614Strips or foils
    • C25D7/0628In vertical cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D1/00Electroforming
    • C25D1/04Wires; Strips; Foils
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/38Electroplating: Baths therefor from solutions of copper
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/387Tin or alloys based on tin
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/485Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H01M4/587Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

Provided is an electrolytic copper foil for use in a collector having consistent Li secondary cell characteristics, that does not give rise to wrinkles in the collector used in an Li secondary cell, that does not rupture, and that has high cohesion to the active material and the collector. This metal foil (copper foil) with a coating layer is furnished with the coating layer on at least one side of an untreated metal film, the coating layer containing free metal particles.

Description

具有被覆層之金屬箔與其製造方法、二次電池用電極及其製造方法與鋰離子二次電池 Metal foil with coating layer, manufacturing method thereof, electrode for secondary battery, manufacturing method thereof and lithium ion secondary battery

本發明係有關於一種作為鋰離子二次電池之電極用、且相當良好之具有被覆層之金屬箔。 The present invention relates to a metal foil having a coating layer which is used as an electrode for a lithium ion secondary battery and which is relatively good.

再者,本發明係有關於一種使用上述具有被覆層之金屬箔之二次電池用電極、使用該電極之鋰離子二次電池。 Furthermore, the present invention relates to a secondary battery electrode using the above-described metal foil having a coating layer, and a lithium ion secondary battery using the same.

鋰離子二次電池係用來作為行動電話、小型便攜型資料收集器、筆記型電腦等之不可或缺的電源。此鋰離子二次電池之負極之集電體一般使用銅箔。負極集電體之形成係於兩面平滑之銅箔表面上塗佈作為負極活性材料層之碳粒子,然後進行壓製以形成負極電極。 Lithium-ion secondary batteries are used as an indispensable power source for mobile phones, small portable data collectors, and notebook computers. The current collector of the negative electrode of the lithium ion secondary battery generally uses a copper foil. The formation of the negative electrode current collector is performed by coating carbon particles as a negative electrode active material layer on the surface of the copper foil which is smooth on both sides, and then pressing to form a negative electrode.

鋰離子二次電池用負極集電體係使用兩表面之表面粗糙度差異小之銅箔,亦即所謂之壓延銅箔,最近,業者針對以兩表面之表面粗糙度差異小之電解銅箔,來抑制該電池之充放電效率降低等問題之技術,積極地進行開發研究(參照專利文獻1)。 The negative electrode current collecting system for a lithium ion secondary battery uses a copper foil having a small difference in surface roughness between the two surfaces, that is, a so-called rolled copper foil. Recently, the manufacturer has directed an electrolytic copper foil having a small difference in surface roughness between the two surfaces. A technique for suppressing problems such as a decrease in the charge and discharge efficiency of the battery has been actively carried out (see Patent Document 1).

兩表面之表面粗糙度差異小之電解銅箔,係適當地選擇水溶性高分子物質、界面活性劑、有機硫化合物、氯離子等,並進行微量添加來製備。為大家所熟知之代表性的技術,例如於電解液中添加具有氫硫基之化合物、氯離子、分子量10000以下之低分子量膠、與高分子多醣類,其所製成之電解銅箔之製造方法(參照專利文獻2)。 An electrolytic copper foil having a small difference in surface roughness between the two surfaces is prepared by appropriately selecting a water-soluble polymer substance, a surfactant, an organic sulfur compound, a chloride ion, or the like, and adding it in a small amount. A well-known representative technique, for example, a compound having a hydrogenthio group, a chloride ion, a low molecular weight gel having a molecular weight of 10,000 or less, and a polymer polysaccharide, which are prepared by adding an electrolytic copper foil to the electrolyte. Manufacturing method (refer to Patent Document 2).

以該製造方法所製作之電解銅箔(集電體),於兩表面上一起塗佈上作為活性物質之黑鉛粒子與黏合劑,然後進行加熱、加壓壓合,形成具有活性物質之銅箔,以作為鋰離子二次電池用之負極電極。 The electrolytic copper foil (current collector) produced by the production method is coated with black lead particles as an active material and a binder on both surfaces, and then heated and pressure-bonded to form copper having an active material. A foil is used as a negative electrode for a lithium ion secondary battery.

近年來,為了達到鋰離子二次電池之高容量化,業者紛紛提出利用可於充電時與鋰進行電化學之合金化的鍺、矽、錫等,來作為負極活性物質之鋰離子二次電池(參照專利文獻3)。 In recent years, in order to achieve a high capacity of a lithium ion secondary battery, a lithium ion secondary battery using a ruthenium, osmium, tin, or the like which can be electrochemically alloyed with lithium during charging has been proposed as a negative electrode active material. (Refer to Patent Document 3).

以高容量化為目的之鋰離子二次電池用負極電極,係於CVD法與濺鍍法等製作之基體金屬箔上,堆積形成例如矽之非晶矽薄膜與微晶矽薄膜。由於以上述方法所形成之活性物質的薄膜層密接於集電體,因此可表面良好的充放電循環(參照專利文獻4)。 The negative electrode for a lithium ion secondary battery for the purpose of increasing the capacity is formed by depositing, for example, an amorphous ruthenium film and a microcrystalline ruthenium film on a base metal foil produced by a CVD method or a sputtering method. Since the thin film layer of the active material formed by the above method is in close contact with the current collector, the surface can be well charged and discharged (see Patent Document 4).

此外,近年來,業者也開發一種將矽粉與亞醯胺類黏合劑,一起藉由有機溶劑形成漿狀,並於銅箔上進行塗佈、乾燥、壓合以形成電極之形成方法。然而,此粉末狀之矽與錫,其一般粒徑小,為0.1~3μm,難以於作為負極集電體之金屬箔之正反兩面上,以均勻的厚度進行具有適當接著力的塗佈,使得塗佈效率不佳。 Further, in recent years, the industry has also developed a method for forming an electrode by forming a slurry of a tantalum powder and a melamine-based binder together with an organic solvent, coating, drying, and pressing on a copper foil. However, the powdery bismuth and tin generally have a small particle diameter of 0.1 to 3 μm, and it is difficult to apply a coating having an appropriate adhesion with a uniform thickness on both sides of the metal foil as the negative electrode current collector. The coating efficiency is not good.

而且,於此鋰離子二次電池用負極電極中,於充電時,例如矽活性物質因吸收鋰離子,其體積最大膨脹約4倍,而於放電時,放出鋰離子而收縮。藉由伴隨充放電之活性物質體積的膨脹與收縮,不僅會有該活性物質由集電體剝離之問題,且集電體會有應力等現象產生。 Further, in the negative electrode for a lithium ion secondary battery, for example, the ruthenium active material absorbs lithium ions at the time of charging, and its volume expands by a maximum of about four times, and at the time of discharge, lithium ions are released and contracted. By the expansion and contraction of the volume of the active material accompanying charging and discharging, not only the problem that the active material is peeled off from the current collector but also the phenomenon that the current collector has stress or the like occurs.

電池中包括具有膨脹收縮劇烈之活性物質層之金屬箔的電極,若重複進行數次之充放電時,因集電體(金屬箔)也同樣進行收縮,故容易於內部產生皺摺。為了容許皺摺,必須使電池內電極所佔之體積保有空間彈性來設計,但相對地,則會有單位體積之能量密度(充放電容量)降低的問題產生。 An electrode including a metal foil having an active material layer having a large expansion and contraction is included in the battery. When the charge and discharge are repeated several times, the current collector (metal foil) is similarly shrunk, so that wrinkles are easily generated inside. In order to allow wrinkles, it is necessary to design the volume occupied by the electrodes in the battery to have a space elasticity, but relatively, there is a problem that the energy density per unit volume (charge and discharge capacity) is lowered.

由於為了提升單位體積之能量密度(充放電容量),使得對集電體之伸縮之彈性變小,造成集電體無法承受內部應力而破裂,且無法維持穩定之電池特性等等問題。 In order to increase the energy density (charge and discharge capacity) per unit volume, the elasticity of the expansion and contraction of the current collector is reduced, causing the current collector to be unable to withstand internal stress and being broken, and it is impossible to maintain stable battery characteristics and the like.

習知技術文獻 Conventional technical literature

專利文獻 Patent literature

專利文獻1:日本專利第3742144號 Patent Document 1: Japanese Patent No. 3742144

專利文獻2:日本專利第3313277號 Patent Document 2: Japanese Patent No. 3313277

專利文獻3:日本專利公開公報平成第10-255768號 Patent Document 3: Japanese Patent Laid-Open Publication No. 10-255768

專利文獻4:日本專利公開公報第2002-083594號 Patent Document 4: Japanese Patent Laid-Open Publication No. 2002-083594

專利文獻5:日本專利昭和第53-39376號 Patent Document 5: Japanese Patent Showa No. 53-39376

當使用具有將鋰離子二次電池用電極以黑鉛類替代、且對以矽、鍺、或錫為主成分之活性物質進行塗佈、堆疊所形成之金屬箔,作為電極時,隨著充放電反應,活性物質層之體積將會膨脹、收縮,造成集電體(金屬箔)承受相當大的應力,而使集電體產生皺摺等問題。而且,當充 放電重複多次時,集電體少數會有斷裂的問題發生。當集電體產生如皺摺等之物理性的變形時,電池中之電極所佔的面積多少會增加,結果將使單位體積之能量密度降低。 When a metal foil having an electrode for a lithium ion secondary battery replaced with black lead and coated with an active material containing ruthenium, osmium, or tin as a main component is used as an electrode, with charging In the discharge reaction, the volume of the active material layer will expand and contract, causing the collector (metal foil) to withstand considerable stress and causing wrinkles and the like of the current collector. And when charging When the discharge is repeated a plurality of times, a small number of collectors may have a problem of fracture. When the current collector is physically deformed such as wrinkles, the area occupied by the electrodes in the battery is somewhat increased, and as a result, the energy density per unit volume is lowered.

此外,當集電體發生斷裂/龜裂的問題時,不僅無法長時間維持電池的性能,且會有充放電特性(循環特性)降低之問題發生。 Further, when the current collector is cracked/cracked, it is not only impossible to maintain the performance of the battery for a long period of time, but also a problem that the charge and discharge characteristics (cycle characteristics) are lowered.

再者,進行活性物質之塗佈堆疊時,由於矽與錫等粒徑小,當以漿狀於負極集電體上進行塗佈時,難以於正反兩面上,以均勻之厚度、並使其具有適當之接著力來進行塗佈,而且塗佈效率也不佳。尤其,於集電體正反面上表面粗糙度之差異增大時,使於正反兩面上塗佈上均勻厚度之活性物質更加地困難。當無法均勻地進行活性物質之塗佈時,將會對電池的輸出特性與循環特性造成不良的影響。 Further, when the active material is coated and stacked, since the particle size of ruthenium and tin is small, when it is applied to the negative electrode current collector in a slurry form, it is difficult to form a uniform thickness on both sides. It has a suitable adhesion to coat and the coating efficiency is not good. In particular, when the difference in surface roughness between the front and back surfaces of the current collector is increased, it is more difficult to apply a uniform thickness of the active material on both the front and back sides. When the application of the active material is not performed uniformly, it will adversely affect the output characteristics and cycle characteristics of the battery.

因此,本發明之主要目的係提供一種鋰離子二次電池,其係使用於集電體上進行以如矽、鍺或錫等為主成分之活性物質的塗佈、堆疊所形成之負極電極的鋰離子二次電池,集電體將不會發生皺摺等問題,且也不會發生集電體的斷裂,不僅活性物質與集電體間的接著力增加,而且可長時間維持穩定之二次電池特性。又本發明之目的係提供一種作為上述二次電池電極用集電體之金屬箔,特別是提供一種電解銅箔。 Therefore, the main object of the present invention is to provide a lithium ion secondary battery which is used for coating and stacking a negative electrode formed by stacking an active material such as ruthenium, osmium or tin as a main component on a current collector. In a lithium ion secondary battery, the current collector will not cause wrinkles and the like, and the current collector will not be broken, and not only the adhesion between the active material and the current collector will increase, but also the stability can be maintained for a long time. Secondary battery characteristics. Further, an object of the present invention is to provide a metal foil as the current collector for a secondary battery electrode, and in particular to provide an electrolytic copper foil.

同時,本發明之目的係提供一種二次電池電極之集電體用之金屬箔,不僅電解銅箔,即使以與上述電解銅箔相同目的使用來作為鋰離子二次電池用之集電體的金屬箔, 與銅箔相同,於集電體並不會產生皺摺,且也不會發生集電體之斷裂,不僅活性物質與集電體間的接著力增加,更可長時間維持穩定之二次電池特性。 Meanwhile, an object of the present invention is to provide a metal foil for a current collector of a secondary battery electrode, which is used not only as a copper foil but also as a current collector for a lithium ion secondary battery for the same purpose as the above-mentioned electrolytic copper foil. Metal foil, Like the copper foil, wrinkles are not generated in the current collector, and the breakage of the current collector does not occur, and not only the adhesion between the active material and the current collector is increased, but also the stable secondary battery can be maintained for a long time. characteristic.

再者,本發明之一目的係緩和鋰離子二次電池電極之集電體用金屬箔與活性物質間之接著界面間之導電率的差異,提高活性物質層之導電性,並提高鋰離子二次電池之單位體積之能量密度。 Further, an object of the present invention is to reduce the difference in electrical conductivity between the interface between the metal foil for a current collector of a lithium ion secondary battery electrode and an active material, to improve the conductivity of the active material layer, and to improve lithium ion II. The energy density per unit volume of the secondary battery.

此外,本發明之目的係提供一種鋰離子二次電池,係使用具有於集電體(金屬箔)上進行以如矽、鍺或錫等為主成分之活性物質的塗佈、堆疊所形成之活性物質層之金屬箔,來作為電極之鋰離子二次電池,於集電體中並不會產生皺摺,且也不會發生集電體之斷裂,不僅活性物質與集電體間(金屬箔)的接著力增加,更可長時間維持穩定之二次電池特性。本發明之另一目的則係提供一種具有作為上述二次電池電極用之活性物質層之金屬箔。 Further, an object of the present invention is to provide a lithium ion secondary battery which is formed by coating and stacking an active material having a main component such as ruthenium, iridium or tin on a current collector (metal foil). The metal foil of the active material layer, the lithium ion secondary battery used as the electrode, does not wrinkle in the current collector, and the fracture of the current collector does not occur, not only between the active material and the current collector (metal The adhesion of the foil) is increased, and stable secondary battery characteristics can be maintained for a long time. Another object of the present invention is to provide a metal foil having an active material layer for the above secondary battery electrode.

本發明之具有被覆層之金屬箔係於未處理金屬箔之至少一表面上配置被覆層,上述被覆層中包含游離金屬粒子。 In the metal foil having a coating layer of the present invention, a coating layer is disposed on at least one surface of the untreated metal foil, and the coating layer contains free metal particles.

上述被覆層較佳為包含游離金屬粒子之可再熔之樹脂組成物。 The coating layer is preferably a remeltable resin composition containing free metal particles.

此外,上述被覆層較佳為包含游離金屬粒子之活性物質層。 Further, the coating layer is preferably an active material layer containing free metal particles.

上述被覆層較佳為包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上方較佳配置有活性物質 層。 Preferably, the coating layer is a remeltable resin composition layer containing free metal particles, and an active material is preferably disposed above the resin composition layer. Floor.

一種具有被覆層之金屬箔,包括:粗糙化處理層,配置於金屬箔之至少一表面上;被覆層,配置於上述粗糙化處理層上,上述被覆層中包含游離金屬粒子。 A metal foil having a coating layer comprising: a roughening treatment layer disposed on at least one surface of the metal foil; and a coating layer disposed on the roughening treatment layer, wherein the coating layer contains free metal particles.

本發明之具有被覆層之金屬箔,包括:配置於未處理之金屬箔之至少一表面上之粗糙化處理層、及配置於上述粗糙化處理層上之被覆層,上述被覆層中包含游離金屬粒子。 The metal foil with a coating layer of the present invention includes: a roughened layer disposed on at least one surface of the untreated metal foil; and a coating layer disposed on the roughened layer, wherein the coating layer contains free metal particle.

上述被覆層中所包含之游離金屬粒子,較佳係由上述粗糙化處理層中所游離出之金屬粒子。 The free metal particles contained in the coating layer are preferably metal particles liberated from the roughened layer.

配置於上述粗糙化處理層上之被覆層較佳為可再熔之樹脂組成物。 The coating layer disposed on the roughening treatment layer is preferably a remeltable resin composition.

此外,配置於上述粗糙化處理層上之被覆層較佳為活性物質層。 Further, the coating layer disposed on the roughening treatment layer is preferably an active material layer.

又配置於上述粗糙化處理層上之被覆層較佳為可再熔之樹脂組成物層,又於上述樹脂組成物層上方配置有活性物質層。 Further, the coating layer disposed on the roughening layer is preferably a remeltable resin composition layer, and an active material layer is disposed above the resin composition layer.

上述游離金屬粒子之粒徑較佳為0.05 μm~3.5 μm。 The particle diameter of the above free metal particles is preferably from 0.05 μm to 3.5 μm.

上述粗糙化處理層較佳為包含銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦中至少一種以上之金屬之粗糙化處理層。 The roughened layer is preferably a roughened layer containing at least one of copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium.

上述具有被覆層之金屬箔之至少最外層之表面上,較佳配置有薄膜或脫模紙。 Preferably, a film or a release paper is disposed on the surface of at least the outermost layer of the metal foil having the coating layer.

本發明之二次電池用電極,於金屬箔之至少一表面上 配置有活性物質層,上述活性物質層中包含游離金屬粒子。 The electrode for a secondary battery of the present invention, on at least one surface of the metal foil An active material layer is disposed, and the active material layer contains free metal particles.

本發明之二次電池用電極,於金屬箔之至少一表面上配置有包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 In the electrode for a secondary battery of the present invention, a remeltable resin composition layer containing free metal particles is disposed on at least one surface of the metal foil, and an active material layer is disposed on the resin composition layer.

本發明之二次電池用電極,較佳於金屬箔之至少一表面上配置有粗糙化處理層,於上述粗糙化處理層上配置有活性物質層,上述活性物質層中包含游離金屬粒子。 In the electrode for a secondary battery of the present invention, it is preferable that a roughening treatment layer is disposed on at least one surface of the metal foil, and an active material layer is disposed on the roughening treatment layer, and the active material layer contains free metal particles.

本發明之二次電池用電極,於金屬箔之至少一表面上配置有粗糙化處理層,於上述粗糙化處理層上配置有包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 In the electrode for a secondary battery of the present invention, a roughening treatment layer is disposed on at least one surface of the metal foil, and a remeltable resin composition layer containing free metal particles is disposed on the roughening treatment layer. An active material layer is disposed on the composition layer.

本發明之二次電池用電極,於金屬箔之至少一表面上配置有粗糙化處理層,於上述粗糙化處理層上配置有包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 In the electrode for a secondary battery of the present invention, a roughening treatment layer is disposed on at least one surface of the metal foil, and a remeltable resin composition layer containing free metal particles is disposed on the roughening treatment layer. An active material layer is disposed on the composition layer.

上述游離金屬粒子之粒徑較佳為0.05 μm~3.5 μm。 The particle diameter of the above free metal particles is preferably from 0.05 μm to 3.5 μm.

上述粗糙化處理層較佳為以包含銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦中至少一種以上之金屬之電鍍槽,進行處理所形成之粗糙化處理層。 The roughened layer is preferably a roughened layer formed by treating a plating bath containing at least one of copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium.

二次電池用電極之至少最外層之表面上,較佳配置有薄膜或脫模紙。 On the surface of at least the outermost layer of the electrode for a secondary battery, a film or a release paper is preferably disposed.

本發明之具有被覆層之金屬箔之製造方法,係於未處理之金屬箔之至少一表面上配置有被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔之製造方法,包 括:對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上形成被覆層;及於被覆層中混入一部份之上述粗糙化處理粒子,以作為游離金屬粒子。 A method for producing a metal foil having a coating layer according to the present invention is a method for producing a metal foil having a coating layer containing at least one surface of an untreated metal foil, wherein the coating layer contains free metal particles, and a coating method a method for forming a roughened layer having a particle diameter of 0.1 μm to 3.5 μm by using a plating bath and a current exceeding a limiting current density on a surface of the metal foil; forming a coating layer on the roughened layer; A part of the roughened particles are mixed in the coating layer as free metal particles.

上述被覆層較佳為可再熔之樹脂組成物層。 The coating layer is preferably a remeltable resin composition layer.

此外,上述被覆層較佳為活性物質層。 Further, the coating layer is preferably an active material layer.

此外,上述被覆層較佳為可再熔之樹脂組成物層,於上述樹脂組成物層上較佳配置有活性物質層。 Further, the coating layer is preferably a remeltable resin composition layer, and an active material layer is preferably disposed on the resin composition layer.

本發明之具有被覆層之金屬箔之製造方法,係於未處理之金屬箔之至少一表面上配置有被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔之製造方法,包括:對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上,塗佈上添加有活性物質、黏合劑、必要時可添加增黏劑、與漿體等所混合而成之活性物質混合體,以形成活性物質層;對形成有上述活性物質層之金屬箔,進行乾燥、加壓,以將上述金屬處理粒子帶入活性物質層中,作為導電助劑;及使上述活性物質層中包含上述粗糙化處理粒子,以作為游離金屬粒子。 A method for producing a metal foil having a coating layer according to the present invention is a method for producing a metal foil having a coating layer containing at least one surface of an untreated metal foil, wherein the coating layer contains free metal particles, including : on the surface of the metal foil, using a plating bath and passing a current above a limiting current density to form a roughened layer having a particle diameter of 0.1 μm to 3.5 μm; on the roughened layer, the coating is added with an active layer a substance, a binder, and a mixture of active materials mixed with a slurry or the like may be added as necessary to form an active material layer; and the metal foil on which the active material layer is formed is dried and pressurized. The metal-treated particles are introduced into the active material layer as a conductive auxiliary agent, and the roughened particles are contained in the active material layer as free metal particles.

本發明之具有被覆層之金屬箔之製造方法,係於金屬箔之至少一表面上配置被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔,對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上,形 成樹脂組成物層;於上述樹脂組成物層上,塗佈上添加有活性物質、黏合劑、必要時可添加增黏劑、與漿體等所混合而成之活性物質混合體,以形成活性物質層;及對形成有上述樹脂組成物層、與上述活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入樹脂組成物層中,來作為游離金屬粒子。本發明之實施例雖使用陰極電解電鍍,但陽極電解電鍍也具有同樣的效果。 In the method for producing a metal foil having a coating layer according to the present invention, a coating layer is disposed on at least one surface of the metal foil, and the coating layer includes a metal foil having a coating layer of free metal particles, and a plating tank is used for the surface of the metal foil. And passing a current above a limiting current density to form a roughened layer having a particle diameter of 0.1 μm to 3.5 μm; on the roughened layer, a resin composition layer; an active material mixture in which an active material, a binder, a tackifier, and a slurry are added to the resin composition layer to form an active material; The material layer; and the metal foil having the resin composition layer and the active material layer formed thereon are dried and pressurized to bring the roughened particles into the resin composition layer to form free metal particles. Although the embodiment of the present invention uses cathodic electroplating, the same effect can be obtained by anodic electroplating.

形成於上述粗糙化處理層上之樹脂組成物層較佳為可再熔之樹脂。 The resin composition layer formed on the roughened layer is preferably a remeltable resin.

本發明之二次電池用電極,係利用上述之具有被覆層之金屬箔之製造方法所製造之金屬箔,來作為集電體。 The electrode for a secondary battery of the present invention is a current collector using a metal foil produced by the above-described method for producing a metal foil having a coating layer.

本發明之二次電池用電極之製造方法,包括:表面粗糙化處理步驟,對未處理之金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;活性物質造粒步驟,添加活性物質、黏合劑、必要時可添加增黏劑、與漿體等,進行混合;第一活性物質層形成步驟,於上述粗糙化處理層之一表面上,塗佈上於上述活性物質造粒步驟中所製造之活性物質混合體;第二活性物質層形成步驟,於薄膜上層積上述活性物質混合體,並層積於金屬箔之另一表面上;及乾燥加壓步驟,對具有以上述第一、與第二步驟中所形成之活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入活性物質層中,來作為導電助劑,上述粗糙化處理粒子將作為游離金屬粒子,包含於活性物質層中。 A method for producing an electrode for a secondary battery according to the present invention comprises: a surface roughening treatment step of forming a particle diameter of 0.1 μm by using a plating bath and a current exceeding a limit current density on an untreated metal foil surface; 3.5 μm roughening treatment layer; active material granulation step, adding active material, binder, if necessary, adding tackifier, and slurry, etc.; mixing; first active material layer forming step, in the above roughening treatment a surface of one of the layers coated with the active material mixture produced in the granulation step of the active material; a second active material layer forming step of laminating the active material mixture on the film and laminating it on the metal foil And drying and pressurizing the metal foil having the active material layer formed in the first and second steps, and drying, to bring the roughened particles into the active material In the layer, as the conductive auxiliary agent, the roughened particles are contained as free metal particles in the active material layer.

本發明之二次電池用電極之製造方法,包括:表面粗糙化處理步驟(以下稱為燒焦電鍍),對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;樹脂組成物層形成步驟,於上述粗糙化處理層上形成樹脂組成物層;活性物質造粒步驟,添加活性物質、黏合劑、必要時可添加增黏劑、與漿體等,進行混合;第一活性物質層形成步驟,於上述樹脂組成物層之一表面上,塗佈上於上述活性物質造粒步驟中所製造之活性物質混合體;第二活性物質層形成步驟,於薄膜上層積上述活性物質混合體,並層積於樹脂組成物層之另一表面上;及乾燥加壓步驟,對具有以上述第一、與第二步驟中所形成之活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入活性物質層中,來作為導電助劑,上述粗糙化處理粒子將作為游離金屬粒子,包含於活性物質層中。 A method for producing an electrode for a secondary battery according to the present invention includes a surface roughening treatment step (hereinafter referred to as "scorch plating"), and a surface of the metal foil is formed by using a plating bath and a current having a limit current density or more to form a pellet a roughening treatment layer having a diameter of 0.1 μm to 3.5 μm; a resin composition layer forming step, forming a resin composition layer on the roughening treatment layer; an active material granulation step, adding an active material, a binder, and adding if necessary a tackifier, a slurry, and the like; a first active material layer forming step, coated on the surface of one of the resin composition layers, and coated with the active material mixture produced in the active material granulation step; a second active material layer forming step of laminating the active material mixture on the film and laminating on the other surface of the resin composition layer; and drying and pressurizing the step, having the first step and the second step The metal foil of the formed active material layer is dried and pressurized to bring the roughened particles into the active material layer to serve as a conductive auxiliary agent, and the above roughening Physical particles as free metal particles contained in the active material layer.

上述樹脂組成物較佳為可再熔之樹脂組成物。 The above resin composition is preferably a remeltable resin composition.

本發明之鋰離子二次電池,係組裝上述電極之二次電池。 The lithium ion secondary battery of the present invention is a secondary battery in which the above electrodes are assembled.

本發明之具有被覆層之金屬箔,由於於金屬箔表面上形成游離金屬離子混入之可再熔樹脂組成層的被覆層,因此可提高例如形成於該被覆層表面上活性物質層間之接著性,且具有可緩和金屬箔與活性物質層間之電解等之優良的效果。 In the metal foil having a coating layer of the present invention, since a coating layer of a remeltable resin composition layer in which free metal ions are mixed is formed on the surface of the metal foil, for example, adhesion between the active material layers formed on the surface of the coating layer can be improved. Further, it has an excellent effect of alleviating electrolysis or the like between the metal foil and the active material layer.

根據本發明之鋰離子二次電池電極之集電體用金屬箔,當以該金屬箔作為集電體時,由於將構成粗糙化處理層之金屬混入活性物質層,因此可提高導電性,而且也具有提高鋰離子二次電池之單位體積之能量密度的效果。 According to the metal foil for a current collector of the lithium ion secondary battery electrode of the present invention, when the metal foil is used as a current collector, since the metal constituting the roughened layer is mixed into the active material layer, conductivity can be improved, and It also has an effect of increasing the energy density per unit volume of the lithium ion secondary battery.

此外,當本發明之金屬箔用來作為集電體時,可抑制因充放電時所產生之活性物質之膨脹收縮所造成之皺摺等的發生,而且可提升鋰離子二次電池之單位體積之能量密度。又本發明可提供一種集電體不會因應力產生斷裂、且因活性物質與集電體間的接著力增加,而具有長時間維持穩定之輸出性能之鋰離子二次電池電極之集電體用金屬箔。 Further, when the metal foil of the present invention is used as a current collector, occurrence of wrinkles or the like due to expansion and contraction of the active material generated during charge and discharge can be suppressed, and the unit volume of the lithium ion secondary battery can be improved. Energy density. Further, the present invention can provide a current collector of a lithium ion secondary battery electrode having a current collector which is not broken by stress and which has an increased output force due to an increase in the adhesion between the active material and the current collector. Use metal foil.

本發明之鋰離子二次電池,由於於該電池之負極使用金屬箔,因此於集電體並不會因充放電產生皺摺,而可提高鋰離子二次電池之單位體積之能量密度,此外,本發明可提供一種集電體不會因應力產生斷裂、且因活性物質與集電體間的接著力增加,而具有長時間維持穩定之輸出性能的鋰離子二次電池電極。 In the lithium ion secondary battery of the present invention, since the metal foil is used for the negative electrode of the battery, the current collector does not wrinkle due to charge and discharge, and the energy density per unit volume of the lithium ion secondary battery can be increased. According to the present invention, it is possible to provide a lithium ion secondary battery electrode which has a stable output performance for a long period of time without causing breakage due to stress and an increase in adhesion between the active material and the current collector.

第一實施形態 First embodiment

以下將依照圖1中所繪示之本發明第一實施形態之具有被覆層之金屬箔之製造流程圖來進行說明。 Hereinafter, a manufacturing flowchart of a metal foil having a coating layer according to the first embodiment of the present invention shown in Fig. 1 will be described.

步驟1(游離金屬粒子之製備) Step 1 (Preparation of free metal particles)

製備包括銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦之金 屬粒子。金屬粒子之粒徑較佳為0.1 μm~3.5 μm之範圍。金屬粒子可根據所混入之下述樹脂組成物之導電率,來選擇使用1種或2種以上的組合。 Preparation of gold including copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, indium Is a particle. The particle diameter of the metal particles is preferably in the range of 0.1 μm to 3.5 μm. The metal particles can be selected from one or a combination of two or more kinds depending on the conductivity of the following resin composition to be mixed.

步驟2(可再熔之樹脂組成物之製備) Step 2 (Preparation of Remeltable Resin Composition)

製備可再熔之樹脂組成物。可再熔之樹脂組成物可使用一般市售之熱可塑性樹脂組成物〔例如聚偏氯乙烯樹脂(以下稱為PVDF)〕、與熱硬化性樹脂組成物〔例如熱硬化性聚亞醯胺樹脂〕。 A remeltable resin composition is prepared. As the remeltable resin composition, a commercially available thermoplastic resin composition (for example, polyvinylidene chloride resin (hereinafter referred to as PVDF)) and a thermosetting resin composition (for example, a thermosetting polyamidamide resin) can be used. ].

此外,本實施形態較佳係選擇於樹脂組成物層上設有後述活性物質層、與可接著之樹脂組成物層。 Further, in the present embodiment, it is preferable to provide an active material layer to be described later and a resin composition layer which can be subsequently provided on the resin composition layer.

步驟3(具有導電性之樹脂組成物之製作) Step 3 (Production of a conductive resin composition)

於步驟2中所選擇之可再熔之樹脂組成物中,混合入於步驟1中所選擇之游離金屬粒子,以製作具有導電性之樹脂組成物。 In the remeltable resin composition selected in the step 2, the free metal particles selected in the step 1 are mixed to prepare a conductive resin composition.

步驟4(被覆) Step 4 (covered)

於金屬箔(銅箔、鋁箔等)之表面上,被覆上於步驟3中所製備之金屬粒子之樹脂組成物。被覆方法可如壓合等方法、或一般之方法等。 The resin composition of the metal particles prepared in the step 3 is coated on the surface of a metal foil (copper foil, aluminum foil, etc.). The coating method may be, for example, a method such as pressing, or a general method.

具體來說,使用熱硬化性聚亞醯胺樹脂之熱硬化性樹脂組成物,以於該樹脂中添加游離金屬粒子之狀態溶解於溶劑中,然後塗佈於金屬箔表面,其後,使溶劑蒸發、乾燥,以使熱硬化性聚亞醯胺樹脂形成B階樹脂,而於金屬箔表面上形成包含游離金屬粒子之可再熔之樹脂層(B階樹脂)。 Specifically, a thermosetting resin composition using a thermosetting polyamidamide resin is dissolved in a solvent in a state in which free metal particles are added to the resin, and then applied to the surface of the metal foil, and thereafter, a solvent is used. Evaporation and drying are performed so that the thermosetting polyimide resin forms a B-stage resin, and a remeltable resin layer (B-stage resin) containing free metal particles is formed on the surface of the metal foil.

抑或是將包含游離金屬粒子之樹脂組成物形成板狀,於金屬箔表面上,以壓合等方法進行壓合,以形成具有被覆層之金屬箔。 Alternatively, the resin composition containing the free metal particles is formed into a plate shape, and is pressed on the surface of the metal foil by press bonding or the like to form a metal foil having a coating layer.

以上述步驟,可製造具有包含游離金屬粒子之可再熔之樹脂組成物層(被覆層)之金屬箔。 In the above steps, a metal foil having a remeltable resin composition layer (coating layer) containing free metal particles can be produced.

圖2係繪示具有於金屬箔10之兩表面上設有可再熔之樹脂組成物層11、12之被覆層的金屬箔10之剖面圖。如圖所示,被覆層11、12中分散有游離金屬粒子。 2 is a cross-sectional view showing the metal foil 10 having a coating layer on which the refusible resin composition layers 11, 12 are provided on both surfaces of the metal foil 10. As shown in the figure, free metal particles are dispersed in the coating layers 11 and 12.

圖2中繪示金屬箔10之兩表面上設置有組成物層11、12,若僅以單一表面即能滿足之情形,則不需要於兩方的表面上設置組成物層。 In Fig. 2, the composition layers 11, 12 are provided on both surfaces of the metal foil 10. If only a single surface can be satisfied, it is not necessary to provide a composition layer on both surfaces.

第二實施形態 Second embodiment

以下將依照圖3中所繪示之本發明第二實施形態之具有被覆層之金屬箔之製造流程圖來進行說明。 Hereinafter, a manufacturing flowchart of a metal foil having a coating layer according to a second embodiment of the present invention shown in FIG. 3 will be described.

步驟21(游離金屬粒子之製備) Step 21 (Preparation of free metal particles)

製備包括銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦之金屬粒子。金屬粒子之粒徑較佳為0.1 μm~3.5 μm之範圍。金屬粒子可根據所混入之活性物質層之導電率,來選擇使用1種或2種以上的組合。 Metal particles including copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium are prepared. The particle diameter of the metal particles is preferably in the range of 0.1 μm to 3.5 μm. The metal particles may be selected from one or a combination of two or more depending on the conductivity of the active material layer to be mixed.

步驟22(活性物質混合體之製作步驟) Step 22 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑、或增黏劑、與漿體,以形成活性物質混合體。此外,當形成活性物質混合體時,可例如混入作為黏合劑之聚亞醯胺。 The active material, the binder, and, if necessary, conductive carbon black, or a tackifier, and a slurry may be added to form an active material mixture. Further, when the active material mixture is formed, for example, polyimide as a binder may be mixed.

步驟23(混合) Step 23 (mixed)

於步驟2中所製作之活性物質混合體中,混合入於步驟1之游離金屬粒子,以對活性物質層賦予導電性。 In the active material mixture prepared in the step 2, the free metal particles in the step 1 are mixed to impart conductivity to the active material layer.

步驟24(被覆) Step 24 (covered)

於金屬箔(銅箔、鋁箔等)30之單一表面上,進行於步驟3中所混合製備之活性物質混合體之塗佈、被覆。被覆方法可例如使用壓合等方法、或一般之方法等。 The coating and coating of the active material mixture prepared in the step 3 are carried out on a single surface of a metal foil (copper foil, aluminum foil, etc.) 30. The coating method can be, for example, a method such as press bonding, a general method, or the like.

以上述步驟,可製造具有包含游離金屬粒子之可再熔之樹脂組成物層(被覆層)之金屬箔。 In the above steps, a metal foil having a remeltable resin composition layer (coating layer) containing free metal particles can be produced.

圖4係繪示具有於金屬箔30之單一表面上設有活性物質層32之被覆層的金屬箔之剖面圖。如圖所示,於被覆層(活性物質層)32中,游離金屬粒子34分散於活性物質33之間隙中。 4 is a cross-sectional view showing a metal foil having a coating layer on which a layer of the active material layer 32 is provided on a single surface of the metal foil 30. As shown in the figure, in the coating layer (active material layer) 32, the free metal particles 34 are dispersed in the gap of the active material 33.

此外,圖4係繪示於金屬箔30之單一表面上設置活性物質層32,若需要於兩方表面上設置之情形時,則可以以下之步驟,於金屬箔之兩表面上設置活性物質層。 In addition, FIG. 4 illustrates that the active material layer 32 is disposed on a single surface of the metal foil 30. If it is required to be disposed on both surfaces, the active material layer may be disposed on both surfaces of the metal foil in the following steps. .

步驟25(被覆) Step 25 (covered)

於金屬箔(銅箔、鋁箔等)之另一表面上,進行步驟3之活性物質混合體的塗佈、被覆。被覆方法可例如使用壓合方法、或一般之方法等。 Applying and coating the active material mixture of the step 3 on the other surface of the metal foil (copper foil, aluminum foil, etc.). The coating method can be, for example, a press-bonding method, a general method, or the like.

以上述步驟,可製造於單一表面、或兩表面上具有包含游離金屬粒子之活性物質層(被覆層)之金屬箔。 In the above steps, a metal foil having an active material layer (coating layer) containing free metal particles on a single surface or both surfaces can be produced.

第三實施形態 Third embodiment

以下將依照圖5中所繪示之本發明第三實施形態之具有被覆層之金屬箔之製造流程圖來進行說明。 Hereinafter, a manufacturing flowchart of a metal foil having a coating layer according to a third embodiment of the present invention shown in FIG. 5 will be described.

步驟31(游離金屬粒子之製備) Step 31 (Preparation of free metal particles)

製備包括銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦之金屬粒子。金屬粒子之粒徑較佳為0.1 μm~3.5 μm之範圍。金屬粒子可根據所混入之後述之樹脂組成物之導電率,來選擇使用1種或2種以上的組合。 Metal particles including copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium are prepared. The particle diameter of the metal particles is preferably in the range of 0.1 μm to 3.5 μm. The metal particles can be selected from one type or a combination of two or more types depending on the conductivity of the resin composition to be described later.

步驟32(可再熔之樹脂組成物之製備) Step 32 (Preparation of Remeltable Resin Composition)

製備可再熔之樹脂組成物。可再熔之樹脂組成物可使用一般市售之熱可塑性樹脂組成物〔例如聚偏氯乙烯樹脂(以下稱為PVDF)〕、與熱硬化性樹脂組成物〔例如熱硬化性聚亞醯胺樹脂〕。 A remeltable resin composition is prepared. As the remeltable resin composition, a commercially available thermoplastic resin composition (for example, polyvinylidene chloride resin (hereinafter referred to as PVDF)) and a thermosetting resin composition (for example, a thermosetting polyamidamide resin) can be used. ].

此外,本實施形態較佳係選擇於樹脂組成物層上設有後述活性物質層、與可接著之樹脂組成物。 Further, in the present embodiment, it is preferable to select an active material layer to be described later and a resin composition which can be attached to the resin composition layer.

步驟33(混合) Step 33 (mixed)

於步驟32中所選擇之可再熔之樹脂組成物中,混合入於步驟31中所選擇之金屬粒子,以製備具有導電性之樹脂組成物。 The metal particles selected in the step 31 are mixed in the remeltable resin composition selected in the step 32 to prepare a conductive resin composition.

步驟34(被覆) Step 34 (covered)

於金屬箔(銅箔、鋁箔等)之表面上,進行於步驟3中混合金屬粒子樹脂組成物之被覆。被覆方法可例如使用壓合等方法、或一般之方法等。 On the surface of the metal foil (copper foil, aluminum foil, etc.), the coating of the metal particle resin composition is mixed in the step 3. The coating method can be, for example, a method such as press bonding, a general method, or the like.

具體來說,使用熱硬化性聚亞醯胺樹脂之熱硬化性樹脂組成物,以於該樹脂中添加游離金屬粒子之狀態溶解於溶劑中,然後塗佈於金屬箔表面,其後,使溶劑蒸發、乾燥,以使熱硬化性聚亞醯胺樹脂形成B階樹脂,而於金屬 箔表面上形成包含游離金屬粒子之可再熔之樹脂層(B階樹脂)。 Specifically, a thermosetting resin composition using a thermosetting polyamidamide resin is dissolved in a solvent in a state in which free metal particles are added to the resin, and then applied to the surface of the metal foil, and thereafter, a solvent is used. Evaporation and drying to form a thermosetting polyamido resin to form a B-stage resin, and to a metal A remeltable resin layer (B-stage resin) containing free metal particles is formed on the surface of the foil.

步驟35(活性物質混合體之製作步驟) Step 35 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑、或增黏劑、與漿體,以製成活性物質混合體。此外,當形成活性物質混合體時,可例如混入作為黏合劑之聚亞醯胺。 The active material, the binder, and, if necessary, conductive carbon black, or a tackifier, and a slurry may be added to form an active material mixture. Further, when the active material mixture is formed, for example, polyimide as a binder may be mixed.

步驟36(活性物質之形成) Step 36 (formation of active substances)

於步驟34中所形成之樹脂組成物層(被覆層)上,以步驟35中所製備之活性物質混合體,來形成活性物質層。 The active material layer is formed on the resin composition layer (coating layer) formed in the step 34 by using the active material mixture prepared in the step 35.

圖6係繪示具有於金屬箔30之單一表面上設有樹脂組成物層,於該組成物層表面上設有活性物質層32之被覆層的金屬箔之剖面圖。如圖所示,於組成物層中分散有游離金屬粒子33,於其上之活性物質層32中也分散有一部份之游離金屬粒子。 Fig. 6 is a cross-sectional view showing a metal foil having a resin composition layer provided on a single surface of the metal foil 30 and a coating layer of the active material layer 32 on the surface of the composition layer. As shown in the figure, free metal particles 33 are dispersed in the composition layer, and a part of the free metal particles are also dispersed in the active material layer 32 thereon.

此外,於圖中,37為黏合劑。 Further, in the figure, 37 is a binder.

於圖4中係繪示於金屬箔30之單一表面上,設置組成物層、活性物質層32,但若必要於兩方表面上設置時,可於兩表面上設置組成物層、與活性物質層。 4, the composition layer and the active material layer 32 are provided on a single surface of the metal foil 30, but if necessary, the composition layer and the active material may be disposed on both surfaces. Floor.

步驟37(電極之製作) Step 37 (Production of Electrode)

將具有以步驟35所製作之活性物質層之金屬箔,製作成電極用。 A metal foil having the active material layer produced in the step 35 was used for the electrode.

步驟38(電池之製作) Step 38 (Production of the battery)

將以步驟36所製作之電極,製作成具有正極與負極之電池。 The electrode prepared in the step 36 was fabricated into a battery having a positive electrode and a negative electrode.

第四實施形態 Fourth embodiment

以下將依照圖7中所繪示之本發明第四實施形態之具有被覆層之金屬箔之製造流程圖、及圖8所繪示之製造裝置來進行說明。 Hereinafter, a manufacturing flow chart of a metal foil having a coating layer according to a fourth embodiment of the present invention shown in FIG. 7 and a manufacturing apparatus shown in FIG. 8 will be described.

步驟41(表面粗糙化處理步驟) Step 41 (surface roughening treatment step)

如圖8所示,將金屬箔1導入於表面粗糙化處理槽2中,以電鍍於金屬箔1之表面上成長金屬粒子,以形成粗糙化金屬層3。 As shown in FIG. 8, the metal foil 1 is introduced into the surface roughening treatment tank 2, and metal particles are grown on the surface of the metal foil 1 to form the roughened metal layer 3.

如圖8所示,金屬箔1藉由給電電極20導入表面粗糙化處理槽2,並使其通過配置於表面粗糙化處理槽2中之電鍍用電極22、24、26。圖8中於3處配置電鍍用電極22、24、26,以對金屬箔1之兩表面進行粗糙化處理,若僅於單一表面上進行粗糙化處理的話,可例如省略電極26。粗糙化處理之條件等將說明如後。 As shown in FIG. 8, the metal foil 1 is introduced into the surface roughening treatment tank 2 by the feeding electrode 20, and passes through the plating electrodes 22, 24, 26 disposed in the surface roughening treatment tank 2. In FIG. 8, the plating electrodes 22, 24, and 26 are disposed at three places to roughen the both surfaces of the metal foil 1, and if the roughening treatment is performed only on a single surface, the electrode 26 can be omitted, for example. The conditions of the roughening treatment and the like will be explained later.

接著,導入於水洗處理槽4中進行粗糙化金屬層3之水洗。 Next, it is introduced into the water washing treatment tank 4 to perform water washing of the roughened metal layer 3.

將水洗之金屬箔再導入防鏽處理槽5,以對粗糙化金屬層3表面塗佈防鏽劑。若無粗糙化金屬層氧化之虞慮的話,則可省略此防鏽處理。 The water-washed metal foil is further introduced into the rust-preventing treatment tank 5 to apply a rust preventive agent to the surface of the roughened metal layer 3. This rust-preventing treatment can be omitted if there is no concern about the oxidation of the roughened metal layer.

步驟42(可再熔之樹脂組成物之製備) Step 42 (Preparation of Remeltable Resin Composition)

於金屬箔(銅箔、鋁箔等)之表面上,以步驟2形成粗糙化處理層之表面上被覆樹脂組成物。被覆方法可如壓合等方法、或一般之方法等。此處係以如圖8所示,將樹脂組成物溶於溶劑中,於步驟41中進行粗糙化處理之金屬 箔表面上進行塗佈之方法來進行說明。 On the surface of the metal foil (copper foil, aluminum foil, etc.), the resin composition is coated on the surface of the roughened layer formed in step 2. The coating method may be, for example, a method such as pressing, or a general method. Here, as shown in FIG. 8, the resin composition is dissolved in a solvent, and the metal is roughened in step 41. The method of coating on the surface of the foil will be described.

如圖8所示,將樹脂組成物溶解於溶劑中,並填充於容器6中。將設置有防鏽層之金屬箔導入容器6(裝滿溶解於溶劑中之樹脂組成物)中,將由樹脂組成物組成之溶液塗佈於表面上。 As shown in FIG. 8, the resin composition was dissolved in a solvent and filled in the container 6. The metal foil provided with the rustproof layer is introduced into the container 6 (filled with the resin composition dissolved in the solvent), and a solution composed of the resin composition is applied onto the surface.

步驟43(乾燥步驟) Step 43 (drying step)

於金屬箔表面上塗佈樹脂組成物之後,於溶劑蒸發裝置8中將溶劑蒸發,以進行乾燥。 After the resin composition is coated on the surface of the metal foil, the solvent is evaporated in the solvent evaporation device 8 to be dried.

步驟44(捲取步驟) Step 44 (rolling step)

將乾燥之具有樹脂組成物層之金屬箔以捲取機11進行捲取。於此製造步驟、或其後之步驟中,使一部份之粗糙化粒子進入樹脂組成物中,如圖4所示,可於金屬箔表面上形成包含金屬粒子之可再熔之樹脂層(B階樹脂)。 The dried metal foil having the resin composition layer is taken up by a coiler 11. In the manufacturing step or the subsequent step, a part of the roughened particles are introduced into the resin composition, and as shown in FIG. 4, a remeltable resin layer containing metal particles may be formed on the surface of the metal foil ( B-stage resin).

以下參照圖8,將對步驟42中之可再熔之樹脂組成物層之形成步驟,作更進一步詳細的說明。以上述電鍍法所形成之粗糙化處理層,較佳係以燒焦電鍍來進行粗糙化處理。實施燒焦電鍍之粗糙化處理層,其於該狀態下維持粗糙化粒子易脫落(粉末脫落)之不健全狀態。於此狀態下,可將金屬箔浸泡、通過於以例如聚偏氯乙烯樹脂(以下稱為PVDF)溶解於1-甲基-2-吡咯烷酮(NMD)溶劑所形成之溶液的儲槽6。PVDF之重量比可藉由適當地調整溶劑之濃度,來控制其附著量。然後,以所需之特定時間進行乾燥,使溶劑蒸發,於金屬箔表面上所附著之樹脂,其粗糙化粒子不會脫落,而會形成具有樹脂組成物之粗糙化銅箔。 The formation step of the remeltable resin composition layer in the step 42 will be described in further detail below with reference to FIG. The roughened layer formed by the above plating method is preferably subjected to a roughening treatment by scorching plating. The roughened layer of the burnt plating is subjected to an unsound state in which the roughened particles are easily peeled off (powder off) in this state. In this state, the metal foil may be immersed in a storage tank 6 of a solution formed by dissolving, for example, polyvinylidene chloride resin (hereinafter referred to as PVDF) in a solvent of 1-methyl-2-pyrrolidone (NMD). The weight ratio of PVDF can be controlled by appropriately adjusting the concentration of the solvent. Then, it is dried at a specific time required to evaporate the solvent, and the resin adhering to the surface of the metal foil does not fall off the roughened particles, and a roughened copper foil having a resin composition is formed.

此外,可再熔之樹脂組成物層採用熱硬化性聚亞醯胺樹脂時,將聚亞醯胺,調整其重量比,溶解於適當之溶劑中,以相同於上述方式,將實施上述燒焦電鍍之粗糙化處理狀態之銅箔,浸泡、並通過於溶液之容器6。其後,為了將熱硬化性聚亞醯胺樹脂形成B階樹脂,以所需之特定時間將溶劑蒸發,進行乾燥,使其附著於銅箔表面。如此,可製造粗糙化粒子混入B階樹脂之具有被覆層之金屬箔。 Further, when the remeltable resin composition layer is a thermosetting polyimide resin, the polyamidene is adjusted in a weight ratio and dissolved in a suitable solvent, and the above-mentioned scorching is carried out in the same manner as described above. The copper foil in the roughened state of electroplating is immersed and passed through the container 6 of the solution. Thereafter, in order to form a thermosetting polyimine resin into a B-stage resin, the solvent is evaporated at a desired specific time, and dried to adhere to the surface of the copper foil. Thus, a metal foil having a coating layer in which roughened particles are mixed with a B-stage resin can be produced.

本發明於以易脆狀態所附著之樹枝狀粗糙化粒子層上,進行樹脂組成物之塗佈、乾燥。樹枝狀之粗糙化粒子於樹脂組成物之塗佈時、或乾燥時之膨脹收縮中、抑或是其後之步驟中將被破壞,所破壞之粒子如圖4所示分散於樹脂組成物層中,而進入樹脂組成物層中。 In the present invention, the resin composition is applied and dried on a dendritic roughened particle layer adhered in a fragile state. The dendritic roughened particles are destroyed during the coating of the resin composition, or during the expansion and contraction during drying, or in the subsequent steps, and the damaged particles are dispersed in the resin composition layer as shown in FIG. And enter the resin composition layer.

第五實施形態 Fifth embodiment

以下將依照圖9中所繪示之本發明第五實施形態之具有被覆層之金屬箔之製造流程圖、及圖10所繪示之製造裝置來進行說明。 Hereinafter, a manufacturing flow chart of a metal foil having a coating layer according to a fifth embodiment of the present invention shown in FIG. 9 and a manufacturing apparatus shown in FIG. 10 will be described.

步驟51(表面粗糙化處理步驟) Step 51 (surface roughening treatment step)

如圖9所示,將金屬箔1導入於表面粗糙化處理槽2中,以電鍍於金屬箔1之表面上成長金屬粒子,以形成粗糙化金屬層3。 As shown in FIG. 9, the metal foil 1 is introduced into the surface roughening treatment tank 2, and metal particles are grown on the surface of the metal foil 1 to form the roughened metal layer 3.

如圖10所示,金屬箔1藉由給電電極20導入表面粗糙化處理槽2,並使其通過配置於表面粗糙化處理槽2中之電鍍用電極22、24、26。圖10中於3處配置電鍍用電極22、24、26,以對金屬箔1之兩表面進行粗糙化處理, 若僅於單一表面上進行粗糙化處理的話,可例如省略電極26。粗糙化處理之條件等將說明如後。 As shown in FIG. 10, the metal foil 1 is introduced into the surface roughening treatment tank 2 by the feeding electrode 20, and passes through the plating electrodes 22, 24, 26 disposed in the surface roughening treatment tank 2. In FIG. 10, plating electrodes 22, 24, and 26 are disposed at three places to roughen both surfaces of the metal foil 1, If the roughening treatment is performed only on a single surface, the electrode 26 can be omitted, for example. The conditions of the roughening treatment and the like will be explained later.

接著,導入於水洗處理槽4中進行粗糙化金屬層3之水洗。 Next, it is introduced into the water washing treatment tank 4 to perform water washing of the roughened metal layer 3.

將水洗之金屬箔再導入防鏽處理槽5,對粗糙化金屬層3表面塗佈防鏽劑。若無粗糙化金屬層氧化之虞慮的話,則可省略此防鏽處理。 The water-washed metal foil is further introduced into the rust-preventing treatment tank 5, and the surface of the roughened metal layer 3 is coated with a rust preventive agent. This rust-preventing treatment can be omitted if there is no concern about the oxidation of the roughened metal layer.

步驟52(活性物質混合體之製作步驟) Step 52 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑或增黏劑、與漿體,以製成活性物質混合體8,然後將活性物質混合體8供給於儲料槽6、7。 The active material, the binder, and, if necessary, a conductive carbon black or a tackifier, and a slurry may be added to form the active material mixture 8, and then the active material mixture 8 is supplied to the storage tanks 6, 7.

當活性物質層形成時,較佳係例如使用聚亞醯胺來作為黏合劑,以形成均質之漿體塗佈層。 When the active material layer is formed, it is preferred to use, for example, polymethyleneamine as a binder to form a homogeneous slurry coating layer.

步驟53(第一活性物質層形成步驟) Step 53 (first active material layer forming step)

必要時可對進行上述表面粗糙化處理之金屬箔表面,以防鏽處理層5進行防鏽處理,由儲料槽6均勻地於另一表面上流入活性物質混合體8,然後以乾燥裝置9進行活性物質混合體8之乾燥,以形成活性物質層31。 If necessary, the surface of the metal foil subjected to the surface roughening treatment may be subjected to rustproof treatment by the rust-preventing treatment layer 5, and the active material mixture 8 may be uniformly flowed from the hopper 6 on the other surface, and then dried. Drying of the active material mixture 8 is performed to form the active material layer 31.

步驟54(第二活性物質層形成步驟) Step 54 (second active material layer forming step)

接著,由儲料槽7均勻地於另一表面上流入活性物質混合體8,然後以乾燥裝置10進行活性物質混合體8之乾燥,以形成活性物質層32。 Next, the active material mixture 8 is uniformly flowed from the hopper 7 on the other surface, and then the active material mixture 8 is dried by the drying device 10 to form the active material layer 32.

步驟55(乾燥‧加壓步驟) Step 55 (drying ‧ pressurization step)

使兩表面上形成有活性物質層31、32之具有活性物質 層之金屬箔通過壓合機11,進行加熱、加壓。藉此加熱、加壓步驟,活性物質層31、32將均勻地密著於金屬箔表面,而且藉此加壓步驟迫使粗糙化粒子移動,如圖4所示,沒有固定於基體金屬箔1之粗糙化金屬粒子將離開基體金屬箔1,分散進入活性物質層31(32),以改善活性物質層31(32)與基體金屬箔1之界面間的導電性。此外,圖中33為活性物質,37為黏合劑與必要時所添加之導電材料。粗糙化金屬粒子分布之特徵係集中於基體金屬箔側,而朝活性物質層之最表面減少。 An active material having active material layers 31, 32 formed on both surfaces The metal foil of the layer is heated and pressurized by the press machine 11. By this heating and pressurizing step, the active material layers 31, 32 will be uniformly adhered to the surface of the metal foil, and thereby the pressing step forces the roughened particles to move, as shown in FIG. 4, which is not fixed to the base metal foil 1. The roughened metal particles will leave the base metal foil 1 and be dispersed into the active material layer 31 (32) to improve the electrical conductivity between the active material layer 31 (32) and the interface of the base metal foil 1. Further, in the figure, 33 is an active material, and 37 is a binder and a conductive material added as necessary. The characteristics of the roughened metal particle distribution are concentrated on the side of the base metal foil and are reduced toward the outermost surface of the active material layer.

步驟56(捲取步驟) Step 56 (rolling step)

將經加壓、乾燥之具有活性物質層之金屬箔以捲取機12進行捲取,接著運送至下一電極(步驟47)、電池(步驟48)之製程。 The pressed and dried metal foil having the active material layer is taken up by the coiler 12, and then transported to the next electrode (step 47) and the battery (step 48).

第六實施形態 Sixth embodiment

以下將依照圖11中所繪示之本發明第六實施形態之具有被覆層之金屬箔之製造流程圖、及圖12所繪示之製造流程圖來進行說明。 Hereinafter, a manufacturing flow chart of a metal foil having a coating layer according to a sixth embodiment of the present invention shown in FIG. 11 and a manufacturing flow chart shown in FIG. 12 will be described.

步驟61(表面粗糙化處理步驟) Step 61 (surface roughening treatment step)

如圖12所示,將金屬箔1導入於表面粗糙化處理槽2中,以電鍍於金屬箔1之表面上成長金屬粒子,以形成粗糙化金屬層3。 As shown in FIG. 12, the metal foil 1 is introduced into the surface roughening treatment tank 2, and metal particles are grown on the surface of the metal foil 1 to form the roughened metal layer 3.

如圖12所示,金屬箔1藉由給電電極20導入粗糙化處理槽2,並使其通過配置於粗糙化處理槽2中之電鍍用電極22、24、26之間。圖12中於3處配置電鍍用電極22、 24、26,以對金屬箔1之兩表面進行粗糙化處理,若僅於單一表面上進行粗糙化處理的話,可例如省略電極26。粗糙化處理之條件等將說明如後。 As shown in FIG. 12, the metal foil 1 is introduced into the roughening treatment tank 2 by the feeding electrode 20, and is passed between the plating electrodes 22, 24, 26 disposed in the roughening treatment tank 2. In FIG. 12, the electroplating electrode 22 is disposed at three places, 24 and 26, the roughening treatment is performed on both surfaces of the metal foil 1, and if the roughening treatment is performed only on a single surface, the electrode 26 can be omitted, for example. The conditions of the roughening treatment and the like will be explained later.

接著,導入於水洗處理槽4中進行粗糙化金屬層3之水洗。 Next, it is introduced into the water washing treatment tank 4 to perform water washing of the roughened metal layer 3.

將水洗之金屬箔導入防鏽處理槽5,以對粗糙化金屬層3表面塗佈防鏽劑。若無粗糙化金屬層氧化之虞慮的話,則可省略此防鏽處理。 The water-washed metal foil is introduced into the rust-preventing treatment tank 5 to apply a rust preventive agent to the surface of the roughened metal layer 3. This rust-preventing treatment can be omitted if there is no concern about the oxidation of the roughened metal layer.

步驟62(活性物質混合體之製作步驟) Step 62 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑或增黏劑、與漿體,以製成活性物質混合體8,然後將活性物質混合體8供給於儲料槽6、7。 The active material, the binder, and, if necessary, a conductive carbon black or a tackifier, and a slurry may be added to form the active material mixture 8, and then the active material mixture 8 is supplied to the storage tanks 6, 7.

當活性物質層形成時,較佳係例如使用聚亞醯胺來作為黏合劑,以形成均質之漿體塗佈層。 When the active material layer is formed, it is preferred to use, for example, polymethyleneamine as a binder to form a homogeneous slurry coating layer.

步驟63(第一活性物質層形成步驟) Step 63 (first active material layer forming step)

必要時可對進行上述表面粗糙化處理之金屬箔表面,以防鏽處理層5進行防鏽處理,由儲料槽6均勻地於另一表面上流入活性物質混合體8,以形成活性物質層31,對活性物質層31之表面,由薄膜供給滾輪15提供、黏貼上塑膠膜或脫膜紙13(若塑膠膜或脫膜紙不需特別區分之情況時,兩者可僅以薄膜13來表示)。 If necessary, the surface of the metal foil subjected to the surface roughening treatment may be subjected to rust-preventing treatment by the rust-preventing treatment layer 5, and the active material mixture 8 may be uniformly flowed from the hopper 6 on the other surface to form an active material layer. 31. The surface of the active material layer 31 is provided by the film supply roller 15 and adhered to the plastic film or the release paper 13 (if the plastic film or the release paper does not need to be particularly distinguished, the two may only be the film 13 Express).

步驟64(第二活性物質層形成步驟) Step 64 (second active material layer forming step)

於由薄膜13之供給滾輪14所提供之薄膜13上,由儲料槽7均勻地流入活性物質混合體8,於經表面粗糙化處 理之金屬箔之另一表面上,提供由薄膜13所搬運之活性物質混合體8,以形成活性物質層32。 On the film 13 provided by the supply roller 14 of the film 13, the active material mixture 8 is uniformly flowed from the hopper 7 to the surface roughened portion. On the other surface of the metal foil, the active material mixture 8 carried by the film 13 is provided to form the active material layer 32.

步驟65(乾燥、加壓步驟) Step 65 (drying, pressurizing step)

使兩表面上形成有活性物質層31、32之具有活性物質層之金屬箔通過乾燥機9、壓合機11,進行加熱、加壓。藉此加熱、加壓步驟,活性物質層31、32將均勻地密著於金屬箔表面,而且藉此加壓步驟,可使以上述表面處理所成長之粗糙化金屬層3之一部分的金屬粒子帶入活性物質層中。關於將游離金屬粒子帶入活性物質層中之步驟已於上述第五實施形態中進行說明,故在此不再贅述。 The metal foil having the active material layers on which the active material layers 31 and 32 are formed on both surfaces is passed through a dryer 9 and a press machine 11, and heated and pressurized. By this heating and pressurizing step, the active material layers 31, 32 are uniformly adhered to the surface of the metal foil, and by this pressurizing step, the metal particles of a part of the roughened metal layer 3 grown by the above surface treatment can be obtained. Bring into the active material layer. The step of bringing the free metal particles into the active material layer has been described in the fifth embodiment, and therefore will not be described again.

步驟66(捲取步驟) Step 66 (rolling step)

將經加壓、乾燥之具有活性物質層之金屬箔以捲取機12進行捲取,接著運送至下一電極、電池之製程。 The pressed and dried metal foil having the active material layer is taken up by the coiler 12, and then transported to the next electrode and the battery.

本實施形態中,薄膜13係設置於活性物質層32之上。因此,捲取機(例如捲軸)12進行捲取時,活性物質層32與活性物質層32間並不會直接互相接觸,故捲取時並不會損壞活性物質層。 In the present embodiment, the film 13 is provided on the active material layer 32. Therefore, when the coiler (for example, the spool) 12 is wound up, the active material layer 32 and the active material layer 32 do not directly contact each other, so that the active material layer is not damaged when wound up.

此外,此薄膜可例如使用與鋰離子二次電池之電極使用相同的隔板,以減少電池組裝時的麻煩。另外,不需要以薄膜來覆蓋活性物質表面時,可於活性物質層乾燥步驟後來去除。 Further, the film can be used, for example, using the same separator as the electrode of the lithium ion secondary battery to reduce troubles in battery assembly. Further, when it is not necessary to cover the surface of the active material with a film, it may be removed after the drying step of the active material layer.

第七實施形態 Seventh embodiment

以下將依照圖13中所繪示之本發明第七實施形態之具有被覆層之金屬箔之製造流程圖、及圖14所繪示之製造 裝置來進行說明。 Hereinafter, a manufacturing flow chart of a metal foil having a coating layer according to a seventh embodiment of the present invention illustrated in FIG. 13 and manufacturing as shown in FIG. 14 will be described. The device is explained.

步驟71(表面粗糙化處理步驟) Step 71 (surface roughening treatment step)

如圖13所示,將金屬箔1導入於表面粗糙化處理槽2中,以電鍍於金屬箔1之表面上成長金屬粒子,以形成粗糙化金屬層3。 As shown in FIG. 13, the metal foil 1 is introduced into the surface roughening treatment tank 2, and metal particles are grown on the surface of the metal foil 1 to form a roughened metal layer 3.

如圖14所示,金屬箔1藉由給電電極20導入表面粗糙化處理槽2,並使其通過配置於表面粗糙化處理槽2中之電鍍用電極22、24、26。圖14中於3處配置電鍍用電極22、24、26,以對金屬箔1之兩表面進行粗糙化處理,若僅於單一表面上進行粗糙化處理的話,可例如省略電極26。粗糙化處理之條件等將說明如後。 As shown in FIG. 14, the metal foil 1 is introduced into the surface roughening treatment tank 2 by the feeding electrode 20, and passes through the plating electrodes 22, 24, 26 disposed in the surface roughening treatment tank 2. In FIG. 14, the plating electrodes 22, 24, and 26 are disposed at three places to roughen the both surfaces of the metal foil 1, and if the roughening treatment is performed only on a single surface, the electrode 26 can be omitted, for example. The conditions of the roughening treatment and the like will be explained later.

接著,導入於水洗處理槽4中進行粗糙化金屬層3之水洗。 Next, it is introduced into the water washing treatment tank 4 to perform water washing of the roughened metal layer 3.

將水洗之金屬箔再導入防鏽處理槽5,對粗糙化金屬層3表面塗佈防鏽劑。若無粗糙化金屬層氧化之虞慮的話,則可省略此防鏽處理。 The water-washed metal foil is further introduced into the rust-preventing treatment tank 5, and the surface of the roughened metal layer 3 is coated with a rust preventive agent. This rust-preventing treatment can be omitted if there is no concern about the oxidation of the roughened metal layer.

步驟72(第一可再熔之樹脂組成物層之形成步驟) Step 72 (step of forming the first remeltable resin composition layer)

對經粗糙化處理之金屬箔之單一表面,提供可再熔之樹脂組成物。可再熔之樹脂組成物可使用一般市售之熱可塑性樹脂組成物。本實施形態如上所述,樹脂組成物層較佳係選擇與其上之活性物質層可接著之樹脂組成物。 A remeltable resin composition is provided on a single surface of the roughened metal foil. As the remeltable resin composition, a commercially available thermoplastic resin composition can be used. In the present embodiment, as described above, the resin composition layer is preferably a resin composition which can be followed by the active material layer thereon.

如圖13所示,對金屬箔1之單一表面,提供可再熔之樹脂組成物之薄膜40,以壓著滾輪41將兩者黏合。必要時可進行熱壓著。 As shown in Fig. 13, a film 40 of a remeltable resin composition is provided on a single surface of the metal foil 1, and the two are bonded by pressing the roller 41. It can be hot pressed if necessary.

步驟73(活性物質混合體之製作步驟) Step 73 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑或增黏劑、與漿體,將活性物質混合體8供給於儲料槽6、7。 The active material, the binder, and, if necessary, a conductive carbon black or a tackifier, and a slurry may be added, and the active material mixture 8 is supplied to the storage tanks 6, 7.

當活性物質層形成時,以上述可再熔之樹脂組合物層40來將活性物質31與金屬箔1接著,必要時最好例如使用聚亞醯胺來作為黏合劑,以形成均質之漿體塗佈層。 When the active material layer is formed, the active material 31 is adhered to the metal foil 1 by the above-mentioned remeltable resin composition layer 40, and if necessary, for example, polybenzamine is preferably used as a binder to form a homogeneous slurry. Coating layer.

步驟74(第一活性物質層形成步驟) Step 74 (first active material layer forming step)

於以上述可再熔之樹脂組合物層40被覆一表面之金屬箔上,由儲料槽6均勻地流入活性物質混合體8,以乾燥裝置9進行活性物質混合體8的乾燥,以形成活性物質層31。 On the metal foil coated with a surface of the remeltable resin composition layer 40, the active material mixture 8 is uniformly flowed from the hopper 6, and the active material mixture 8 is dried by the drying device 9 to form an active material. Material layer 31.

步驟75(第二可再熔之樹脂組成物層之形成步驟) Step 75 (step of forming a second remeltable resin composition layer)

同於步驟72,如圖13所示,對金屬箔1之另一表面提供可再熔之樹脂組成物之薄膜42,以壓著滾輪41將兩者黏合。必要時可進行熱壓著。 In the same manner as in step 72, as shown in Fig. 13, a film 42 of a remeltable resin composition is provided on the other surface of the metal foil 1, and the two are bonded by pressing the roller 41. It can be hot pressed if necessary.

步驟76(第二活性物質層形成步驟) Step 76 (second active material layer forming step)

接著,於可再熔之樹脂組合物層之薄膜42之表面上,由儲料槽7均勻地流入活性物質混合體8,以乾燥裝置10進行乾燥,以形成活性物質層32。 Next, on the surface of the film 42 of the remeltable resin composition layer, the active material mixture 8 is uniformly flowed from the hopper 7 and dried by the drying device 10 to form the active material layer 32.

步驟77(乾燥、加壓步驟) Step 77 (drying, pressurizing step)

使兩表面上形成有活性物質層31、32之具有活性物質層之金屬箔通過壓合機11,進行加熱、加壓。藉此加熱、加壓步驟,活性物質層31、32將藉由可再熔之樹脂組合物 層40、42,均勻地密著於金屬箔表面。而且,藉由上述貼合步驟、加熱、加壓步驟,可將以上述表面處理所成長之粗糙化金屬層3之一部分的金屬粒子帶入可再熔之樹脂組合物層中。 The metal foil having the active material layers on which the active material layers 31 and 32 are formed on both surfaces is passed through a press machine 11 to be heated and pressurized. By this heating and pressurizing step, the active material layers 31, 32 will be made of a remeltable resin composition. The layers 40, 42 are evenly adhered to the surface of the metal foil. Further, by the bonding step, the heating and the pressurizing step, the metal particles of a part of the roughened metal layer 3 grown by the above surface treatment can be brought into the remeltable resin composition layer.

如圖6所示,粗糙化金屬粒子35於可再熔之樹脂組合物層之貼合步驟、活性物質之加壓步驟中離開金屬箔表面而移動,進而進入可再熔之樹脂組合物層40(42),以改善活性物質層31(32)與金屬箔1之界面間的導電性。此外,圖中33為活性物質,37為黏合劑與必要時所添加之導電材料。粗糙化金屬粒子分布之特徵係集中於金屬箔側,而朝活性物質層減少。 As shown in FIG. 6, the roughened metal particles 35 are moved away from the surface of the metal foil in the bonding step of the remeltable resin composition layer and the pressing step of the active material, and further into the remeltable resin composition layer 40. (42) to improve the electrical conductivity between the interface between the active material layer 31 (32) and the metal foil 1. Further, in the figure, 33 is an active material, and 37 is a binder and a conductive material added as necessary. The characteristics of the roughened metal particle distribution are concentrated on the metal foil side and are reduced toward the active material layer.

步驟78(捲取步驟) Step 78 (rolling step)

將經加壓、乾燥之具有活性物質層之金屬箔以捲取機12進行捲取,接著運送至下一電極、電池之製程。 The pressed and dried metal foil having the active material layer is taken up by the coiler 12, and then transported to the next electrode and the battery.

此外,上述薄膜可藉由例如使用與鋰離子二次電池之電極使用相同的隔板,來減少電池組裝時的麻煩。 Further, the above film can reduce troubles in battery assembly by, for example, using the same separator as the electrode of the lithium ion secondary battery.

第八實施形態 Eighth embodiment

以下將依照圖15中所繪示之本發明第八實施形態之具有被覆層之金屬箔之製造流程圖、及圖16所繪示之製造裝置來進行說明。 Hereinafter, a manufacturing flow chart of a metal foil having a coating layer according to an eighth embodiment of the present invention shown in FIG. 15 and a manufacturing apparatus shown in FIG. 16 will be described.

步驟81(表面粗糙化處理步驟) Step 81 (surface roughening treatment step)

如圖16所示,將金屬箔1導入於表面粗糙化處理槽2中,以電鍍於金屬箔1之表面上成長金屬粒子,以形成粗糙化金屬層3。 As shown in FIG. 16, the metal foil 1 is introduced into the surface roughening treatment tank 2, and metal particles are grown on the surface of the metal foil 1 to form the roughened metal layer 3.

如圖15所示,金屬箔1藉由給電電極20導入表面粗糙化處理槽2,並使其通過配置於表面粗糙化處理槽2中之電鍍用電極22、24、26。圖13中於3處配置電鍍用電極22、24、26,以對金屬箔1之兩表面進行粗糙化處理,若僅於單一表面上進行粗糙化處理的話,可例如省略電極26。粗糙化處理之條件等將說明如後。 As shown in FIG. 15, the metal foil 1 is introduced into the surface roughening treatment tank 2 by the feeding electrode 20, and passes through the plating electrodes 22, 24, 26 disposed in the surface roughening treatment tank 2. In FIG. 13, the plating electrodes 22, 24, and 26 are disposed at three places to roughen the both surfaces of the metal foil 1, and if the roughening treatment is performed only on a single surface, the electrode 26 can be omitted, for example. The conditions of the roughening treatment and the like will be explained later.

接著,導入於水洗處理槽4中進行粗糙化金屬層3之水洗。 Next, it is introduced into the water washing treatment tank 4 to perform water washing of the roughened metal layer 3.

將水洗之金屬箔再導入防鏽處理槽5,對粗糙化金屬層3表面塗佈防鏽劑。若無粗糙化金屬層氧化之虞慮的話,則可省略此防鏽處理。 The water-washed metal foil is further introduced into the rust-preventing treatment tank 5, and the surface of the roughened metal layer 3 is coated with a rust preventive agent. This rust-preventing treatment can be omitted if there is no concern about the oxidation of the roughened metal layer.

步驟82(可再熔之樹脂組成物層之形成步驟) Step 82 (Step of forming a remeltable resin composition layer)

對經粗糙化處理之金屬箔1之兩表面,提供可再熔之樹脂組成物層40。可再熔之樹脂組成物可使用一般市售之熱可塑性樹脂組成物。本實施形態中,較佳係選擇與設置於樹脂組成物層上之活性物質層可接著之樹脂組成物。 On both surfaces of the roughened metal foil 1, a remeltable resin composition layer 40 is provided. As the remeltable resin composition, a commercially available thermoplastic resin composition can be used. In the present embodiment, it is preferred to select a resin composition which can be attached to the active material layer provided on the resin composition layer.

如圖16所示,對金屬箔1之兩表面,提供可再熔之樹脂組成物之薄膜40,以壓著滾輪41將兩者黏合。必要時可進行熱壓著。 As shown in Fig. 16, a film 40 of a remeltable resin composition is provided on both surfaces of the metal foil 1, and the two are bonded by a roller 41. It can be hot pressed if necessary.

此外,薄膜可藉由例如使用與鋰離子二次電池之電極使用相同的隔板,來減少電池組裝時的麻煩。 Further, the film can reduce troubles in battery assembly by, for example, using the same separator as the electrode of the lithium ion secondary battery.

步驟83(活性物質混合體之製作步驟) Step 83 (Step of producing active substance mixture)

混合活性物質、黏合劑、及必要時可添加導電性碳黑或增黏劑、與漿體,將活性物質混合體8供給於儲料槽6、 7。 a mixed active material, a binder, and, if necessary, a conductive carbon black or a tackifier, and a slurry, and the active material mixture 8 is supplied to the storage tank 6, 7.

當活性物質層形成時,以上述可再熔之樹脂組合物層40來將活性物質31與金屬箔1接著,必要時最好例如使用聚亞醯胺來作為黏合劑,以形成均質之漿體塗佈層。 When the active material layer is formed, the active material 31 is adhered to the metal foil 1 by the above-mentioned remeltable resin composition layer 40, and if necessary, for example, polybenzamine is preferably used as a binder to form a homogeneous slurry. Coating layer.

步驟84(第一活性物質層形成步驟) Step 84 (first active material layer forming step)

於以可再熔之樹脂組合物層所形成之金屬箔之一表面上,由儲料槽6均勻地流入活性物質混合體8,以形成活性物質層31,對該活性物質層31之表面,由薄膜供給滾輪15提供薄膜13,來進行貼合。 On the surface of one of the metal foils formed of the remeltable resin composition layer, the active material mixture 8 is uniformly flowed from the hopper 6 to form the active material layer 31, and the surface of the active material layer 31 is The film 13 is supplied from the film supply roller 15 to be bonded.

步驟85(第二活性物質層形成步驟) Step 85 (second active material layer forming step)

於由薄膜13之供給滾輪14所提供之薄膜13上,由儲料槽7均勻地流入活性物質混合體8,於以可再熔之樹脂組成物層所被覆之金屬箔之另一表面上,提供由薄膜13所搬運之活性物質混合體8,以形成活性物質層32。 On the film 13 provided by the supply roller 14 of the film 13, the hopper 14 is uniformly flowed into the active material mixture 8 on the other surface of the metal foil covered with the remeltable resin composition layer. The active material mixture 8 carried by the film 13 is provided to form the active material layer 32.

步驟86(乾燥、加壓步驟) Step 86 (drying, pressurizing step)

使兩表面上形成有活性物質層31、32之具有活性物質層之金屬箔通過壓合機11,進行加熱、加壓。藉此加熱、加壓步驟,活性物質層31、32將藉由可再熔之樹脂組成物層40、42,均勻地密著於金屬箔表面。而且,藉此上述貼合步驟、加熱、加壓步驟,可將以上述表面處理所成長之粗糙化金屬層3之一部分的金屬粒子帶入可再熔之樹脂組成物層中。 The metal foil having the active material layers on which the active material layers 31 and 32 are formed on both surfaces is passed through a press machine 11 to be heated and pressurized. By this heating and pressurizing step, the active material layers 31, 32 are uniformly adhered to the surface of the metal foil by the remeltable resin composition layers 40, 42. Further, by the bonding step, the heating and the pressurizing step, the metal particles of a part of the roughened metal layer 3 grown by the surface treatment can be brought into the remeltable resin composition layer.

步驟87(捲取步驟) Step 87 (rolling step)

將經加壓、乾燥之具有活性物質層之金屬箔以捲取機 12進行捲取,接著運送至下一電極、電池之製程。 Pressurized and dried metal foil with active material layer as coiler 12 is taken up and then transported to the next electrode, battery process.

本實施形態中,薄膜13係設置於活性物質層32之上。因此,捲取機(例如捲軸)12進行捲取時,活性物質層32與活性物質層32間並不會直接互相接觸,故捲取時並不會損壞活性物質層。 In the present embodiment, the film 13 is provided on the active material layer 32. Therefore, when the coiler (for example, the spool) 12 is wound up, the active material layer 32 and the active material layer 32 do not directly contact each other, so that the active material layer is not damaged when wound up.

此外,薄膜可例如使用與鋰離子二次電池之電極使用相同的隔板,以減少電池組裝時的麻煩。另外,不需要以薄膜來覆蓋活性物質表面時,可於活性物質層乾燥步驟後來去除。 Further, the film can be used, for example, using the same separator as the electrode of the lithium ion secondary battery to reduce troubles in battery assembly. Further, when it is not necessary to cover the surface of the active material with a film, it may be removed after the drying step of the active material layer.

步驟88 Step 88

使用具有上述製作之活性物質層之金屬箔,來製作電池用電極。 A battery electrode was produced using the metal foil having the active material layer produced as described above.

步驟89 Step 89

將上述電極用電池的組裝,以完成電池之製作。 The battery for the above electrode is assembled to complete the production of the battery.

本發明之具有被覆層之金屬箔中,作為被覆層之活性物質層之金屬箔,由於活性物質層形成於金屬箔表面,可以此狀態用來作為電池用電極。因此,金屬箔可選擇適當之金屬,來作為構成電池電極之集電體。例如,鋰離子二次電池之正極可選擇鋁箔,而負極可選擇銅箔。 In the metal foil having a coating layer of the present invention, the metal foil as the active material layer of the coating layer can be used as a battery electrode in this state because the active material layer is formed on the surface of the metal foil. Therefore, the metal foil can be selected from a suitable metal as a current collector constituting the battery electrode. For example, the positive electrode of the lithium ion secondary battery may be selected from an aluminum foil, and the negative electrode may be selected from a copper foil.

以下的說明將以電解銅箔作為金屬箔為例來進行說明,但亦可將電解銅箔置換為壓延銅箔。 In the following description, an electrolytic copper foil is used as a metal foil as an example, but the electrolytic copper foil may be replaced with a rolled copper foil.

此外,不僅是電解銅箔,與電解銅箔相同目的所使用之鋰離子二次電池用、或用來作為其他目的之電池用集電體之金屬箔中,與銅箔相同,只要是於集電體不會發生皺 摺、不會發生集電體的斷裂、而且可增加活性物質與集電基體金屬箔間之接著力、並可長時間維持穩定之二次電池特性的鋰離子二次電池用電極(具有活性物質層之金屬箔)之金屬箔,不管選擇其中何種金屬箔,均可用來作為具有活性物質層之金屬箔。 Further, not only the electrolytic copper foil, but also the metal foil for the lithium ion secondary battery used for the same purpose as the electrolytic copper foil or the battery current collector for other purposes, the copper foil is the same as the copper foil. The electric body does not wrinkle An electrode for a lithium ion secondary battery (with active material that can be folded, does not cause breakage of the current collector, and can increase the adhesion between the active material and the current collector metal foil, and can maintain stable secondary battery characteristics for a long period of time The metal foil of the metal foil of the layer, regardless of which metal foil is selected, can be used as the metal foil having the active material layer.

本實施形態中,表面粗糙化步驟中,於例如銅箔之金屬箔表面上,藉由於電解槽中流通極限電流密度以上之電流的燒焦電鍍法,來形成粗糙化處理層。以燒焦電鍍法之粗糙化處理所形成之粗糙化處理層為樹枝狀,此樹枝狀之粗糙化處理層之前端部分為易脆的。 In the present embodiment, in the surface roughening step, a roughened layer is formed on the surface of the metal foil of the copper foil by a scoring plating method in which a current exceeding a limit current density flows in the electrolytic cell. The roughened layer formed by the roughening treatment by the scorch plating method is dendritic, and the front end portion of the dendritic roughened layer is fragile.

本實施形態中,於表面粗糙度Rz為0.5~5 μm之基體金屬箔表面上,以燒焦電鍍法形成粗糙化處理層。粗糙化處理中,較佳成長粒徑為0.1~3 μm之粒子。此外,當基體金屬之兩表面上形成活性物質層時,基體金屬箔之正反表面之粗糙度Rz的差異較佳於2.5 μm以下。 In the present embodiment, the roughened layer is formed by a scoring plating method on the surface of the base metal foil having a surface roughness Rz of 0.5 to 5 μm. In the roughening treatment, particles having a growth particle diameter of 0.1 to 3 μm are preferred. Further, when the active material layer is formed on both surfaces of the base metal, the difference in roughness Rz between the front and back surfaces of the base metal foil is preferably 2.5 μm or less.

於對粗糙化處理層之前端部分成長為粒子狀、於該粗糙化處理層表面上設置活性物質層之步驟中,較佳係利用上述陰極電解電鍍法之燒焦電鍍法,以脫落‧分散之強度來設置於活性物質層上。 In the step of growing the active material layer on the surface of the roughened layer before the roughening layer is formed, it is preferable to use the above-mentioned cathodic electrolytic plating method to remove the ‧ dispersion The strength is set on the active material layer.

然而,以表面處理所成長之金屬粒子,只要採用之電鍍法可使其成長於上述較佳範圍中,並不僅限於燒焦電鍍法。此外,對金屬箔表面實施粒子狀之表面粗糙化處理、該粒子狀粗糙化處理層所成長之前端部分,於上述粗糙化處理層表面上設置活性物質層之步驟中,只要是於活性物 質層中可設定脫落‧分散之強度的電鍍法,不論採用其中何種方法,均可選擇來利用。 However, the metal particles grown by the surface treatment can be grown in the above preferred range by electroplating, and are not limited to the scorch plating method. Further, the surface of the metal foil is subjected to a particle-like surface roughening treatment, and the front end portion where the particulate roughening treatment layer is grown is provided in the step of providing the active material layer on the surface of the roughening treatment layer as long as it is active material The plating method in which the strength of the peeling and the dispersion can be set in the layer can be selected and used regardless of the method.

此外,於金屬箔之正反兩表面上,以電鍍法進行粗糙化處理時,較佳係選擇表面平滑之金屬箔,於電解槽中使極限電流密度以上之電流流通,並形成粒徑為0.1~3.5 μm之樹枝狀的粗糙化處理層,該粗糙化處理層之表面粗糙度Rz為0.5~5 μm,正反面之表面粗糙度Rz之差異為2.5μm以下。 Further, in the roughening treatment by the electroplating method on both the front and back surfaces of the metal foil, it is preferred to select a metal foil having a smooth surface, and to flow a current having a limit current density or more in the electrolytic cell to form a particle diameter of 0.1. A dendritic roughening layer of ~3.5 μm, the surface roughness Rz of the roughened layer is 0.5 to 5 μm, and the difference of the surface roughness Rz between the front and back surfaces is 2.5 μm or less.

另外,於正反兩表面上形成活性物質層時,若上述金屬箔為電解銅泊的話,該剖面之結晶構造較佳為微細之粒狀結晶。藉由銅箔之結晶構造為粒狀結晶,可使正反兩表面之粗糙度差異變小,這是由於賦予粗糙化粒子後之粗糙度Rz值之差異縮小之緣故。當銅箔為柱狀結晶構造時,正反面粗糙度之差異變大,即使進行粗糙化處理後,也難以消除其差異。 Further, when the active material layer is formed on both the front and back surfaces, if the metal foil is electrolytic copper, the crystal structure of the cross section is preferably fine granular crystal. Since the crystal structure of the copper foil is a granular crystal, the difference in roughness between the front and back surfaces can be made small, because the difference in roughness Rz value after the roughened particles are applied is reduced. When the copper foil has a columnar crystal structure, the difference in the roughness of the front and back surfaces becomes large, and it is difficult to eliminate the difference even after the roughening treatment.

本發明之鋰離子二次電池電極用金屬箔,利用於電解槽中使極限電流密度以上之電流流通之燒焦電鍍(以下簡稱為燒焦電鍍),於該基體金屬箔之正反面上設置粒徑為0.1~3 μm之粗糙化粒子的層,其個別之表面之表面粗糙度Rz為0.5~5 μm、正反面之粗糙度Rz的差異為2.5 μm以下。 The metal foil for a lithium ion secondary battery electrode of the present invention is used in a electrolytic cell for causing a current having a current of a limit current or more to flow through a scorching plating (hereinafter referred to as a scorch plating), and a grain is formed on the front and back surfaces of the base metal foil. The layer of roughened particles having a diameter of 0.1 to 3 μm has a surface roughness Rz of 0.5 to 5 μm on the individual surfaces and a roughness Rz of 2.5 μm or less on the front and back surfaces.

當金屬箔例如為電解銅箔時,藉由於基體銅箔表面上進行粗糙化粒子處理,不僅改善與活性物質間之密著性,而且,伴隨電池內部之膨脹收縮之體積變化,可以粗糙化處理所得到之空隙空間來使應力得到舒緩與吸收。 When the metal foil is, for example, an electrolytic copper foil, the roughening particle treatment on the surface of the base copper foil not only improves the adhesion to the active material, but also can be roughened by the volume change of the expansion and contraction inside the battery. The resulting void space is used to soothe and absorb the stress.

當金屬箔為電解銅箔時,形成上述粗糙化處理層之材料較佳為Cu粗糙化粒子、或以Cu為主成分、且包含Fe、Ni、Cr、W、Mo、V、或包含複數種之粒子。藉由以Cu或以Cu為主成分之銅合金組成所構成之粗糙化粒子來形成粗糙化處理層,可提升粗糙化粒子與基體銅箔間之密著性,或藉由適當地控制燒焦電鍍之電流密度(極限電流密度)以控制粗糙化粒子之粒徑,可更為容易且任意地調整表面粗糙度Rz值。 When the metal foil is an electrolytic copper foil, the material forming the roughening treatment layer is preferably Cu roughened particles, or Cu as a main component, and contains Fe, Ni, Cr, W, Mo, V, or a plurality of species. Particles. By forming a roughened layer by roughening particles composed of Cu or a copper alloy containing Cu as a main component, the adhesion between the roughened particles and the base copper foil can be improved, or by appropriately controlling the charring The current density (limited current density) of the plating is used to control the particle diameter of the roughened particles, and the surface roughness Rz value can be adjusted more easily and arbitrarily.

作為金屬箔之銅箔可為電解銅箔,亦可為壓延銅箔,其較佳為表面粗糙度為0.8~2.0 μm,於常溫下結晶粒界組織係由粒徑為5μm以下之粒狀結晶構成,物性方面,拉伸強度(T.S)為常溫時300MPa以上、延伸率(E)為3.5%以上,再加上150℃ x15小時後之拉伸強度可維持於250MPa以上。 The copper foil as the metal foil may be an electrolytic copper foil or a rolled copper foil, and preferably has a surface roughness of 0.8 to 2.0 μm, and the crystal grain boundary structure at room temperature is a granular crystal having a particle diameter of 5 μm or less. In terms of physical properties, the tensile strength (TS) is 300 MPa or more at normal temperature, and the elongation (E) is 3.5% or more, and the tensile strength after 150 ° C for 15 hours can be maintained at 250 MPa or more.

一般結晶粒徑愈大,會有金屬箔之拉伸強度(T.S)降低、延伸率(E)增大之傾向。當鍺、矽、錫等用來作為負極活性物質之情況、以及集電體(金屬箔)之強度(T.S)低之情況時,不論進行何種粗糙化處理,均無法吸收電池的膨脹收縮,且金屬箔易發生龜裂、斷裂。為了避免此情形,拉伸強度最好為300MPa以上,伸長較佳為3.5%以上,且此結晶構造粒徑較佳為5μm以下。 Generally, the larger the crystal grain size, the lower the tensile strength (T.S) of the metal foil and the higher the elongation (E). When ruthenium, osmium, tin, or the like is used as the negative electrode active material and the strength (TS) of the current collector (metal foil) is low, the expansion and contraction of the battery cannot be absorbed regardless of the roughening treatment. Moreover, the metal foil is prone to cracking and fracture. In order to avoid this, the tensile strength is preferably 300 MPa or more, the elongation is preferably 3.5% or more, and the crystal structure particle diameter is preferably 5 μm or less.

此外,於鋰離子二次電池用負極集電體之製程中有乾燥步驟,當此乾燥不完全時,會使電池特性劣化是眾所周知的。此時之乾燥條件一般為100~200℃下進行5~20小 時。此時當集電體(金屬箔)塑性變形或軟化的話,因如上述理由將於充放電時發生金屬箔龜裂斷裂等問題,因此於乾燥步驟後金屬箔之強度(硬度)即成為重要的物性因素。 Further, there is a drying step in the process of the negative electrode current collector for a lithium ion secondary battery, and when the drying is incomplete, deterioration of battery characteristics is well known. The drying conditions at this time are generally 5 to 20 small at 100 to 200 ° C. Time. At this time, when the current collector (metal foil) is plastically deformed or softened, problems such as cracking of the metal foil during charging and discharging occur due to the above reasons, and therefore the strength (hardness) of the metal foil becomes important after the drying step. Physical factors.

於使用金屬箔之乾燥步驟條件中,最機械性物性變動的為銅箔。 Among the drying step conditions in which the metal foil is used, the most mechanical property changes are copper foil.

關於電解銅箔至此的開發,抑制電解銅箔之加熱時的再結晶(塑性變形)技術中,較佳為製箔法,其係於電解銅箔時對電解液之添加劑組成之濃度分別設定為MPS(3-巰基-1-丙烷磺酸鈉)為3~10ppm、HEC(羥乙基纖維素‧高分子多醣類)為15~20ppm、動物性膠為30~70ppm。 In the development of the electrolytic copper foil to the present, in the technique of suppressing recrystallization (plastic deformation) during heating of the electrolytic copper foil, it is preferable to use a foil forming method in which the concentration of the additive composition of the electrolytic solution is set to be different when the electrolytic copper foil is pressed. MPS (sodium 3-mercapto-1-propane sulfonate) is 3 to 10 ppm, HEC (hydroxyethyl cellulose ‧ polymeric polysaccharides) is 15 to 20 ppm, and animal glue is 30 to 70 ppm.

賦予上述粗糙化粒子之處理後的表面積比較佳為2.5~5倍。所謂表面積比,係使用KEYENCE公司所製之VK-8500,來測量金屬箔表面之2500 μm2(50μm x 50μm)的面積,以此值將基體金屬箔(粗糙化處理前)與粗糙化處理後之面積,以比例表示所得之比。亦即,表面積比為1的話,極表示粗糙化處理前後之表面積未改變,粗糙化處理後之面積若為5000μm2,即表示表面積變成2倍。 The surface area after the treatment of the roughened particles is preferably 2.5 to 5 times. The surface area ratio is measured using a VK-8500 manufactured by KEYENCE Corporation to measure the area of 2500 μm 2 (50 μm x 50 μm) on the surface of the metal foil. The base metal foil (before roughening treatment) and roughening treatment are used. The area is expressed in proportion to the ratio obtained. That is, when the surface area ratio is 1, the surface of the electrode before and after the roughening treatment is not changed, and if the area after the roughening treatment is 5000 μm 2 , the surface area is doubled.

本發明之拉伸強度(T.S)、延伸率(E)係以日本工業規格(JISK 6251)所定之方法進行測量所得到的值。 The tensile strength (T.S) and the elongation (E) of the present invention are values obtained by measurement according to the method specified in Japanese Industrial Standards (JISK 6251).

另外,表面粗糙度Rz係以日本工業規格(JISB 0601-1994)所定之十點平均粗糙度、及算術表面粗糙度,以一般之表面粗糙度計測量所得到的值。 Further, the surface roughness Rz is a value obtained by measuring a ten-point average roughness and an arithmetic surface roughness defined by Japanese Industrial Standards (JISB 0601-1994) using a general surface roughness meter.

以燒焦電鍍法對金屬箔之正反表面進行粗糙化表面處 理時,基體金屬箔之正反兩表面之表面粗糙度Rz較佳為0.5~5 μm之平滑的表面。 Roughening the surface of the metal foil by scorch plating The surface roughness Rz of the front and back surfaces of the base metal foil is preferably a smooth surface of 0.5 to 5 μm.

燒焦電鍍法係於電解槽中使極限電流密度以上之電流流通之電鍍法,適用於對平滑之基體金屬箔表面賦予均勻之凹凸圖案之粗糙化處理方法。利用此燒焦電鍍法,可將金屬箔之正反表面進行粗糙化。 The scoring method is a plating method in which an electric current of a limit current density or more is passed through an electrolytic cell, and is applied to a roughening treatment method for imparting a uniform concave-convex pattern to a smooth base metal foil surface. By this scoring plating method, the front and back surfaces of the metal foil can be roughened.

藉由燒焦電鍍法,對金屬箔,尤其是電解銅箔表面,以進行粗糙化表面處理之方法,例如可採用揭示於專利文獻5(日本專利公開公報昭和第53-39376號)中之方法,較佳使用一般用於印刷電路用銅箔之方法。 For the method of roughening the surface of the metal foil, in particular, the surface of the electrolytic copper foil by the scoring method, for example, the method disclosed in Patent Document 5 (Japanese Patent Laid-Open No. 53-39376) can be used. Preferably, a method generally used for printing a copper foil for a circuit is used.

然而,上述專利文獻5中藉由「燒焦電鍍」,於形成粉粒狀銅電鍍層之後,對此粉粒狀銅電鍍層以不損壞其凹凸形狀之狀況下進行「膠囊電鍍」,即實質地形成平滑的電鍍層,以形成粉粒狀銅不脫落(不脫落粉末)之健全的海藻帶狀之銅粗糙化層之技術。 However, in the above-mentioned Patent Document 5, after the formation of the powdery copper plating layer by "scorch plating", the powdery copper plating layer is subjected to "capsule plating" without damaging the uneven shape, that is, the essence A smooth plating layer is formed to form a smooth seaweed ribbon-like copper roughening layer in which the powdery copper does not fall off (without falling off the powder).

本發明僅以燒焦電鍍進行處理之理由如下。 The reason why the present invention is treated only by scorch plating is as follows.

對基體金屬箔表面進行燒焦電鍍時,形成樹枝狀之粗糙化粒子將均勻地附著於金屬箔正反表面。此伸展成樹枝狀之粗糙化粒子係以前端容易折損、脫落之易脆狀態附著於金屬箔正反表面。 When the surface of the base metal foil is subjected to scoring plating, the dendritic particles forming dendrites are uniformly attached to the front and back surfaces of the metal foil. The roughened particles which are dendritic are attached to the front and back surfaces of the metal foil in a fragile state in which the front end is easily broken and peeled off.

本發明係於以上述易脆狀態所附著之樹枝狀粗糙化粒子層上方塗佈活性物質層。對上述可再熔之具有樹脂之粗糙化銅箔,進行具有活性物質與黏合劑之活性物質組成物的塗佈、乾燥,接著進行壓合步驟,所附著之樹脂再次成 為液體,樹枝狀粗糙化粒子於塗佈活性物質時、或乾燥時之膨脹收縮時、抑或是壓合時將會被損壞,所損壞之粒子將分散於活性物質組成物中,而混入成為活性物質組成物中的一部分。 In the present invention, the active material layer is applied over the dendritic roughened particle layer adhered in the above-described fragile state. Coating and drying the active material composition having the active material and the binder on the remeltable resin roughened copper foil, followed by a pressing step, and the adhered resin is again formed For liquids, the dendritic roughened particles will be damaged when the active material is applied, or when it is expanded and contracted during drying, or when it is pressed, and the damaged particles will be dispersed in the active material composition, and the mixed particles become active. Part of the composition of matter.

此外,於活性物質層之製作步驟中,燒焦電鍍層並不會造成阻礙。 Further, in the production step of the active material layer, the scorching of the plating layer does not cause hindrance.

經過活性組成物之塗佈、乾燥、加熱加壓步驟後,將構成漿狀之活性物質中之不需要之溶劑揮發,以形成固結之活性物質。此時,樹枝狀粒子將脫落,其脫落之粗糙化粒子將混入活性物質層中,另外,樹枝狀活性物質未脫落的部份會構成銅箔表面之粗糙(凹凸),於該粗糙化表面上之活性物質層,藉由黏合劑密切地接著於銅箔正反表面。因此,利用燒焦電鍍之粗糙化處理,係將伸展成樹枝狀之前端部分帶入活性物質層,於活性物質中之銅粒游離的狀態下形成活性物質層。其基礎部份沿著活性物質之形狀,形成銅箔表面之粗糙化形狀,不僅提升活性物質與銅箔間之密著性,比起習知之粗糙化銅箔,其內部殘留應力較少,導電率提高,形成發熱少知電池用電極。另外,活性物質組成物之塗佈、乾燥、加熱、加壓壓合製程中,因暴露於300℃之高溫,其基礎部份之粗糙化粒子將會燒結,而固著於銅箔表面。 After the application, drying, heating and pressurization steps of the active composition, the unnecessary solvent in the slurry-form active material is volatilized to form a consolidated active material. At this time, the dendritic particles will fall off, and the roughened particles which are detached will be mixed into the active material layer, and the portion where the dendritic active material does not fall off will constitute the roughness (concavity and convexity) of the surface of the copper foil on the roughened surface. The active material layer is closely adhered to the front and back surfaces of the copper foil by the adhesive. Therefore, by the roughening treatment by the scorch plating, the front end portion which is stretched into a dendritic shape is brought into the active material layer, and the active material layer is formed in a state where the copper particles in the active material are free. The basic part forms a roughened shape of the surface of the copper foil along the shape of the active material, which not only enhances the adhesion between the active material and the copper foil, but also has less internal residual stress than the conventional roughened copper foil. The rate is increased, and an electrode for generating a battery for heat generation is formed. Further, in the coating, drying, heating, and press-bonding processes of the active material composition, the roughened particles of the base portion are sintered and adhered to the surface of the copper foil due to exposure to a high temperature of 300 °C.

除上述燒焦電鍍之外,如日本專利公開公報第2007-270184號中所揭示地,可於粗糙化處理槽2中置換成包含高分子分散介質之導電性水溶液,來進行於未處理 銅箔表面上析出銅奈米粒子之處理。由於銅粒子會變小,其後於作為電池負極時,銅奈米粒子可與活性物質間無間隙地進行接觸,具有提升與負極集電體之導電率的效果。 In addition to the above-described scorching plating, as disclosed in Japanese Laid-Open Patent Publication No. 2007-270184, the roughening treatment tank 2 can be replaced with a conductive aqueous solution containing a polymer dispersion medium to be untreated. The treatment of depositing copper nanoparticles on the surface of the copper foil. Since the copper particles are small, and thereafter, when used as a battery negative electrode, the copper nanoparticles can be brought into contact with the active material without a gap, and the effect of improving the electrical conductivity with the negative electrode current collector can be obtained.

本實施形態之粗糙化處理步驟中,與習知不同,於燒焦電鍍後並不進行膠囊電鍍。由於不進行膠囊電鍍,粗糙化粒子不會固接於基體金屬箔上,藉由加熱‧加壓製程中(壓合)之壓力促使活性物質形成粗糙化粒子、並移動,粗糙化粒子將沿著活性物質之形狀,以一部份混入活性物質層中之之狀態來進行移動,粗糙化粒子與活性物質間將形成最大之接觸面積。當使用於習知之上述燒焦電鍍後進行膠囊電鍍之銅箔時,因粗糙化粒子固接於基體金屬箔,即使以壓合壓力迫使粗糙化粒子混入活性物質,粗糙化粒子仍不移動,將造成殘留應力發生於活性物質與基體金屬箔之間的狀態,而其作為在電池負極時,則將會造成基體金屬箔斷裂。 In the roughening treatment step of the present embodiment, unlike conventionally, capsule plating is not performed after the scoring plating. Since the capsule plating is not performed, the roughened particles are not fixed to the base metal foil, and the active material forms roughened particles and moves by heating under pressure (pressing), and the roughened particles will follow along. The shape of the active material is moved in a state in which it is partially mixed into the active material layer, and the largest contact area is formed between the roughened particles and the active material. When the copper foil which is subjected to capsule electroplating after the above-mentioned scorching electroplating is used, since the roughened particles are fixed to the base metal foil, even if the roughened particles are mixed into the active material under the pressing pressure, the roughened particles do not move, and the roughened particles will not move. The residual stress is caused to occur between the active material and the base metal foil, and when it is used as the negative electrode of the battery, the base metal foil is broken.

本發明之活性物質除了習知之黑鉛類之外,也可選擇可吸收‧放出鋰之物質,藉由進行鋰之合金化來進行吸收之活性物質。此活性物質可例如矽、鍺、錫、鉛、鋅、錳、鈉、鋁、鉀、銦等。而其中因作為負極活性物質時,矽與錫具有高的理論容量、且容易使用,因此以此兩種為佳,近年來也開始逐漸被使用。 In addition to the conventional black lead, the active material of the present invention may also be an active material which can absorb and release lithium and perform alloying by lithium alloying. The active material may be, for example, ruthenium, osmium, tin, lead, zinc, manganese, sodium, aluminum, potassium, indium or the like. Among them, ruthenium and tin have a high theoretical capacity and are easy to use because they are used as a negative electrode active material. Therefore, both of them are preferable, and they have been gradually used in recent years.

鋰離子二次電池之負極活性物質層除黑鉛類之外,較佳係使用矽、或以錫為主成分之活性物質層,尤其更佳係以矽為主成分之薄層。 In addition to the black lead, the negative electrode active material layer of the lithium ion secondary battery is preferably an active material layer containing ruthenium or tin as a main component, and more preferably a thin layer mainly composed of ruthenium.

另外,活性物質層較佳為非晶質層或微結晶層,若選擇矽類時,則較佳為非晶矽層或微結晶矽層。 Further, the active material layer is preferably an amorphous layer or a microcrystalline layer, and when an anthracene is selected, an amorphous layer or a microcrystalline layer is preferred.

本實施形態係以集電體厚度薄之前提來揭示,二次電池之設計也以輕量輕薄為佳。因此,金屬箔較佳係選擇銅箔作為負極集電體用,選擇鋁作為正極集電體用。活性物質層可於集電體之單一表面、或兩表面上進行塗佈、堆積來形成。當於集電體之正反兩面形成活性物質層時,較佳為集電體兩表面之表面粗糙度Rz於0.5~5 μm範圍之同時,也使正反表面之Rz值的差異於2.5 μm以下。 In the present embodiment, it is revealed that the thickness of the current collector is small, and the design of the secondary battery is preferably light and light. Therefore, the metal foil is preferably selected from a copper foil as a negative electrode current collector, and aluminum is selected as a positive electrode current collector. The active material layer can be formed by coating and stacking on a single surface or both surfaces of the current collector. When the active material layer is formed on both the front and back sides of the current collector, it is preferable that the surface roughness Rz of both surfaces of the current collector is in the range of 0.5 to 5 μm, and the Rz value of the front and back surfaces is also different from 2.5 μm. the following.

集電體(金屬箔)之厚度,薄者較佳為8 μm,厚者較佳為20 μm。這是因為8 μm以下無法保有金屬箔(作為集電體)之強度,且於活性物質之膨脹‧收縮時容易產生龜裂、斷裂之緣故。而當超過20 μm的話,雖然可滿足電池特性,但電池本身將會變大、且變重,故較佳設定至約為20 μm左右。 The thickness of the current collector (metal foil) is preferably 8 μm for the thinner and 20 μm for the thicker one. This is because the strength of the metal foil (as a current collector) cannot be maintained below 8 μm, and cracks and fractures are likely to occur during expansion and contraction of the active material. On the other hand, when it exceeds 20 μm, although the battery characteristics can be satisfied, the battery itself becomes large and becomes heavy, so it is preferably set to about 20 μm.

兩表面之Rz值設定於0.5~5 μm之範圍。這是因為Rz值低於下限值的話,與活性物質層間之固著效果之密著性降低之緣故;而當超出上限值的話,相對地活性物質無法均一地進入粗糙化凹凸中之山谷凹處,而使得集電體與活性物質層間之密著性不夠充足,因此最好不超過此上限。 The Rz values of the two surfaces are set in the range of 0.5 to 5 μm. This is because if the Rz value is lower than the lower limit value, the adhesion to the anchoring effect between the active material layers is lowered. When the upper limit value is exceeded, the relatively active material does not uniformly enter the valley in the roughened unevenness. The recess is such that the adhesion between the current collector and the active material layer is insufficient, so it is preferable not to exceed this upper limit.

當表面粗糙度之正反面相差太大的話,活性物質之塗佈製程中兩表面之活性物質厚度將會不同,而導致電池電極特性發生問題。因此,正反表面之粗糙度Rz值的差異設定於2.5 μm以下。亦即,當正反表面之粗糙度Rz值的差 異於2.5 μm以上的話,活性物質之塗佈製程中兩表面之活性物質厚度將會不同,而無法充分顯示電池電極之特性。 When the difference between the front and back of the surface roughness is too large, the thickness of the active material on the two surfaces in the coating process of the active material will be different, resulting in problems in the electrode characteristics of the battery. Therefore, the difference in the roughness Rz value between the front and back surfaces is set to 2.5 μm or less. That is, when the difference between the Rz values of the front and back surfaces is If it is different from 2.5 μm or more, the thickness of the active material on both surfaces in the coating process of the active material will be different, and the characteristics of the battery electrode cannot be sufficiently displayed.

本發明之鋰離子二次電池包括塗佈、層積有以黑鉛類、矽類或錫類為主成分之鋰離子二次電池用活性物質之活性物質層的負極電極、使用可吸收‧放出鋰之物質的正極、非水電解質、及隔板。 The lithium ion secondary battery of the present invention includes a negative electrode which is coated and laminated with an active material layer of an active material for a lithium ion secondary battery mainly composed of black lead, bismuth or tin, and can be used for absorption and discharge. A positive electrode of a lithium substance, a nonaqueous electrolyte, and a separator.

本發明之鋰離子二次電池中所使用之非水電解質為將溶質溶解於溶劑中之電解質,非水電解質之溶劑只要為可用於鋰離子二次電池之溶劑,其他並無特別之限制,可例如為碳酸乙烯酯、碳酸丙烯酯、碳酸丁烯酯、碳酸亞乙烯酯等之環狀碳酸酯、碳酸二甲酯、碳酸二乙酯、碳酸甲乙酯等鏈狀碳酸酯等,而較佳係使用環狀碳酸酯與鏈狀碳酸酯之混合溶劑。此外,亦可使用環狀碳酸酯與1,2-二甲氧基乙烷、1,2-二乙氧基乙烷等醚類溶劑、γ-丁內酯、環丁碸、乙酸甲酯等鏈狀酯類等之混合溶劑。 The nonaqueous electrolyte used in the lithium ion secondary battery of the present invention is an electrolyte in which a solute is dissolved in a solvent, and the solvent of the nonaqueous electrolyte is not particularly limited as long as it is a solvent usable for a lithium ion secondary battery. For example, it is a cyclic carbonate such as ethylene carbonate, propylene carbonate, butylene carbonate or vinylene carbonate, a chain carbonate such as dimethyl carbonate, diethyl carbonate or ethyl methyl carbonate, and the like. A mixed solvent of a cyclic carbonate and a chain carbonate is used. Further, an ether solvent such as a cyclic carbonate and 1,2-dimethoxyethane or 1,2-diethoxyethane, γ-butyrolactone, cyclobutyl hydrazine, methyl acetate or the like may be used. A mixed solvent of a chain ester or the like.

非水電解質之溶質只要為可用於鋰離子二次電池之溶質,其他並無特別之限制,可例如為LiPF6、LiBF4、LiCF3SO3、LiN(CF3SO2)2、LiN(C2F5SO2)2、LiN(CF3SO2)(C4F9SO2)、LiC(CF3SO2)3、LiC(C2F5SO2)3、LiAsF6、LiClO4、Li2B10Cl10、Li2B12Cl12等。 The solute of the nonaqueous electrolyte is not particularly limited as long as it is a solute usable for a lithium ion secondary battery, and may be, for example, LiPF 6 , LiBF 4 , LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 , LiN (C). 2 F 5 SO 2 ) 2 , LiN(CF 3 SO 2 )(C 4 F 9 SO 2 ), LiC(CF 3 SO 2 ) 3 , LiC(C 2 F 5 SO 2 ) 3 , LiAsF 6 , LiClO 4 , Li 2 B 10 Cl 10 , Li 2 B 12 Cl 12 and the like.

此外,非水電解質可使用於聚氧化乙烯、聚丙烯腈、聚偏氯乙烯樹脂等之聚合物電解質中浸泡電解液之膠狀聚合物電解質、與LiI、Li3N等之無機固體電解質。 Further, the non-aqueous electrolyte can be used as a colloidal polymer electrolyte for immersing an electrolyte in a polymer electrolyte such as polyethylene oxide, polyacrylonitrile or polyvinylidene chloride resin, and an inorganic solid electrolyte such as LiI or Li 3 N.

本發明之鋰離子二次電池之電解質只要於電池之充放 電時、或保存時之電壓不分解之範圍下,可無限制地使用任意電解質。 The electrolyte of the lithium ion secondary battery of the present invention is only required to be charged and discharged in the battery Any electrolyte can be used without limitation in the range of electricity or when the voltage at the time of storage is not decomposed.

另外,正極所使用之正極活性物質可例如為LiCoO2、LiNiO2、LiMn2O4、LiMnO2、LiCo0.5Ni0.5O2、LiNi0.7Co0.2Mn0.1O2等之含鋰之過渡金屬氧化物、MnO2等之不含鋰之金屬氧化物等,但只要是電池中可吸收與放出鋰離子之物質,均可無限制地使用任意該物質。 Further, the positive electrode active material used for the positive electrode may be, for example, a lithium-containing transition metal oxide such as LiCoO 2 , LiNiO 2 , LiMn 2 O 4 , LiMnO 2 , LiCo 0.5 Ni 0.5 O 2 , LiNi 0.7 Co 0.2 Mn 0.1 O 2 or the like. And a metal oxide or the like which does not contain lithium, such as MnO 2 , but any substance which can absorb and release lithium ions in the battery can be used without limitation.

根據本發明,活性物質混合體進行塗佈時,藉由於乾燥‧加壓製程等中,導電性金屬微粒(脫落之粗糙化處理層)混入活性物質層,並適當分散於活性物質層中,不僅提升活性物質層之導電度,而且可抑制於充放電時負極集電體發生皺折與龜裂、斷裂的情形,提高鋰離子二次電池之單位體積之能量密度,進而可提供可長時間維持穩定性能之鋰離子二次電池。 According to the present invention, when the active material mixture is applied, the conductive metal fine particles (the roughened layer to be peeled off) are mixed into the active material layer by the drying, the pressurization process, or the like, and are appropriately dispersed in the active material layer. The conductivity of the active material layer is increased, and wrinkles, cracks, and fractures of the negative electrode current collector during charge and discharge are suppressed, and the energy density per unit volume of the lithium ion secondary battery is improved, thereby providing long-term maintenance. Lithium ion secondary battery with stable performance.

圖11、15所示之實施形態中,當捲取具有活性物質層之金屬箔時,為了保護重疊之活性物質層表面,可相隔薄膜(隔板)。 In the embodiment shown in Figs. 11 and 15, when the metal foil having the active material layer is wound up, a film (separator) may be interposed in order to protect the surface of the active material layer which is overlapped.

如上所述,由於於一表面上安置薄膜,當捲曲具有活性物質層之金屬箔時,可事先避免活性物質層相互接觸,且有時因損壞所造成的問題。 As described above, since the film is disposed on one surface, when the metal foil having the active material layer is curled, the active material layers can be prevented from contacting each other in advance, and sometimes problems due to damage.

此外,當使用此具有活性物質層之金屬箔作為二次電池之電極時,若上述薄膜係以電池電極用之隔板相同材料所構成的話,則隔板與電極可共用,並不需移除。 Further, when the metal foil having the active material layer is used as the electrode of the secondary battery, if the film is formed of the same material as the separator for the battery electrode, the separator and the electrode can be shared without removing .

另外,除作為電極時之隔板之外,薄膜較佳可使用脫 模紙。 In addition, in addition to the separator as an electrode, the film is preferably used Molded paper.

電池隔板係電池中分隔正極與負極、且維持電解液、以確保正極與負極間之離子傳導性之重要材料。隔板之種類因電池而異,鋰離子電池中係使用聚乙烯(超高分子量PE)與聚丙烯(PP)所製之微多孔膜,具有由個別單層之類型、至PE/PP之雙層結構、PP/PE/PP之三層結構之種類。因應這些樹脂之玻璃轉換溫度(TG)之特性,必須將乾燥溫度、或加熱加壓之條件設定於樹脂之玻璃轉換溫度(TG)以下之溫度。本實施形態中係使用聚乙烯(超高分子量PE)。 The battery separator is an important material for separating the positive electrode from the negative electrode and maintaining the electrolyte to ensure ionic conductivity between the positive electrode and the negative electrode. The type of the separator varies depending on the battery. In the lithium ion battery, a microporous membrane made of polyethylene (ultrahigh molecular weight PE) and polypropylene (PP) is used, which has a single layer type and a pair of PE/PP. Layer structure, type of three-layer structure of PP/PE/PP. In view of the characteristics of the glass transition temperature (TG) of these resins, the drying temperature or the conditions of heating and pressurization must be set to a temperature lower than the glass transition temperature (TG) of the resin. In the present embodiment, polyethylene (ultrahigh molecular weight PE) is used.

實施例 Example

以下將以以電解銅箔為例之實施例,對本發明之一實施形態來作詳細的說明,然而本發明並不會受以下實施例之限制,亦可於不會變更本發明精神之範圍內,作適當之變更,例如使用銅箔以外之金屬箔等。 In the following, an embodiment of the present invention will be described in detail with reference to an embodiment of the present invention. However, the present invention is not limited by the following examples, and may be within the scope of the spirit of the present invention. For appropriate changes, for example, a metal foil other than copper foil or the like is used.

〔實施例1~3與比較例1〕 [Examples 1 to 3 and Comparative Example 1]

〔電解銅箔之製造〕 [Manufacture of electrolytic copper foil]

實施例1、4與比較例1 Examples 1, 4 and Comparative Example 1

本實施例中金屬箔係採用銅箔。 In the present embodiment, the metal foil is made of copper foil.

製箔用電解母液 Electrolytic mother liquor for foil production

於具有金屬銅70~130g/l、硫酸80~140g/l之硫酸銅電解槽中,添加如表格1所示之組成之MPS、HEC與作為添加劑之氯離子,以製備製箔用電解母液。表格中,MPS係3-巰基-1-丙烷磺酸鈉,HEC(高分子多醣類)係羥乙基纖 維素,膠係指分子量為3000之低分子量膠。 In a copper sulfate electrolytic cell having a metal copper of 70 to 130 g/l and a sulfuric acid of 80 to 140 g/l, MPS, HEC having the composition shown in Table 1 and chloride ions as an additive were added to prepare an electrolytic mother liquid for foil formation. In the table, MPS is sodium 3-mercapto-1-propane sulfonate, HEC (polymer polysaccharide) hydroxyethylcellulose Vitamin, a gel refers to a low molecular weight gel with a molecular weight of 3,000.

此處將氯離子濃度調整為30ppm,但氯離子濃度可依電解條件來作適當的變更,並不僅限於此濃度。 Here, the chloride ion concentration is adjusted to 30 ppm, but the chloride ion concentration can be appropriately changed depending on the electrolysis conditions, and is not limited to this concentration.

製箔 Foil

使用所調配之電解母液,於陽極使用貴金屬氧化物被覆鈦電極、於陰極使用鈦製之轉筒,以表格1所示之電解條件(電流密度、液溫),來製作具有厚度10μm之電解銅箔。製箔之電解銅箔之表面粗糙度Rz、機械物性列於表格2中。 Using the prepared electrolytic mother liquid, a titanium electrode was coated with a noble metal oxide at the anode, a titanium cylinder was used for the cathode, and electrolytic copper having a thickness of 10 μm was produced by the electrolytic conditions (current density, liquid temperature) shown in Table 1. Foil. The surface roughness Rz and mechanical properties of the foil-formed electrolytic copper foil are shown in Table 2.

3-氫硫基-1-丙烷磺酸鈉 Sodium 3-hydrogenthio-1-propane sulfonate

羥乙基纖維素 Hydroxyethyl cellulose

分子量約為3000之動物性膠 Animal gum with a molecular weight of about 3,000

此外,表格2所示之各測定值係以下列方法測量所得之值。 Further, each of the measured values shown in Table 2 was measured by the following method.

〔箔之厚度、拉伸強度(T.S)、延伸率(E)之測定〕 [Measurement of Thickness, Tensile Strength (T.S), Elongation (E) of Foil]

以測微計測量所得之實測值,拉伸強度(T.S)、延伸率(E)係利用拉伸測試器(英士特(Instron)公司製1122型)測量所得之數值。表面粗糙度Rz係以探針式表面粗糙計(小坂研究所製SE-3C型)測量所得之值。 The measured values were measured by a micrometer, and the tensile strength (T.S.) and elongation (E) were measured by a tensile tester (Model 1122 manufactured by Instron Co., Ltd.). The surface roughness Rz is a value measured by a probe type surface roughness meter (SE-3C type manufactured by Otaru Laboratory).

〔金屬箔之表面粗糙化〕 [Roughening of the surface of metal foil]

對以上述製箔條件所製造之10μm之電解銅箔之正反表面,使用圖8所示之裝置,以下列條件來進行銅的燒焦電鍍。 The positive and negative surfaces of the 10 μm electrolytic copper foil produced under the above-described foil-forming conditions were subjected to scorch plating of copper under the following conditions using the apparatus shown in FIG.

亦即,實施例1係以圖8所示之給電軸20作為陽極、以配置於處理槽3中之給電電極20作為陰極,對上述所製箔之電解銅箔,以下列燒焦電鍍條件進行表面處理,接著於處理槽4中進行水洗。水洗用之處理槽4於圖8中雖僅繪示出一個槽,但必要時可增加水洗用的處理槽。接著,必要時,於其後之乾燥製程中,於銅箔不變色之情況下,可增設防鏽處理槽5以進行防鏽處理,並於漿體塗佈前稍為進行乾燥。 That is, in the first embodiment, the electric heating shaft 20 shown in FIG. 8 is used as an anode, and the electric current electrode 20 disposed in the processing tank 3 is used as a cathode. The electrolytic copper foil of the above-mentioned foil is subjected to the following scoring conditions. The surface treatment is followed by water washing in the treatment tank 4. Although only one tank is shown in Fig. 8 in the treatment tank 4 for water washing, the treatment tank for water washing can be added as necessary. Next, if necessary, in the subsequent drying process, in the case where the copper foil does not change color, the rust-preventing treatment tank 5 may be added to perform rust-preventing treatment, and may be slightly dried before the slurry coating.

賦予粗糙化粒子後之特性值列於表格3中。 The property values assigned to the roughened particles are listed in Table 3.

利用燒焦電鍍所賦予之粗糙化粒子後之特性值列於表格3中。 The property values after the roughened particles imparted by the scoring plating are listed in Table 3.

表面粗糙化處理(燒焦電鍍)條件:金屬銅 22.5~24.0 g/l Surface roughening treatment (scorch plating) conditions: metallic copper 22.5~24.0 g/l

硫酸 90~120 g/l Sulfuric acid 90~120 g/l

Mo添加金屬 0.35 g/l Mo added metal 0.35 g/l

槽溫 18~30℃ Slot temperature 18~30°C

電流密度 25~35 A/dm2 Current density 25~35 A/dm 2

處理時間 2.5~7.5秒 Processing time 2.5~7.5 seconds

其他代表性之添加金屬例如有Fe、Ni、Cr、W、V等。此外,亦可選擇、且添加複數種之上述金屬。 Other representative addition metals are, for example, Fe, Ni, Cr, W, V, and the like. Further, a plurality of the above metals may be selected and added.

實施例4係以圖8所示之給電軸20作為陽極、以給電電極20作為陰極,並利用下列條件來進行粗糙化處理。 In the fourth embodiment, the power supply shaft 20 shown in Fig. 8 was used as an anode, and the electric current electrode 20 was used as a cathode, and the roughening treatment was carried out under the following conditions.

表面粗糙化處理條件 Surface roughening treatment conditions

一般之銅電解液(硫酸銅40~250 g/l、硫酸30~210 g/l、鹽酸10~800 ppm、如光澤劑等之添加劑,以製造商之指定量來製備)中,電解液溫度係維持18~32℃,並設定1A/dm2之電流密度。 Generally copper electrolyte (copper sulfate 40~250 g/l, sulfuric acid 30~210 g/l, hydrochloric acid 10~800 ppm, additives such as brightener, prepared by the manufacturer's specified amount), electrolyte temperature Maintain 18~32 °C and set the current density of 1A/dm 2 .

電流密度比1A/dm2低時,銅電鍍量將會過少,幾乎連銅微粒也無法析出。因此,實施例4中係以8A/dm2來進行。當提高電流密度時,由於析出的銅微粒增加,必要時可藉由控制電流密度,來控制銅微粒之析出量。 When the current density is lower than 1 A/dm 2 , the amount of copper plating will be too small, and almost no copper particles can be precipitated. Therefore, in Example 4, it was carried out at 8 A/dm 2 . When the current density is increased, the amount of precipitated copper particles is increased, and if necessary, the amount of precipitation of copper particles can be controlled by controlling the current density.

實施例2、3 Example 2, 3

實施例2、3係採用壓延銅箔,對上述銅箔進行與實施例1相同之表面處理。 In Examples 2 and 3, a rolled copper foil was used, and the copper foil was subjected to the same surface treatment as in Example 1.

實施例2與比較例2 Example 2 and Comparative Example 2

本實施例係使用日本製箔股份有限公司所製之低粗糙度壓延銅箔(接點用銅)。 In the present embodiment, a low-roughness rolled copper foil (copper for contacts) made by Nippon Foil Co., Ltd. was used.

實施例3 Example 3

本實施例係使用日本製箔股份有限公司所製之含錫(0.15wt%)之銅合金箔(C14410)。 In the present embodiment, a tin-containing (0.15 wt%) copper alloy foil (C14410) made by Nippon Foil Co., Ltd. was used.

實施例4 Example 4

實施例4係使用實施例1相同之電解銅箔,以給電軸20作為陽極、以給電電極20作為陰極,以與實施例1相同之表面粗糙化處理條件,於箔表面上生成銅微粒(0.1μm~3.5μm),接著,於處理槽4中進行水洗。水洗用之處理槽於圖2中雖僅繪示出一個槽,但必要時可增加水洗用的處理槽。接著,必要時,於其後之乾燥製程中,於銅箔不變色之情況下,可增設防鏽處理槽5以進行防鏽處理,並於漿體塗佈前稍為進行乾燥。 In the embodiment 4, the same electrolytic copper foil as in the first embodiment was used, and the electric axis 20 was used as the anode and the electric electrode 20 was used as the cathode. The surface roughening treatment conditions similar to those in the example 1 were carried out to form copper particles on the surface of the foil (0.1). Μm~3.5 μm), followed by water washing in the treatment tank 4. Although the treatment tank for washing is shown in Fig. 2, only one tank is shown, but if necessary, the treatment tank for water washing can be added. Next, if necessary, in the subsequent drying process, in the case where the copper foil does not change color, the rust-preventing treatment tank 5 may be added to perform rust-preventing treatment, and may be slightly dried before the slurry coating.

粗糙化粒子賦予後之特性值一併列入表格3中。 The property values assigned by the roughened particles are listed in Table 3.

〔Rz值、表面積、結晶粒徑之測定〕 [Measurement of Rz value, surface area, crystal grain size]

銅箔正反面之Rz值係以小坂研究所製之SE-3C型測量裝置來測定,粗糙化粒子賦予處理後之銅箔表面積係以KEYENCE公司製之VK-8500來測量。結晶構造之粒徑剖面係利用眼睛目測掃描式電子顯微鏡所拍攝之SEM影像來判斷。 The Rz value of the front and back of the copper foil was measured by a SE-3C type measuring apparatus manufactured by Otaru Laboratory, and the surface area of the copper foil after the roughening particle treatment was measured by VK-8500 manufactured by KEYENCE. The particle size profile of the crystal structure was judged by an SEM image taken by an eye visual scanning electron microscope.

活性物質造粒 Active material granulation

活性物質可採用矽(SiO),並混合矽(SiO)、乙炔炭黑、PVDF(聚偏氯乙烯樹脂)、NMP(1-甲基-2-吡咯烷酮),以形成漿體。 The active material may be cerium (SiO) mixed with cerium (SiO), acetylene black, PVDF (polyvinylidene chloride resin), NMP (1-methyl-2-pyrrolidone) to form a slurry.

活性物質層之形成 Formation of active material layer

將各實施例、比較例之銅箔分別作為集電體,並將上述漿狀所形成之活性物質塗佈於上述集電體上,進行加溫乾燥、加熱壓合,形成矽類堆積層(活性物質層),以製作具有活性物質之銅箔。 Each of the copper foils of the examples and the comparative examples is used as a current collector, and the active material formed in the slurry form is applied onto the current collector, and dried by heating and pressure-bonding to form a ruthenium-based buildup layer ( The active material layer) is used to produce a copper foil having an active material.

為了使利用淋幕式平面塗裝機之塗佈容易進行,活性物質混合體為揮發性溶劑,以調整成適當之漿體黏度。此外,在此係利用淋幕式平面塗裝機來塗佈活性物質混合體之方法,但利用其他之滾輪之塗佈方法等也可適用。 In order to facilitate the application by the curtain type flat coater, the active material mixture is a volatile solvent to adjust to a suitable slurry viscosity. Further, although a method of applying an active material mixture by a curtain type flat coater is used here, it is also applicable to a coating method using other rolls.

以具有活性物質層之金屬薄製造方法,添加以活性物質、黏合劑為主成分、必要時亦可加調整黏度之增黏材料或導電助劑,來進行混練。將混練所成之活性物質混合體塗佈於析出金屬粒子之金屬箔表面,乾燥後利用熱輪壓合法,使金屬粒子與活性物質強烈接觸,由於一部份作為導電助劑之金屬粒子將分散於活性物質層表面,可降低活性物質層與集電體(金屬箔)之接觸阻抗。另外,由於一部份作為導電助劑之粗糙化處理層,將由金屬箔表面朝活性物質層內部安置,且由於導電性具有由金屬箔表面朝活性物質層內部減少之傾向,與金屬箔之接觸面積,比起一般施以膠囊電鍍之銅箔,可將其接觸面積形成最大值,進而 可貢獻於電池之循環特性。 The method of manufacturing a thin metal having an active material layer is carried out by adding an active material or a binder as a main component, and if necessary, a viscosity-increasing material or a conductive auxiliary agent may be added to adjust the viscosity. The active material mixture formed by the kneading is applied to the surface of the metal foil on which the metal particles are deposited, and after drying, the metal particles are strongly contacted with the active material by heat-pressing, and a part of the metal particles as the conductive auxiliary agent will be dispersed. On the surface of the active material layer, the contact resistance between the active material layer and the current collector (metal foil) can be lowered. In addition, since a part of the roughening treatment layer as a conductive auxiliary agent is disposed from the surface of the metal foil toward the inside of the active material layer, and since the conductivity has a tendency to decrease from the surface of the metal foil toward the inside of the active material layer, contact with the metal foil The area is larger than the copper foil which is usually applied by capsule plating, and the contact area is maximized. Can contribute to the cycle characteristics of the battery.

負極集電體之安裝與評估係以下列條件來進行。 The installation and evaluation of the anode current collector were carried out under the following conditions.

〔電解池之製作〕 [Production of Electrolysis Cell]

將所製作之負極集電體作為電極,於充滿氬氣之手套箱中,來製作三電極式電解池。電解池係由在充滿於玻璃容器內之電解液中,浸入反對極(正極)、作用極(負極)、及參考電極來構成。 The produced negative electrode current collector was used as an electrode, and a three-electrode electrolytic cell was fabricated in an argon-filled glove box. The electrolytic cell is composed of an anti-electrode (positive electrode), a working electrode (negative electrode), and a reference electrode in an electrolytic solution filled in a glass container.

電解液係利用相對於碳酸乙烯酯與碳酸二乙酯以3:7之體積比所混合之溶劑,溶解1莫耳/升之LiPF6所形成之電解液。反對極與參考電極係利用鋰金屬。 The electrolytic solution was obtained by dissolving 1 mol/liter of LiPF 6 with respect to a solvent in which a ratio of ethylene carbonate to diethyl carbonate was 3:7 by volume. The counter electrode and the reference electrode system utilize lithium metal.

充放電循環特性之評估 Evaluation of charge and discharge cycle characteristics

於25℃下以4mA之定電流,使作用極(負極)達0V(v.s.Li/Li+)之電位對上述所製作之電解池進行充電,之後,以4mA之定電流,使作用極(負極)達2V(v.s.Li/Li+)之電位進行放電,於充放電效率100循環之後來進行放電容量維持率之評估。 The electrolytic cell prepared by charging the working electrode (negative electrode) at a potential of 0 V (vsLi/Li + ) at a constant current of 4 mA at 25 ° C, and then applying a current of 4 mA to the working electrode (negative electrode) The potential was increased to a potential of 2 V (vsLi/Li + ), and the discharge capacity retention rate was evaluated after 100 cycles of charge and discharge efficiency.

其評估結果一併列於表格3中。 The results of the assessment are listed in Table 3.

外,對重複進行300循環之充放電後之銅箔的龜裂/斷裂的有無,進行確認,其結果也一併列於表格3中。 In addition, the presence or absence of cracking/fracture of the copper foil after repeated charge and discharge for 300 cycles was confirmed, and the results are also shown in Table 3.

如表格3所示,實施例1之集電體中,其基體銅箔之Rz值之差異於標準值內,其賦予粗糙化粒子後之粗糙化粒子粒徑、表面積也均於標準值內。 As shown in Table 3, in the current collector of Example 1, the Rz value of the base copper foil was different from the standard value, and the roughened particle diameter and surface area after the roughened particles were supplied were also within the standard values.

以實施例1之銅箔作為集電體所製作之電解池電池中所進行之充放電循環特性的評估,完全符合標準,重複進 行300循環之充放電之後的集電體中,也沒有發現龜裂/斷裂的現象。 The evaluation of the charge-discharge cycle characteristics of the electrolytic cell battery fabricated by using the copper foil of Example 1 as a current collector completely conforms to the standard and is repeated. No cracking/fracture was observed in the current collector after charging and discharging for 300 cycles.

實施例2、實施例3之基體銅箔係採用壓延銅箔,進行與上述實施例1之電解銅箔相同之粗糙化處理,並以上述粗糙化處理壓延銅箔作為集電體,與實施例1相同來進行電池的組裝,並進行其電池特性之評估。其結果與實施例1共同列於表格3中。 The base copper foil of Example 2 and Example 3 was subjected to the same roughening treatment as the electrolytic copper foil of the above-described Example 1 by using a rolled copper foil, and the roughened copper foil was used as the current collector, and the examples were as follows. The same is done for the assembly of the battery and the evaluation of its battery characteristics. The results are shown in Table 3 together with Example 1.

另一方面,比較例1雖與實施例1相同使用未處理之銅箔,但其粗糙化處理後之兩表面之粗糙度Rz值變大,因此充放電效率100循環後之放電容量維持率無法符合標準值。 On the other hand, in Comparative Example 1, the untreated copper foil was used in the same manner as in Example 1, but the roughness Rz value of both surfaces after the roughening treatment was increased, so that the discharge capacity retention rate after 100 cycles of charge and discharge efficiency could not be obtained. Meet the standard value.

此外,比較例1中,於重覆進行300循環充放電後之集電體發現有龜裂/斷裂的現象。 Further, in Comparative Example 1, a phenomenon of cracking/fracture was observed in the current collector after repeated charge and discharge for 300 cycles.

根據本發明,不僅可提升鋰離子二次電池之單位體積的能量密度,也可抑制於充放電時集電體之皺折、龜裂斷裂等變形之問題發生,即使重覆進行充放電循環,也可提供一種具有不會引起容量降低之高壽命、以及可進行小型化之鋰離子二次電池。 According to the present invention, not only the energy density per unit volume of the lithium ion secondary battery but also the problem of deformation such as wrinkles and cracks of the current collector during charge and discharge can be suppressed, and even if the charge and discharge cycle is repeated, It is also possible to provide a lithium ion secondary battery which has a high life without causing a decrease in capacity and which can be miniaturized.

1‧‧‧金屬箔 1‧‧‧metal foil

2‧‧‧表面粗糙化處理槽 2‧‧‧Surface roughening treatment tank

3‧‧‧粗糙化金屬層 3‧‧‧Roughened metal layer

4‧‧‧水洗處理槽 4‧‧‧Washing treatment tank

5‧‧‧防鏽處理槽 5‧‧‧Anti-rust treatment tank

6‧‧‧儲料槽 6‧‧‧ hopper

7‧‧‧儲料槽 7‧‧‧ hopper

8‧‧‧活性物質混合體 8‧‧‧Active substance mixture

9‧‧‧乾燥裝置 9‧‧‧Drying device

10‧‧‧乾燥裝置 10‧‧‧Drying device

11‧‧‧壓合機 11‧‧‧Compression machine

12‧‧‧捲取機 12‧‧‧Winding machine

13‧‧‧薄膜 13‧‧‧film

14‧‧‧薄膜供給裝置 14‧‧‧ film supply device

15‧‧‧薄膜供給裝置 15‧‧‧film supply device

16‧‧‧貼合裝置 16‧‧‧Fitting device

20‧‧‧給電電極 20‧‧‧Power electrode

22、24、26‧‧‧電極 22, 24, 26‧‧‧ electrodes

31、32‧‧‧活性物質層 31, 32‧‧‧ active material layer

33‧‧‧活性物質 33‧‧‧Active substances

35‧‧‧金屬粒子 35‧‧‧Metal particles

37‧‧‧黏合劑(導電材料) 37‧‧‧Binder (conductive material)

圖1係繪示根據第一實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 1 is a flow chart showing the manufacture of a metal foil having a coating layer according to the first embodiment.

圖2係繪示根據第一實施形態所示之具有被覆層之金屬箔之剖面圖。 Fig. 2 is a cross-sectional view showing a metal foil having a coating layer according to the first embodiment.

圖3係繪示根據第二實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 3 is a flow chart showing the manufacture of a metal foil having a coating layer according to the second embodiment.

圖4係繪示根據第二實施形態所示之具有被覆層之金屬箔之剖面圖。 Fig. 4 is a cross-sectional view showing a metal foil having a coating layer according to a second embodiment.

圖5係繪示根據第三實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 5 is a flow chart showing the manufacture of a metal foil having a coating layer according to a third embodiment.

圖6係繪示根據第三實施形態所示之具有被覆層之金屬箔之剖面圖。 Fig. 6 is a cross-sectional view showing a metal foil having a coating layer according to a third embodiment.

圖7係繪示根據第四實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 7 is a flow chart showing the manufacture of a metal foil having a coating layer according to a fourth embodiment.

圖8係繪示根據第四實施形態所示之具有被覆層之金屬箔之剖面圖。 Fig. 8 is a cross-sectional view showing a metal foil having a coating layer according to a fourth embodiment.

圖9係繪示根據第五實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 9 is a flow chart showing the manufacture of a metal foil having a coating layer according to a fifth embodiment.

圖10係繪示根據第五實施形態所示之具有被覆層之金屬箔之製造裝置。 Fig. 10 is a view showing a manufacturing apparatus of a metal foil having a coating layer according to a fifth embodiment.

圖11係繪示根據第六實施形態所示之具有被覆層之金屬箔之製造裝置。 Fig. 11 is a view showing a manufacturing apparatus of a metal foil having a coating layer according to a sixth embodiment.

圖12係繪示根據第六實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 12 is a flow chart showing the manufacture of a metal foil having a coating layer according to a sixth embodiment.

圖13係繪示根據第七實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 13 is a flow chart showing the manufacture of a metal foil having a coating layer according to the seventh embodiment.

圖14係繪示根據第七實施形態所示之具有被覆層之金屬箔之製造裝置說明圖。 Fig. 14 is an explanatory view showing a manufacturing apparatus of a metal foil having a coating layer according to a seventh embodiment.

圖15係繪示根據第八實施形態所示之具有被覆層之金屬箔之製造流程圖。 Fig. 15 is a flow chart showing the manufacture of a metal foil having a coating layer according to the eighth embodiment.

圖16係繪示根據第八實施形態所示之具有被覆層之金屬箔之製造裝置說明圖。 Fig. 16 is an explanatory view showing a manufacturing apparatus of a metal foil having a coating layer according to an eighth embodiment.

10‧‧‧金屬箔 10‧‧‧metal foil

11‧‧‧游離金屬離子 11‧‧‧Free metal ions

12‧‧‧塗佈樹脂 12‧‧‧ Coating resin

Claims (34)

一種具有被覆層之金屬箔,於金屬箔之至少一表面上配置被覆層,上述被覆層中包含游離金屬粒子。 A metal foil having a coating layer on which a coating layer is disposed on at least one surface of the metal foil, and the coating layer contains free metal particles. 如申請專利範圍第1項所述之具有被覆層之金屬箔,其中上述被覆層為包含游離金屬粒子之可再熔之樹脂組成物。 The metal foil with a coating layer according to claim 1, wherein the coating layer is a remeltable resin composition containing free metal particles. 如申請專利範圍第1項所述之具有被覆層之金屬箔,其中上述被覆層為包含游離金屬粒子之活性物質層。 The metal foil with a coating layer according to claim 1, wherein the coating layer is an active material layer containing free metal particles. 如申請專利範圍第1項所述之具有被覆層之金屬箔,其中上述被覆層為包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上方配置有活性物質層。 The metal foil with a coating layer according to claim 1, wherein the coating layer is a remeltable resin composition layer containing free metal particles, and an active material layer is disposed above the resin composition layer. 一種具有被覆層之金屬箔,配置粗糙化處理層於金屬箔之至少一表面上,配置被覆層於上述粗糙化處理層上,上述被覆層中包含游離金屬粒子。 A metal foil having a coating layer on which at least one surface of a metal foil is disposed, and a coating layer is disposed on the roughened layer, wherein the coating layer contains free metal particles. 如申請專利範圍第5項所述之具有被覆層之金屬箔,其中上述被覆層中所包含之游離金屬粒子係由上述粗糙化處理層中所游離出之金屬粒子。 The metal foil having a coating layer according to claim 5, wherein the free metal particles contained in the coating layer are metal particles liberated from the roughening treatment layer. 如申請專利範圍第5或6項所述之具有被覆層之金屬箔,其中上述被覆層為可再熔之樹脂組成物。 A metal foil having a coating layer according to the invention of claim 5, wherein the coating layer is a remeltable resin composition. 如申請專利範圍第5或6項所述之具有被覆層之金屬箔,其中上述被覆層為活性物質層。 A metal foil having a coating layer according to claim 5 or 6, wherein the coating layer is an active material layer. 如申請專利範圍第5或6項所述之具有被覆層之金屬箔,其中上述被覆層為可再熔之樹脂組成物層,於上述樹脂組成物層上方配置有活性物質層。 The metal foil having a coating layer according to claim 5, wherein the coating layer is a remeltable resin composition layer, and an active material layer is disposed above the resin composition layer. 如申請專利範圍第1至9項中任一項所述之具有被覆層之金屬箔,其中上述金屬箔為電解銅箔或壓延銅箔。 The metal foil having a coating layer according to any one of claims 1 to 9, wherein the metal foil is an electrolytic copper foil or a rolled copper foil. 如申請專利範圍第1至9項中任一項所述之具有被覆層之金屬箔,其中上述游離金屬粒子之粒徑為0.05 μm~3.5 μm。 The metal foil having a coating layer according to any one of claims 1 to 9, wherein the free metal particles have a particle diameter of 0.05 μm to 3.5 μm. 如申請專利範圍第5至9項中任一項所述之具有被覆層之金屬箔,其中上述粗糙化處理層為包含銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦中至少一種以上之金屬之粗糙化處理層。 The metal foil with a coating layer according to any one of claims 5 to 9, wherein the roughening treatment layer comprises at least copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium. A roughening treatment layer of more than one metal. 一種具有被覆層之金屬箔,於如申請專利範圍第1至9項中任一項所述之具有被覆層之金屬箔之至少最外層之表面上,配置有薄膜或脫模紙。 A metal foil having a coating layer on which a film or a release paper is disposed on a surface of at least the outermost layer of the metal foil having a coating layer according to any one of claims 1 to 9. 一種二次電池用電極,於金屬箔之至少一表面上配置有活性物質層,上述活性物質層中包含游離金屬粒子。 An electrode for a secondary battery, wherein an active material layer is disposed on at least one surface of the metal foil, and the active material layer contains free metal particles. 一種二次電池用電極,於金屬箔之至少一表面上配置有包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 An electrode for a secondary battery in which a remeltable resin composition layer containing free metal particles is disposed on at least one surface of a metal foil, and an active material layer is disposed on the resin composition layer. 一種二次電池用電極,於金屬箔之至少一表面上配置有粗糙化處理層,於上述粗糙化處理層上配置有活性物質層,上述活性物質層中包含游離金屬粒子。 An electrode for a secondary battery, wherein a roughened layer is disposed on at least one surface of the metal foil, and an active material layer is disposed on the roughened layer, and the active material layer contains free metal particles. 如申請專利範圍第16項所述之二次電池用電極,其中上述活性物質層中所包含之游離金屬粒子係由上述粗糙化處理層中所游離出之金屬粒子。 The electrode for a secondary battery according to claim 16, wherein the free metal particles contained in the active material layer are metal particles liberated from the roughened layer. 一種二次電池用電極,於金屬箔之至少一表面上 配置有粗糙化處理層,於上述粗糙化處理層上配置有包含游離金屬粒子之可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 An electrode for a secondary battery on at least one surface of a metal foil A roughening treatment layer is disposed, and a remeltable resin composition layer containing free metal particles is disposed on the roughening treatment layer, and an active material layer is disposed on the resin composition layer. 如申請專利範圍第16項所述之二次電池用電極,其中上述可再熔之樹脂組成物層中所包含之游離金屬粒子係由上述粗糙化處理層中所游離出之金屬粒子。 The electrode for a secondary battery according to claim 16, wherein the free metal particles contained in the remeltable resin composition layer are metal particles liberated from the roughened layer. 如申請專利範圍第14至17項中任一項所述之二次電池用電極,其中上述金屬箔為電解銅箔或壓延銅箔。 The electrode for a secondary battery according to any one of claims 14 to 17, wherein the metal foil is an electrolytic copper foil or a rolled copper foil. 如申請專利範圍第14至17項中任一項所述之二次電池用電極,其中上述游離金屬粒子之粒徑為0.05 μm~3.5 μm。 The electrode for a secondary battery according to any one of claims 14 to 17, wherein the free metal particles have a particle diameter of 0.05 μm to 3.5 μm. 如申請專利範圍第14至17項中任一項所述之二次電池用電極,其中上述粗糙化處理層係以包含銅、鎳、錳、鐵、鉻、鎢、鉬、釩、銦中至少一種以上之金屬之電鍍槽,進行處理所形成之粗糙化處理層。 The electrode for a secondary battery according to any one of claims 14 to 17, wherein the roughening treatment layer contains at least at least copper, nickel, manganese, iron, chromium, tungsten, molybdenum, vanadium, and indium. One or more metal plating baths are subjected to a roughened treatment layer formed by the treatment. 一種二次電池用電極,於如申請專利範圍第14至18項中任一項所述之二次電池用電極之至少最外層之表面上,配置有薄膜或脫模紙。 An electrode for a secondary battery, wherein a film or a release paper is disposed on a surface of at least the outermost layer of the electrode for a secondary battery according to any one of claims 14 to 18. 如申請專利範圍第21項所述之二次電池用電極,其中上述薄膜係電池用隔板。 The electrode for a secondary battery according to claim 21, wherein the film is a separator for a battery. 一種具有被覆層之金屬箔之製造方法,於金屬箔之至少一表面上配置有被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔,對金屬箔表面,利用電鍍槽、並通以極限電流密度以 上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上形成被覆層;於被覆層中混入一部份之上述粗糙化處理粒子,以作為游離金屬粒子。 A method for producing a metal foil having a coating layer, wherein a coating layer is disposed on at least one surface of the metal foil, wherein the coating layer includes a metal foil having a coating layer of free metal particles, and the surface of the metal foil is coated with a plating bath Passing the limit current density a current is applied to form a roughened layer having a particle diameter of 0.1 μm to 3.5 μm; a coating layer is formed on the roughening layer; and a part of the roughened particles are mixed in the coating layer to serve as a free metal particle. 如申請專利範圍第23項所述之具有被覆層之金屬箔之製造方法,其中上述被覆層為可再熔之樹脂組成物層。 The method for producing a metal foil having a coating layer according to claim 23, wherein the coating layer is a remeltable resin composition layer. 如申請專利範圍第23項所述之具有被覆層之金屬箔之製造方法,其中上述被覆層為活性物質層。 The method for producing a metal foil having a coating layer according to claim 23, wherein the coating layer is an active material layer. 如申請專利範圍第23項所述之具有被覆層之金屬箔之製造方法,其中上述被覆層為可再熔之樹脂組成物層,於上述樹脂組成物層上配置有活性物質層。 The method for producing a metal foil having a coating layer according to claim 23, wherein the coating layer is a remeltable resin composition layer, and an active material layer is disposed on the resin composition layer. 一種具有被覆層之金屬箔之製造方法,於金屬箔之至少一表面上配置有被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔,對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上,塗佈上添加有活性物質、黏合劑、必要時可添加增黏劑、與漿體等所混合而成之活性物質混合體,以形成活性物質層;對形成有上述活性物質層之金屬箔,進行乾燥、加壓,以將上述金屬處理粒子帶入活性物質層中,作為導電助劑;使上述活性物質層中包含上述粗糙化處理粒子,以作為游離金屬粒子。 A method for producing a metal foil having a coating layer, wherein a coating layer is disposed on at least one surface of the metal foil, wherein the coating layer includes a metal foil having a coating layer of free metal particles, and the surface of the metal foil is coated with a plating bath Passing a current above the limiting current density to form a roughened layer having a particle diameter of 0.1 μm to 3.5 μm; on the roughening layer, an active material, a binder, and a viscosity-increasing layer may be added to the coating. a mixture of active materials mixed with a slurry or a slurry to form an active material layer; and drying and pressurizing the metal foil on which the active material layer is formed to bring the metal-treated particles into the active material layer In the above, the conductive material layer contains the roughened particles as the free metal particles. 一種具有被覆層之金屬箔之製造方法,係於金屬箔之至少一表面上配置被覆層,上述被覆層中包含游離金屬粒子之具有被覆層之金屬箔,對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;於上述粗糙化處理層上,形成可再熔之樹脂組成物層;於上述樹脂組成物層上,塗佈上添加有活性物質、黏合劑、必要時可添加增黏劑、與漿體等所混合而成之活性物質混合體,以形成活性物質層;及對形成有上述樹脂組成物層、與上述活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入樹脂組成物層中,來作為游離金屬粒子。 A method for producing a metal foil having a coating layer, wherein a coating layer is disposed on at least one surface of a metal foil, wherein the coating layer includes a metal foil having a coating layer of free metal particles, and a surface of the metal foil is coated with a plating bath a roughening treatment layer having a particle diameter of 0.1 μm to 3.5 μm is formed by a current exceeding a limit current density; a remeltable resin composition layer is formed on the roughening treatment layer; and the resin composition layer is formed on the resin composition layer And an active material mixture in which an active material, a binder, a tackifier, a slurry, or the like may be added to the coating to form an active material layer; and the resin composition layer is formed, The metal foil of the active material layer is dried and pressurized to bring the roughened particles into the resin composition layer to form free metal particles. 一種二次電池用電極,利用以如申請專利範圍第23~28項所述之具有被覆層之金屬箔之製造方法所製造之金屬箔。 An electrode for a secondary battery, which is a metal foil produced by the method for producing a metal foil having a coating layer as described in claims 23 to 28. 一種二次電池用電極之製造方法,包括:表面粗糙化處理步驟,對金屬箔之表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;活性物質造粒步驟,添加活性物質、黏合劑、必要時可添加增黏劑、與漿體等,進行混合;第一活性物質層形成步驟,於上述粗糙化處理層之一表面上,塗佈上於上述活性物質造粒步驟中所製造之活性物質混合體; 第二活性物質層形成步驟,於薄膜上層積上述活性物質混合體,並層積於金屬箔之另一表面上;及乾燥加壓步驟,對具有以上述第一、與第二步驟中所形成之活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入活性物質層中,來作為導電助劑,上述粗糙化處理粒子將作為游離金屬粒子,包含於活性物質層中。 A method for manufacturing an electrode for a secondary battery, comprising: a surface roughening treatment step of forming a surface having a particle diameter of 0.1 μm to 3.5 μm by using a plating bath and a current exceeding a limiting current density on a surface of the metal foil; a treatment layer; an active material granulation step, adding an active material, a binder, and if necessary, adding a tackifier, and a slurry, etc.; mixing; a first active material layer forming step on one surface of the roughening treatment layer Upper, applying the active substance mixture produced in the above-mentioned active material granulation step; a second active material layer forming step of laminating the active material mixture on the film and laminating on the other surface of the metal foil; and drying and pressurizing the step, having the first step and the second step formed The metal foil of the active material layer is dried and pressurized to bring the roughened particles into the active material layer to serve as a conductive auxiliary agent, and the roughened particles are contained as free metal particles in the active material layer. in. 一種二次電池用電極之製造方法,包括:表面粗糙化處理步驟,對金屬箔表面,利用電鍍槽、並通以極限電流密度以上之電流,以形成粒徑為0.1 μm~3.5 μm之粗糙化處理層;樹脂組成物層形成步驟,於上述粗糙化處理層上,形成可再熔之樹脂組成物層;活性物質造粒步驟,添加活性物質、黏合劑、必要時可添加增黏劑、與漿體等,進行混合;第一活性物質層形成步驟,於上述樹脂組成物層之一表面上,塗佈上於上述活性物質造粒步驟中所製造之活性物質混合體;第二活性物質層形成步驟,於薄膜上層積上述活性物質混合體,並層積於樹脂組成物層之另一表面上;及乾燥加壓步驟,對具有以上述第一、與第二步驟中所形成之活性物質層之金屬箔,進行乾燥‧加壓,以將上述粗糙化處理粒子帶入活性物質層中,來作為導電助劑,上述粗糙化處理粒子將作為游離金屬粒子,包含於活性物質 層中。 A method for manufacturing an electrode for a secondary battery, comprising: a surface roughening treatment step of forming a roughening of a particle diameter of 0.1 μm to 3.5 μm by using a plating bath and a current exceeding a limiting current density on a surface of the metal foil a treatment layer forming step of forming a remeltable resin composition layer on the roughening treatment layer; an active material granulation step, adding an active material, a binder, and if necessary, adding a tackifier, and a slurry or the like, which is mixed; a first active material layer forming step, coated on the surface of one of the resin composition layers, coated with the active material mixture produced in the active material granulation step; and a second active material layer a forming step of laminating the active material mixture on the film and laminating on the other surface of the resin composition layer; and drying and pressurizing the pair to have the active material formed in the first and second steps The metal foil of the layer is dried and pressurized to bring the roughened particles into the active material layer to serve as a conductive auxiliary agent, and the roughened particles will be used as Free metal particles, containing the active substance In the layer. 一種鋰離子二次電池,利用如申請專利範圍第1至13項中任一項所述之金屬箔、或如申請專利範圍第23至28項中任一項所述之製造方法所製造之金屬箔、或如申請專利範圍第14至22項中任一項所述之二次電池用電極、或利用如申請專利範圍第30至31項中任一項所述之製造方法所製造之電極。 A lithium ion secondary battery using the metal foil according to any one of claims 1 to 13 or the metal produced by the manufacturing method according to any one of claims 23 to 28 A foil, or an electrode for a secondary battery according to any one of claims 14 to 22, or an electrode produced by the production method according to any one of claims 30 to 31.
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