WO2006095683A1 - Negative electrode collector for dry cell - Google Patents

Negative electrode collector for dry cell Download PDF

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Publication number
WO2006095683A1
WO2006095683A1 PCT/JP2006/304274 JP2006304274W WO2006095683A1 WO 2006095683 A1 WO2006095683 A1 WO 2006095683A1 JP 2006304274 W JP2006304274 W JP 2006304274W WO 2006095683 A1 WO2006095683 A1 WO 2006095683A1
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WO
WIPO (PCT)
Prior art keywords
negative electrode
current collector
electrode current
plating
dry battery
Prior art date
Application number
PCT/JP2006/304274
Other languages
French (fr)
Japanese (ja)
Inventor
Yukio Uchimoto
Kanae Yamagishi
Takashi Arima
Masaya Asakami
Shoji Imai
Original Assignee
Fukui Byora Co., Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Fukui Byora Co., Ltd. filed Critical Fukui Byora Co., Ltd.
Publication of WO2006095683A1 publication Critical patent/WO2006095683A1/en

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Classifications

    • 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
    • H01M4/665Composites
    • H01M4/667Composites in the form of layers, e.g. coatings
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10Electroplating with more than one layer of the same or of different metals
    • 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
    • C25D5/50After-treatment of electroplated surfaces by heat-treatment
    • 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
    • C25D7/0607Wires
    • 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
    • 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
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/75Wires, rods or strips
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/04Cells with aqueous electrolyte
    • H01M6/06Dry cells, i.e. cells wherein the electrolyte is rendered non-fluid
    • H01M6/08Dry cells, i.e. cells wherein the electrolyte is rendered non-fluid with cup-shaped electrodes

Definitions

  • the present invention relates to a negative electrode current collector for a dry cell, and more particularly, to a negative electrode current collector incorporated in an axial center portion of an alkaline dry cell or a nickel dry cell.
  • the negative electrode current collector disposed at the axial center portion of the alkaline dry battery is formed through a wire drawing process in which a wire made of brass or the like is inserted through the inside diameter of a wire drawing die of a predetermined diameter and drawn. .
  • the metal (Fe, Ni, Cr, Mo, W, V, As, etc.) constituting the die and the fine pieces made of these oxides are corroded on the surface of the current collector.
  • metal fine pieces that are fixed to the current collector in this way react with the zinc in the gelled negative electrode to generate hydrogen gas and raise the internal pressure of the battery. It will cause fluid leakage.
  • the surface of a brass-made wire is mechanically peeled off by polishing to remove metal fine particles that have been corroded and embedded in the surface of a current collector.
  • the technology disclosed in Patent Document 2 after copper or copper alloy wire drawing is pre-melted with tin, and then tin is further electrolessly plated on the surface of a current collector cut and formed into a predetermined shape. , The surface of the current collector is covered with a metal fine piece which is embedded.
  • the material cost is high because brass is used as a material, and mechanical force is also used to lengthen the cycle time as well as generate chips. There is a problem that labor and cost for processing are also strong.
  • Patent Document 2 is expensive because it uses wire drawing made of copper or a copper alloy to which molten plating of tin has been applied in advance, and the force is not uniform in outer diameter size, and further after molten plating. There is a problem that labor and cost for electrolessly plating tin also increase.
  • Patent Document 1 Japanese Patent Application Laid-Open No. 5-307961.
  • Patent Document 2 Japanese Patent Application Laid-Open No. 7-29573
  • the present invention has been made to solve the above-mentioned problems of the prior art, and it is possible to prevent the generation of hydrogen gas, and to reduce the manufacturing cost, cycle time It is an object of the present invention to provide a negative electrode current collector for a dry battery, which is short, easy to mass-produce, has high dimensional accuracy, and can produce a stable quality dry battery. Means to solve the problem
  • the invention described in claim 1 relates to a negative electrode current collector for a dry battery, characterized in that the surface of an iron wire rod formed in a predetermined shape by forging is subjected to a plating treatment. Do.
  • the invention according to claim 2 relates to the negative electrode current collector according to claim 1, wherein the plating treatment is performed by electrolytic plating.
  • the invention according to claim 3 relates to the negative electrode current collector for a dry battery according to claim 1 or 2, wherein the metal is zinc.
  • the invention according to claim 4 is characterized in that a passivation treatment is carried out after the plating treatment, and a sealing treatment is further carried out.
  • the present invention relates to any one of the negative electrode current collectors for dry batteries.
  • the invention according to claim 5 is characterized in that the metal layer has a two-layer structure in which the inner layer is made of copper and the outer layer is made of tin.
  • the present invention relates to a negative electrode current collector for a dry cell.
  • the invention according to claim 6 is that the negative electrode collection for a dry battery according to claim 1, wherein a reflow process is performed after the plating process. It relates to a collector.
  • the invention according to claim 7 is characterized in that the iron comprises not more than 0.30% by weight of carbon, the balance of iron and inevitable impurities.
  • the present invention relates to a negative electrode current collector for a dry cell described in 1.
  • the material cost can be suppressed at low cost and high strength as compared to copper and copper alloy.
  • a stable, high quality dry battery is obtained that can be bent at the time of transportation, at the time of label processing, at the time of incorporation into a battery, etc.
  • the surface of the material of the current collector and the metal fine pieces that bite into the surface of the current collector are covered with metal plating to prevent generation of hydrogen gas when incorporated into a dry battery. Is possible.
  • the processing cycle time is shortened and chips are not generated, so that the labor and cost of manufacturing can be suppressed, and mass production can be performed.
  • the plating process is performed by electrolytic plating, a stable and uniform film thickness of the film can be formed, and a current collector with high dimensional accuracy can be obtained. Can.
  • the resin when the negative electrode current collector is used by being incorporated into a dry cell, the resin is less likely to be damaged because the metal is zinc.
  • the passivation treatment is carried out after the matting treatment, whereby an oxide film is formed on the surface of the negative electrode current collector, and the corrosion resistance is improved. Therefore, when incorporated into a dry cell and used, the effect of preventing the generation of hydrogen gas is enhanced.
  • the negative electrode current collector is further inactivated due to the pore-sealing treatment. And corrosion resistance), and the effect of preventing the generation of hydrogen gas when used by incorporating it into a dry battery is further enhanced, and furthermore, the surface is smoothed to prevent damage to the packing when incorporated into the dry battery. Can.
  • the inner layer is coated with copper and the outer layer is coated with a double layer of tin plating, defects such as pinholes may be temporarily formed on the outer surface of the outer layer. Even so, the copper plating film on the inner layer prevents the iron material from being exposed, making it possible to more reliably prevent the generation of hydrogen gas.
  • the iron film comprising less than 0.30% by weight of carbon and the balance iron and the unavoidable impurities is used, so that the film can be formed in a short time. It can be formed uniformly, achieving reduced manufacturing costs and improved quality.
  • FIG. 1 is a front view showing an example of a negative electrode current collector for a dry cell according to the present invention.
  • the negative electrode current collector (1) according to the present invention has a cylindrical shaft (11) and a disk portion (12 having a diameter larger than that of a shaft provided near the proximal end of the shaft (11)). And a tapered conical portion (13) provided at the tip of the shaft portion (11).
  • FIG. 2 is a partially cutaway cross-sectional view of a dry battery incorporating the negative electrode current collector according to the present invention. As shown in FIG. 2, the negative electrode current collector (1) is located at the axial center of the dry battery (2). It is arranged.
  • the dry cell (2) includes a bottomed cylindrical metal container (21) which also serves as a positive electrode terminal, and a hollow cylindrical positive electrode which is pressure-formed at a predetermined pressure housed in the metal container (21). Material (22) and gelled negative electrode filled inside of positive electrode material (22) via separator (23) (24) and a negative electrode current collector (1) inserted into the gelled negative electrode (24) through the sealing cap (25) and the gasket (26).
  • a dry battery in which the negative electrode current collector according to the present invention is incorporated in addition to a general alkaline dry battery using manganese dioxide as a main component of the positive electrode material, as a main component of the positive electrode material.
  • a nickel dry battery using nickel oxyhydride eg, Oxyride dry battery (trade name) manufactured by Matsushita Electric Industrial Co., Ltd.
  • Oxyride dry battery (trade name) manufactured by Matsushita Electric Industrial Co., Ltd.) can be mentioned.
  • the negative electrode current collector (1) according to the present invention is manufactured through the following steps.
  • the first step is a step of subjecting the wire to drawing (wire drawing) with a die
  • the second step is a step of cutting the drawn wire into a predetermined size, and these steps are specific steps. Is performed as follows.
  • the wire rod (1A) is fed between the feed rolls (2A) and (2B) as shown in FIG. 3 and supplied to the through hole (71) of the die (7) by rotating the hole.
  • the tip of the wire (1A) coming out of the through hole (71) is received by the stock bar (8), and cut into a predetermined size by the cutting knife (9).
  • the material of the wire rod (1A) is iron.
  • the reason for using an iron wire rod is because there are the following advantages as compared with the case where copper or a copper alloy is used conventionally.
  • electrolytic plating is easier than copper and copper alloys, so that it is easy to apply and requires less time for plating, which reduces the cost of plating and facilitates mass production. Also, since no exposure of the substrate occurs, no hydrogen gas is generated when it is incorporated into a dry cell.
  • iron composed of not more than 0.30% by weight of carbon, the balance of iron and unavoidable impurities, as iron to be a material of the wire rod.
  • iron having a carbon content of not more than 0.30% by weight is used, a coating film can be formed uniformly in a short time during coating treatment, thereby achieving reduction in manufacturing cost and improvement in quality. It is because it can.
  • the third step is a step of subjecting a wire rod cut to a predetermined size to cold forging (cold forging) to form it into a predetermined shape (shape shown in FIG. 1), and this step is a specific step. Is done as follows.
  • the wire (1A) cut to a predetermined size is pushed into the die (4) with the first punch (3) having the wide diameter opening (31) as shown in FIG.
  • the tapered end (41) provided at the end of the end portion performs a drawing process to form a truncated cone portion (13), and the base end portion thereof is the wide diameter opening (31) of the first punch (3). Expand the diameter with (see Figure 5).
  • the second punch (5) having a circular recess (51) is further pressed to the die (4) side to make the wire rod (1A)
  • a disc (12) is formed at the base end, and then, as shown in FIG. 7, the second punch (5) is retracted and the wire (1A) is pushed out with the knock out pin (6).
  • (10) is a mold main body, (6A) is a knockout rod attached with a knockout pin, and the knockout rod (6A) is moved in the pushing direction.
  • the illustration of the moving means for causing the movement is omitted.
  • the negative electrode current collector of the present invention as described above is formed into a predetermined shape only by forging, the processing cycle time becomes short, and no cutting force is generated. Cost is reduced and mass production is possible.
  • the fourth step is a step of subjecting the surface of the iron wire rod, which has been formed into a predetermined shape by forging processing, to a tacking treatment.
  • Zinc plating or tin plating is performed as the plating treatment. This is because zinc and tin have high hydrogen overvoltage !, and are suitable for suppressing the generation of hydrogen gas!
  • Zinc plating is performed by electrolytic plating.
  • Tin plating may be electrolytic plating or nonelectrolytic plating. However, in the present invention, electrolytic plating is preferred.
  • the reason is that, since electrolytic plating is performed, a stable and uniform film thickness is formed, and a negative electrode current collector with high dimensional accuracy can be obtained.
  • the thickness of zinc plating or tin plating is 2 to 5 ⁇ m.
  • the material surface of the current collector itself and the metal constituting the die cut into the surface (Fe, N i, Cr, Mo, W, V, As, etc.) and metal fine pieces made of these acid oxides, which can be coated to prevent generation of hydrogen gas when incorporated into a dry cell. Become.
  • tin plating is performed as the matting treatment in the fourth step, only tin plating may be performed, but by applying copper plating to the surface of the iron wire rod and then applying tin plating, the inner layer becomes copper plating, It is preferred that the outer layer form a tin-meat two-layer structure.
  • each layer in this case is, for example, 1 to 2 / ⁇ for the copper layer in the inner layer, and 2 to 5 ⁇ m for the tin layer in the outer layer.
  • the copper plating film on the inner layer prevents the iron material from being exposed, and hydrogen gas can be used. It becomes possible to prevent occurrence more reliably.
  • the anode current collector according to the present invention is subjected to a passivation treatment as a fifth step.
  • the passivation treatment is performed by etching the surface of the negative electrode current collector after plating to activate it, and then immersing in an acidic solution such as nitric acid.
  • sealing treatment is applied as a sixth step.
  • the pore-sealing treatment is performed by immersing the passivation-treated negative electrode current collector in a solution containing a surfactant.
  • the negative electrode current collector is further inactivated (it becomes difficult to be oxidized and the corrosion resistance is improved), and the effect of preventing the generation of hydrogen gas is further enhanced when incorporated into a dry battery. Can. Furthermore, since the surface is smoothed, the effect of preventing damage to the packing when being incorporated into the dry battery is also obtained.
  • the conditions for the reflow process are, for example, a heating temperature of 220 to 260 ° C. (preferably about 250 ° C.) and a heating time of 5 to 15 seconds (preferably about 10 seconds).
  • the defect is repaired, and at the same time, the tin plating surface is cured.
  • the present invention can be used as a negative electrode current collector incorporated in an alkaline dry battery or a nickel dry battery.
  • FIG. 1 is a front view showing an example of a negative electrode current collector for a dry cell according to the present invention.
  • FIG. 2 is a partially cutaway sectional view of a dry battery incorporating the negative electrode current collector for a dry battery according to the present invention.
  • FIG. 3 is a view showing a first step and a second step of a manufacturing process of a negative electrode current collector for a dry battery according to the present invention.
  • FIG. 4 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
  • FIG. 5 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
  • FIG. 6 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
  • FIG. 7 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention. Explanation of sign

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  • Engineering & Computer Science (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
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Abstract

Disclosed is a negative electrode collector for dry cells which enables to prevent generation of a hydrogen gas. In addition, this negative electrode collector for dry cells enables to manufacture an easily mass-producible dry cell having a short cycle time, high dimensional accuracy and stable quality at a lower production cost. Specifically disclosed is a negative electrode collector for dry cells which is obtained by plating, preferably electrolytic plating the surface of an iron wire rod which is formed into a desired shape by forging.

Description

明 細 書  Specification
乾電池用負極集電体  Negative electrode current collector for dry cell
技術分野  Technical field
[0001] 本発明は乾電池用負極集電体に関し、より詳しくは、アルカリ乾電池やニッケル乾 電池の軸心部分に組み込まれる負極集電体に関する。  The present invention relates to a negative electrode current collector for a dry cell, and more particularly, to a negative electrode current collector incorporated in an axial center portion of an alkaline dry cell or a nickel dry cell.
背景技術  Background art
[0002] 一般に、アルカリ乾電池の軸心部分に配置される負極集電体は、黄銅等からなる 線材を所定径寸法の線引きダイスの内径に挿通して引き抜く伸線加工を経て形成さ れている。  Generally, the negative electrode current collector disposed at the axial center portion of the alkaline dry battery is formed through a wire drawing process in which a wire made of brass or the like is inserted through the inside diameter of a wire drawing die of a predetermined diameter and drawn. .
しかしながら、この伸線力卩ェの際に、ダイスを構成する金属(Fe, Ni, Cr, Mo, W, V, As等)やこれらの酸化物からなる微細片が集電体の表面に食!、込んで固着して しまうことがあり、このように集電体に固着した金属微細片は、ゲル状負極中の亜鉛と 反応することによって水素ガスを発生し、電池の内圧を上昇させて液漏れを引き起こ してしまう。  However, during this drawing force, the metal (Fe, Ni, Cr, Mo, W, V, As, etc.) constituting the die and the fine pieces made of these oxides are corroded on the surface of the current collector. In some cases, metal fine pieces that are fixed to the current collector in this way react with the zinc in the gelled negative electrode to generate hydrogen gas and raise the internal pressure of the battery. It will cause fluid leakage.
[0003] 上述のような問題点に鑑みて、従来よりアルカリ乾電池の負極集電体において水 素ガスの発生を防ぐ為の種々の技術が提案されており、一例としては、下記特許文 献 1及び 2の開示技術が挙げられる。  [0003] In view of the above problems, various techniques for preventing the generation of hydrogen gas in the negative electrode current collector of the alkaline dry battery have been conventionally proposed, and one example is disclosed in the following patent document 1 And 2 disclosed technologies.
特許文献 1の開示技術は、黄銅力 なる線材の表面を研磨により機械的に皮むき することによって、集電体の表面に食 、込んだ金属微細片を除去するものである。 特許文献 2の開示技術は、銅又は銅合金力 なる伸線に予め錫の溶融メツキを施 した後、所定形状に切断形成した集電体の表面に更に錫を無電解メツキすることによ り、集電体の表面に食!、込んだ金属微細片を被覆するものである。  According to the technology disclosed in Patent Document 1, the surface of a brass-made wire is mechanically peeled off by polishing to remove metal fine particles that have been corroded and embedded in the surface of a current collector. According to the technology disclosed in Patent Document 2, after copper or copper alloy wire drawing is pre-melted with tin, and then tin is further electrolessly plated on the surface of a current collector cut and formed into a predetermined shape. , The surface of the current collector is covered with a metal fine piece which is embedded.
[0004] これら特許文献 1及び 2の開示技術によれば、集電体の表面に食い込んだ金属微 細片を除去もしくは被覆することができ、水素ガスの発生を防止することが可能となる ものの、これらの開示技術には夫々以下に述べる問題点が存在していた。 According to the techniques disclosed in these Patent Documents 1 and 2, it is possible to remove or coat metal fines biting into the surface of the current collector, and it becomes possible to prevent the generation of hydrogen gas. Each of the disclosed techniques has the following problems.
先ず、特許文献 1の開示技術では、黄銅を材料とするために材料費が高価であり、 し力も機械的皮むきを行うことにより、サイクルタイムが長くなる上に、発生する切屑の 処理のための手間と費用も力かるという問題がある。 First, in the technology disclosed in Patent Document 1, the material cost is high because brass is used as a material, and mechanical force is also used to lengthen the cycle time as well as generate chips. There is a problem that labor and cost for processing are also strong.
また、特許文献 2の開示技術では、予め錫の溶融メツキを施した銅又は銅合金から なる伸線を用いるために高価となり、し力も外径寸法が一定とならず、更に溶融メツキ の後に更に錫を無電解メツキするための手間と費用も力かるという問題がある。  Further, the technology disclosed in Patent Document 2 is expensive because it uses wire drawing made of copper or a copper alloy to which molten plating of tin has been applied in advance, and the force is not uniform in outer diameter size, and further after molten plating. There is a problem that labor and cost for electrolessly plating tin also increase.
[0005] 特許文献 1 :特開平 5— 307961号公報 Patent Document 1: Japanese Patent Application Laid-Open No. 5-307961.
特許文献 2:特開平 7— 29573号公報  Patent Document 2: Japanese Patent Application Laid-Open No. 7-29573
発明の開示  Disclosure of the invention
発明が解決しょうとする課題  Problem that invention tries to solve
[0006] 本発明は、上記従来技術の問題点を解決するためになされたものであって、水素 ガスの発生を防止することが可能であるとともに、製造コストを低く抑えることができ、 サイクルタイムが短くて大量生産が容易であり、し力も高い寸法精度を有し、安定した 品質の乾電池を生産することができる乾電池用負極集電体を提供するものである。 課題を解決するための手段 The present invention has been made to solve the above-mentioned problems of the prior art, and it is possible to prevent the generation of hydrogen gas, and to reduce the manufacturing cost, cycle time It is an object of the present invention to provide a negative electrode current collector for a dry battery, which is short, easy to mass-produce, has high dimensional accuracy, and can produce a stable quality dry battery. Means to solve the problem
[0007] 請求の範囲第 1項に記載の発明は、鍛造加工により所定形状に形成された鉄製の 線材の表面にメツキ処理が施されていることを特徴とする乾電池用負極集電体に関 する。 The invention described in claim 1 relates to a negative electrode current collector for a dry battery, characterized in that the surface of an iron wire rod formed in a predetermined shape by forging is subjected to a plating treatment. Do.
請求の範囲第 2項に記載の発明は、前記メツキ処理が、電解メツキによりなされてい ることを特徴とする請求の範囲第 1項記載の乾電池用負極集電体に関する。  The invention according to claim 2 relates to the negative electrode current collector according to claim 1, wherein the plating treatment is performed by electrolytic plating.
請求の範囲第 3項に記載の発明は、前記メツキが、亜鉛メツキであることを特徴とす る請求の範囲第 1項又は第 2項記載の乾電池用負極集電体に関する。  The invention according to claim 3 relates to the negative electrode current collector for a dry battery according to claim 1 or 2, wherein the metal is zinc.
請求の範囲第 4項に記載の発明は、前記メツキ処理の後に不導態化処理が施され 、更に封孔処理が施されていることを特徴とする請求の範囲第 1項乃至第 3項いずれ かに記載の乾電池用負極集電体に関する。  The invention according to claim 4 is characterized in that a passivation treatment is carried out after the plating treatment, and a sealing treatment is further carried out. The present invention relates to any one of the negative electrode current collectors for dry batteries.
請求の範囲第 5項に記載の発明は、前記メツキが、内層が銅メツキ、外層が錫メツキ の二層構造とされていることを特徴とする請求の範囲第 1項又は第 2項記載の乾電池 用負極集電体に関する。  The invention according to claim 5 is characterized in that the metal layer has a two-layer structure in which the inner layer is made of copper and the outer layer is made of tin. The present invention relates to a negative electrode current collector for a dry cell.
請求の範囲第 6項に記載の発明は、前記メツキ処理の後にリフロー処理がなされて いることを特徴とする請求の範囲第 1項、第 2項、又は第 5項記載の乾電池用負極集 電体に関する。 The invention according to claim 6 is that the negative electrode collection for a dry battery according to claim 1, wherein a reflow process is performed after the plating process. It relates to a collector.
請求の範囲第 7項に記載の発明は、前記鉄が、 0. 03重量%以下の炭素と残部の 鉄及び不可避不純物からなることを特徴とする請求の範囲第 1項乃至第 6項いずれ かに記載の乾電池用負極集電体に関する。  The invention according to claim 7 is characterized in that the iron comprises not more than 0.30% by weight of carbon, the balance of iron and inevitable impurities. The present invention relates to a negative electrode current collector for a dry cell described in 1.
発明の効果  Effect of the invention
[0008] 請求の範囲第 1項に記載の発明によれば、鉄の線材力 形成されているため、銅 や銅合金に比べて、材料費が安価に抑えられるとともに、高強度であるために、輸送 時、メツキ処理時、電池への組み込み時等において曲がりにくぐ安定した高品質の 乾電池が得られる。  [0008] According to the invention described in claim 1, since the wire force of iron is formed, the material cost can be suppressed at low cost and high strength as compared to copper and copper alloy. A stable, high quality dry battery is obtained that can be bent at the time of transportation, at the time of label processing, at the time of incorporation into a battery, etc.
また、表面にメツキが施されていることで、集電体の素材表面並びに表面に食い込 んだ金属微細片がメツキにより被覆されて、乾電池に組み込んだ時に水素ガスの発 生を防止することが可能となる。  In addition, the surface of the material of the current collector and the metal fine pieces that bite into the surface of the current collector are covered with metal plating to prevent generation of hydrogen gas when incorporated into a dry battery. Is possible.
更に、鍛造加工のみにより所定形状に形成されることで、加工のサイクルタイムが短 縮され、しかも切屑が発生しないために、製造の手間と費用が抑えられ、大量生産が 可能となる。  Furthermore, by forming into a predetermined shape only by forging, the processing cycle time is shortened and chips are not generated, so that the labor and cost of manufacturing can be suppressed, and mass production can be performed.
[0009] 請求の範囲第 2項に記載の発明によれば、メツキ処理が電解メツキによりなされてい るため、安定した均一な膜厚のメツキが形成され、高い寸法精度の集電体を得ること ができる。  According to the invention described in the second aspect, since the plating process is performed by electrolytic plating, a stable and uniform film thickness of the film can be formed, and a current collector with high dimensional accuracy can be obtained. Can.
また、銅や銅合金に比べて電解メツキが容易な鉄を材料とするため、メツキが容易 に付着し、メツキに要する時間が少なくて済む。そのため、メツキ費用のコストが低減 されて大量生産が容易となり、し力も素地の露出が起こらないために、乾電池に組み 込んだ時に水素ガスの発生が生じな!/、。  In addition, since iron is used as the material of which electrolytic plating is easier than copper and copper alloys, the adhesion is easy and the time required for the adhesion can be reduced. Therefore, the cost of the plastic cost is reduced, mass production becomes easy, and no exposure of the substrate occurs, so no hydrogen gas is generated when incorporated into the dry cell! /.
[0010] 請求の範囲第 3項に記載の発明によれば、メツキが亜鉛メツキであることにより、負 極集電体を乾電池に組み込んで使用した場合にメツキが損傷を受け難い。  [0010] According to the invention described in claim 3, when the negative electrode current collector is used by being incorporated into a dry cell, the resin is less likely to be damaged because the metal is zinc.
[0011] 請求の範囲第 4項に記載の発明によれば、メツキ処理の後に不導態化処理が施さ れることにより、負極集電体表面に酸化被膜が形成され、耐食性が向上する。そのた め、乾電池に組み込んで使用した場合に水素ガスの発生を防止する効果が高まる。 また、封孔処理が施されていることにより、負極集電体がより一層不活性化 (耐酸ィ匕 性、耐食性の向上)し、乾電池に組み込んで使用した場合の水素ガスの発生を防止 する効果が一層高まり、更に、表面が平滑化されるため、乾電池に組み込む際のパ ッキンの損傷を防ぐことができる。 According to the invention described in the fourth aspect, the passivation treatment is carried out after the matting treatment, whereby an oxide film is formed on the surface of the negative electrode current collector, and the corrosion resistance is improved. Therefore, when incorporated into a dry cell and used, the effect of preventing the generation of hydrogen gas is enhanced. In addition, the negative electrode current collector is further inactivated due to the pore-sealing treatment. And corrosion resistance), and the effect of preventing the generation of hydrogen gas when used by incorporating it into a dry battery is further enhanced, and furthermore, the surface is smoothed to prevent damage to the packing when incorporated into the dry battery. Can.
[0012] 請求の範囲第 5項に記載の発明によれば、内層が銅メツキ、外層が錫メツキの二層 構造のメツキが施されているので、仮に外層のメツキ被膜にピンホール等の欠陥があ つても、内層の銅メツキ被膜により鉄素材の露出が防がれ、水素ガスの発生をより確 実に防止することが可能となる。  According to the invention described in claim 5, since the inner layer is coated with copper and the outer layer is coated with a double layer of tin plating, defects such as pinholes may be temporarily formed on the outer surface of the outer layer. Even so, the copper plating film on the inner layer prevents the iron material from being exposed, making it possible to more reliably prevent the generation of hydrogen gas.
[0013] 請求の範囲第 6項に記載の発明によれば、メツキ処理の後にリフロー処理がなされ ているため、仮にメツキ被膜にピンホール等の欠陥があってもその欠陥が修復され、 同時にメツキ表面が硬化されるため、特に運搬時や電池への組み込み時において、 集電体同士や他の部材と接触しても傷がつきにくぐ更に錫メツキ表面に発生する白 色化腐蝕が抑えられる。  According to the invention described in claim 6, since the reflow process is performed after the matting process, even if there is a defect such as a pinhole in the matting film, the defect is repaired, and at the same time, the mecking is repeated. Since the surface is cured, damage to the collectors and contact with other members can be suppressed even during transportation or assembly into a battery, and whitening corrosion generated on the tin plating surface can be suppressed. .
[0014] 請求の範囲第 7項に記載の発明によれば、 0. 03重量%以下の炭素と残部の鉄及 び不可避不純物からなる鉄を使用して 、るため、メツキ被膜が短時間で均一に形成 され、製造コストの低減と品質の向上を達成することができる。  [0014] According to the invention described in claim 7, the iron film comprising less than 0.30% by weight of carbon and the balance iron and the unavoidable impurities is used, so that the film can be formed in a short time. It can be formed uniformly, achieving reduced manufacturing costs and improved quality.
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0015] 以下、本発明に係る乾電池用負極集電体の好適な実施形態について、図面を参 照しつつ説明する。 Hereinafter, a preferred embodiment of the negative electrode current collector for a dry battery according to the present invention will be described with reference to the drawings.
図 1は本発明に係る乾電池用負極集電体の一例を示す正面図である。 本発明に係る負極集電体(1)は、円柱状の軸部(11)と、この軸部(11)の基端近 傍に設けられた軸部よりも大径の円板部(12)と、軸部(11)の先端に設けられた先 細り状の円錐台状部(13)とから構成されている。  FIG. 1 is a front view showing an example of a negative electrode current collector for a dry cell according to the present invention. The negative electrode current collector (1) according to the present invention has a cylindrical shaft (11) and a disk portion (12 having a diameter larger than that of a shaft provided near the proximal end of the shaft (11)). And a tapered conical portion (13) provided at the tip of the shaft portion (11).
[0016] 図 2は本発明に係る負極集電体を組み込んだ乾電池の部分切り欠き断面図である 負極集電体(1)は、図 2に示すように乾電池(2)の軸心部分に配設される。 FIG. 2 is a partially cutaway cross-sectional view of a dry battery incorporating the negative electrode current collector according to the present invention. As shown in FIG. 2, the negative electrode current collector (1) is located at the axial center of the dry battery (2). It is arranged.
すなわち、乾電池(2)は、正極端子を兼ねる有底筒状の金属容器(21)と、この金 属容器 (21)内に収納された所定圧力で加圧成形されて成る中空円筒状の正極材 料(22)と、正極材料(22)の内側にセパレータ(23)を介して充填されたゲル状負極 (24)と、封口キャップ(25)及びガスケット(26)を貫通してゲル状負極(24)に挿入さ れた負極集電体(1)とを備えている。 That is, the dry cell (2) includes a bottomed cylindrical metal container (21) which also serves as a positive electrode terminal, and a hollow cylindrical positive electrode which is pressure-formed at a predetermined pressure housed in the metal container (21). Material (22) and gelled negative electrode filled inside of positive electrode material (22) via separator (23) (24) and a negative electrode current collector (1) inserted into the gelled negative electrode (24) through the sealing cap (25) and the gasket (26).
[0017] 本発明に係る負極集電体が組み込まれる乾電池としては、正極材料の主成分とし て二酸ィ匕マンガンを使用する一般的なアルカリ乾電池の他に、正極材料の主成分と してォキシ水素化ニッケルを使用するニッケル乾電池 (例えば、松下電器産業株式 会社製のォキシライド乾電池 (商品名))が挙げられる。 As a dry battery in which the negative electrode current collector according to the present invention is incorporated, in addition to a general alkaline dry battery using manganese dioxide as a main component of the positive electrode material, as a main component of the positive electrode material. A nickel dry battery using nickel oxyhydride (eg, Oxyride dry battery (trade name) manufactured by Matsushita Electric Industrial Co., Ltd.) can be mentioned.
[0018] 本発明に係る負極集電体(1)は、以下のような工程を経て製造される。 The negative electrode current collector (1) according to the present invention is manufactured through the following steps.
第一工程は、線材にダイスでの引き抜き加工 (伸線加工)を施す工程であり、第二 工程は引き抜きカ卩ェされた線材を所定寸法に切断する工程であり、これらの工程は 具体的には以下のように行われる。  The first step is a step of subjecting the wire to drawing (wire drawing) with a die, and the second step is a step of cutting the drawn wire into a predetermined size, and these steps are specific steps. Is performed as follows.
先ず、線材(1A)を、図 3に示すように送りロール(2A) , (2B)の間に挟み込んで口 ールを回転させることによりダイス (7)の貫通孔(71)に供給し、該貫通孔(71)力 出 てきた線材(1A)の先端をストツバ(8)で受けてカッティングナイフ(9)で所定寸法に 切断する。  First, the wire rod (1A) is fed between the feed rolls (2A) and (2B) as shown in FIG. 3 and supplied to the through hole (71) of the die (7) by rotating the hole. The tip of the wire (1A) coming out of the through hole (71) is received by the stock bar (8), and cut into a predetermined size by the cutting knife (9).
[0019] 本発明において、線材(1A)の素材は鉄とされる。  In the present invention, the material of the wire rod (1A) is iron.
鉄製の線材を使用する理由は、従来のように銅や銅合金を用いた場合と比較して 以下のような利点があるためである。  The reason for using an iron wire rod is because there are the following advantages as compared with the case where copper or a copper alloy is used conventionally.
第一には、銅や銅合金に比べて安価であるために、製造コストを低く抑えられると いうことである。  First, it is less expensive than copper and copper alloys, so the manufacturing cost can be kept low.
第二には、銅や銅合金に比べて高強度であるために、輸送時、メツキ処理時、電池 への組み込み時等において曲がりにくぐ安定した高品質の乾電池が得られるという ことである。  Second, because they have high strength compared to copper and copper alloys, stable, high-quality dry batteries can be obtained which are bent when transported, mated, incorporated in batteries, and the like.
第三には、銅や銅合金に比べて電解メツキが容易であるため、メツキが容易に付着 し、メツキに要する時間が少なくて済み、そのため、メツキ費用のコストが低減されて 大量生産が容易となり、し力も素地の露出が起こらないために、乾電池に組み込んだ 時に水素ガスの発生が生じな 、と 、うことである。  Thirdly, electrolytic plating is easier than copper and copper alloys, so that it is easy to apply and requires less time for plating, which reduces the cost of plating and facilitates mass production. Also, since no exposure of the substrate occurs, no hydrogen gas is generated when it is incorporated into a dry cell.
[0020] 本発明において線材の素材となる鉄としては、 0. 03重量%以下の炭素と残部の鉄 及び不可避不純物からなる鉄を用いることが好ま 、。 その理由は、炭素含有量が 0. 03重量%以下の鉄を用いると、メツキ処理の際にメ ツキ被膜が短時間で均一に形成され、製造コストの低減と品質の向上を達成すること ができるためである。 In the present invention, it is preferable to use iron composed of not more than 0.30% by weight of carbon, the balance of iron and unavoidable impurities, as iron to be a material of the wire rod. The reason is that when iron having a carbon content of not more than 0.30% by weight is used, a coating film can be formed uniformly in a short time during coating treatment, thereby achieving reduction in manufacturing cost and improvement in quality. It is because it can.
[0021] 第三工程は、所定寸法に切断された線材に冷間鍛造 (冷間圧造)加工を施して所 定形状(図 1に示す形状)に成形する工程であり、この工程は具体的には以下のよう に行われる。  The third step is a step of subjecting a wire rod cut to a predetermined size to cold forging (cold forging) to form it into a predetermined shape (shape shown in FIG. 1), and this step is a specific step. Is done as follows.
所定寸法に切断された線材(1A)を、図 4に示すように広径の開口部(31)を有する 第 1のパンチ(3)でダイス (4)内に押し込んで、ダイス (4)内に設けられた先細り部 (4 1)により先端に絞り加工を施して円錐台状部(13)を形成するとともに、その基端部 を第 1のパンチ(3)の広径開口部(31)で拡径する(図 5参照)。  The wire (1A) cut to a predetermined size is pushed into the die (4) with the first punch (3) having the wide diameter opening (31) as shown in FIG. The tapered end (41) provided at the end of the end portion performs a drawing process to form a truncated cone portion (13), and the base end portion thereof is the wide diameter opening (31) of the first punch (3). Expand the diameter with (see Figure 5).
次いで、図 6に示すように、第 1のパンチ(3)に代えて円状凹部(51)を有する第 2 のパンチ(5)を更にダイス (4)側に押し付けて線材 ( 1 A)の基端部に円板部( 12)を 形成し、その後、図 7に示すように、第 2のパンチ(5)を退動させて、線材(1A)をノッ クアウトピン (6)で押し出す。  Then, as shown in FIG. 6, instead of the first punch (3), the second punch (5) having a circular recess (51) is further pressed to the die (4) side to make the wire rod (1A) A disc (12) is formed at the base end, and then, as shown in FIG. 7, the second punch (5) is retracted and the wire (1A) is pushed out with the knock out pin (6).
[0022] 尚、図 3乃至図 7において、(10)は金型本体であり、(6A)はノックアウトピンが取り つけられたノックアウトロッドであって、ノックアウトロッド(6A)を押し出し方向に移動さ せる移動手段の図示は省略されている。  In FIGS. 3 to 7, (10) is a mold main body, (6A) is a knockout rod attached with a knockout pin, and the knockout rod (6A) is moved in the pushing direction. The illustration of the moving means for causing the movement is omitted.
[0023] 上記した如ぐ本発明の負極集電体は、鍛造加工のみにより所定形状に形成され るために、加工のサイクルタイムが短くなり、し力も切屑が発生しないために、製造の 手間と費用が抑えられ、大量生産が可能となる。  Since the negative electrode current collector of the present invention as described above is formed into a predetermined shape only by forging, the processing cycle time becomes short, and no cutting force is generated. Cost is reduced and mass production is possible.
[0024] 第四工程は、鍛造加工により所定形状に形成された鉄製線材の表面にメツキ処理 を施す工程である。  The fourth step is a step of subjecting the surface of the iron wire rod, which has been formed into a predetermined shape by forging processing, to a tacking treatment.
メツキ処理としては亜鉛メツキ又は錫メツキが行われる。これは、亜鉛及び錫は水素 過電圧が高!、ために、水素ガスの発生を抑制するのに適して!/、るためである。  Zinc plating or tin plating is performed as the plating treatment. This is because zinc and tin have high hydrogen overvoltage !, and are suitable for suppressing the generation of hydrogen gas!
亜鉛メツキは電解メツキにより行われる力 錫メツキは電解メツキによるものでも無電 解メツキによるものもよい。但し、本発明では電解メツキによることが好ましい。  Zinc plating is performed by electrolytic plating. Tin plating may be electrolytic plating or nonelectrolytic plating. However, in the present invention, electrolytic plating is preferred.
その理由は、電解メツキとすること〖こより、安定した均一な膜厚のメツキが形成され、 高い寸法精度の負極集電体を得ることができるためである。 亜鉛メツキ又は錫メツキの厚みは 2〜5 μ mとされる。 The reason is that, since electrolytic plating is performed, a stable and uniform film thickness is formed, and a negative electrode current collector with high dimensional accuracy can be obtained. The thickness of zinc plating or tin plating is 2 to 5 μm.
[0025] 本発明に係る負極集電体では、上述した如く鉄製線材の表面にメツキが施されるた め、集電体の素材表面自体並びに表面に食い込んだダイスを構成する金属 (Fe, N i, Cr, Mo, W, V, As等)やこれらの酸ィ匕物からなる金属微細片カ^ッキにより被覆 されて、乾電池に組み込んだ時に水素ガスの発生を防止することが可能となる。 In the negative electrode current collector according to the present invention, since the surface of the iron wire is coated as described above, the material surface of the current collector itself and the metal constituting the die cut into the surface (Fe, N i, Cr, Mo, W, V, As, etc.) and metal fine pieces made of these acid oxides, which can be coated to prevent generation of hydrogen gas when incorporated into a dry cell. Become.
[0026] 第四工程におけるメツキ処理として錫メツキを行う場合、錫メツキのみとしてもよいが 、鉄製線材の表面に対して、銅メツキを施した後に錫メツキを施すことにより、内層が 銅メツキ、外層が錫メツキの二層構造のメツキを形成することが好ましい。 When tin plating is performed as the matting treatment in the fourth step, only tin plating may be performed, but by applying copper plating to the surface of the iron wire rod and then applying tin plating, the inner layer becomes copper plating, It is preferred that the outer layer form a tin-meat two-layer structure.
この場合における各層のメツキ厚は、例えば、内層の銅メツキの厚みが 1〜2 /ζ πι、 外層の錫メツキの厚みが 2〜5 μ mとされる。  The thickness of each layer in this case is, for example, 1 to 2 / ζπι for the copper layer in the inner layer, and 2 to 5 μm for the tin layer in the outer layer.
このような二層構造のメツキを形成することによって、仮に外層の錫メツキ被膜にピ ンホール等の欠陥があっても、内層の銅メツキ被膜により鉄素材の露出が防がれ、水 素ガスの発生をより一層確実に防ぐことが可能となる。  By forming such a two-layered structure, even if there is a pinhole or other defect in the outer layer tin plating film, the copper plating film on the inner layer prevents the iron material from being exposed, and hydrogen gas can be used. It becomes possible to prevent occurrence more reliably.
[0027] 本発明に係る負極集電体は、上記第四工程で亜鉛メツキ処理が行われた場合、そ の後に第五工程として不導態化処理が施される。  When the zinc plating treatment is performed in the fourth step, the anode current collector according to the present invention is subjected to a passivation treatment as a fifth step.
不導態化処理は、メツキ後の負極集電体の表面をエッチング処理して活性化させ た後、硝酸等の酸性の溶液に浸漬することにより行われる。  The passivation treatment is performed by etching the surface of the negative electrode current collector after plating to activate it, and then immersing in an acidic solution such as nitric acid.
これにより、負極集電体の表面に酸ィ匕被膜が生成されるため、乾電池に組み込ん で使用した場合に水素ガスの発生を防止することができる。  As a result, since an oxide coating is formed on the surface of the negative electrode current collector, generation of hydrogen gas can be prevented when incorporated into a dry battery.
[0028] 不導態化処理が施された後、第六工程として封孔処理が施される。 After the passivation treatment, sealing treatment is applied as a sixth step.
封孔処理は、不導態化処理が施された負極集電体を、界面活性剤を含む溶液に 浸漬することにより行われる。  The pore-sealing treatment is performed by immersing the passivation-treated negative electrode current collector in a solution containing a surfactant.
これにより、負極集電体がより一層不活性化 (酸ィ匕しにくくなり、耐食性が向上する) し、乾電池に組み込んで使用した場合に水素ガスの発生を防止する効果を一層高 めることができる。更に、表面が平滑ィ匕されるため、乾電池に組み込む際のパッキン の損傷が防がれるという効果も得られる。  As a result, the negative electrode current collector is further inactivated (it becomes difficult to be oxidized and the corrosion resistance is improved), and the effect of preventing the generation of hydrogen gas is further enhanced when incorporated into a dry battery. Can. Furthermore, since the surface is smoothed, the effect of preventing damage to the packing when being incorporated into the dry battery is also obtained.
[0029] 本発明に係る負極集電体は、上記第四工程で錫メツキ処理が行われた場合、その 後に第五工程として、所定形状に成形されてメツキ処理が施された線材をリフロー処 理する工程が付加される。 [0029] In the negative electrode current collector according to the present invention, when the tin plating treatment is performed in the fourth step, a wire that has been molded into a predetermined shape and has been subjected to the plating treatment is reflowed in a fifth step. Process is added.
リフロー処理の条件は、例えば、加熱温度 220〜260°C (好ましくは約 250°C)、加 熱時間 5〜 15秒 (好ましくは約 10秒)とされる。  The conditions for the reflow process are, for example, a heating temperature of 220 to 260 ° C. (preferably about 250 ° C.) and a heating time of 5 to 15 seconds (preferably about 10 seconds).
[0030] このように錫メツキ処理の後にリフロー処理がなされることにより、仮に錫メツキ被膜 にピンホール等の欠陥があってもその欠陥が修復され、同時に錫メツキ表面が硬化 される。 As described above, by performing the reflow process after the tin plating process, even if there is a defect such as a pinhole in the tin plating film, the defect is repaired, and at the same time, the tin plating surface is cured.
そのため、特に運搬時や電池への組み込み時において、集電体同士や他の部材 と接触しても傷がつきに《なる。また、錫メツキ表面に発生する白色化腐蝕が抑えら れるという効果も得られる。  As a result, particularly during transportation or assembly into a battery, even if the current collectors come in contact with each other or with other members, they may be damaged. In addition, the effect of suppressing the whitening corrosion generated on the tin-plated surface is also obtained.
[0031] 以上説明した第一工程力 第六工程 (亜鉛メツキの場合)もしくは第一工程力 第 五工程 (錫メツキの場合)を経ることによって、本発明に係る乾電池用負極集電体の 製造が完了し、このように製造された負極集電体は、上述したようにアルカリ乾電池 やニッケル乾電池の軸心部分に組み込まれて使用される。 産業上の利用可能性 [0031] The production of the negative electrode current collector for a dry battery according to the present invention through the above-described first process power sixth process (for zinc coating) or first process power fifth process (for tin plating). As described above, the negative electrode current collector thus manufactured is used by being incorporated into the core portion of an alkaline dry battery or a nickel dry battery as described above. Industrial applicability
[0032] 本発明は、アルカリ乾電池やニッケル乾電池に組み込まれる負極集電体として利 用することができる。 The present invention can be used as a negative electrode current collector incorporated in an alkaline dry battery or a nickel dry battery.
図面の簡単な説明  Brief description of the drawings
[0033] [図 1]本発明に係る乾電池用負極集電体の一例を示す正面図である。 FIG. 1 is a front view showing an example of a negative electrode current collector for a dry cell according to the present invention.
[図 2]本発明に係る乾電池用負極集電体を組み込んだ乾電池の部分切り欠き断面 図である。  FIG. 2 is a partially cutaway sectional view of a dry battery incorporating the negative electrode current collector for a dry battery according to the present invention.
[図 3]本発明に係る乾電池用負極集電体の製造工程の第一工程及び第二工程を示 す図である。  FIG. 3 is a view showing a first step and a second step of a manufacturing process of a negative electrode current collector for a dry battery according to the present invention.
[図 4]本発明に係る乾電池用負極集電体の製造工程の第三工程を示す図である。  FIG. 4 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
[図 5]本発明に係る乾電池用負極集電体の製造工程の第三工程を示す図である。  FIG. 5 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
[図 6]本発明に係る乾電池用負極集電体の製造工程の第三工程を示す図である。  FIG. 6 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention.
[図 7]本発明に係る乾電池用負極集電体の製造工程の第三工程を示す図である。 符号の説明  FIG. 7 is a view showing a third step of the process for producing a negative electrode current collector for a dry battery according to the present invention. Explanation of sign
[0034] 1 乾電池用負極集電体 線材 1 Negative electrode current collector for dry cell wire

Claims

請求の範囲 The scope of the claims
[1] 鍛造加工により所定形状に形成された鉄製の線材の表面にメツキ処理が施されて [1] The surface of an iron wire rod formed in a predetermined shape by forging is subjected to a tacking treatment
Vヽることを特徴とする乾電池用負極集電体。 A negative electrode current collector for a dry cell, characterized in that it contains V.
[2] 前記メツキ処理が、電解メツキによりなされていることを特徴とする請求の範囲第 1項 記載の乾電池用負極集電体。 [2] The negative electrode current collector for a dry battery according to claim 1, wherein the plating treatment is performed by electrolytic plating.
[3] 前記メツキが、亜鉛メツキであることを特徴とする請求の範囲第 1項又は第 2項記載 の乾電池用負極集電体。 [3] The negative electrode current collector for a dry battery according to any one of claims 1 and 2, wherein the metal is zinc.
[4] 前記メツキ処理の後に不導態化処理が施され、更に封孔処理が施されていることを 特徴とする請求の範囲第 1項乃至第 3項いずれかに記載の乾電池用負極集電体。 [4] The negative electrode collection for a dry cell according to any one of claims 1 to 3, characterized in that a passivation treatment is applied after the plating treatment, and a sealing treatment is further applied. Collector.
[5] 前記メツキが、内層が銅メツキ、外層が錫メツキの二層構造とされていることを特徴と する請求の範囲第 1項又は第 2項記載の乾電池用負極集電体。 [5] The negative electrode current collector for a dry battery according to claim 1 or 2, wherein the metallized layer has a two-layered structure of an inner layer made of copper and an outer layer made of tin.
[6] 前記メツキ処理の後にリフロー処理がなされていることを特徴とする請求の範囲第 1 項、第 2項、又は第 5項記載の乾電池用負極集電体。 [6] The negative electrode current collector for a dry battery according to claim 1, wherein a reflow process is performed after the plating process.
[7] 前記鉄が、 0. 03重量%以下の炭素と残部の鉄及び不可避不純物力 なることを 特徴とする請求の範囲第 1項乃至第 6項いずれかに記載の乾電池用負極集電体。 [7] The negative electrode current collector for a dry battery according to any one of claims 1 to 6, characterized in that the iron comprises carbon in an amount of not more than 0.30% by weight, iron of the balance and unavoidable impurity power. .
PCT/JP2006/304274 2005-03-07 2006-03-06 Negative electrode collector for dry cell WO2006095683A1 (en)

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Application Number Priority Date Filing Date Title
JP2005-062772 2005-03-07
JP2005062772 2005-03-07

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61133568A (en) * 1984-12-04 1986-06-20 Fuji Elelctrochem Co Ltd Cylindrical alkaline battery
JPS6337568A (en) * 1986-07-31 1988-02-18 Arukari Kandenchi Gijutsu Kenkyu Kumiai Alkaline cell
JPH05135776A (en) * 1991-11-13 1993-06-01 Hitachi Maxell Ltd Cylindrical alkaline battery
JPH05182658A (en) * 1991-12-28 1993-07-23 Sanyo Electric Co Ltd Manufacture of negative electrode collector for zinc alkaline battery
JPH05283080A (en) * 1992-03-31 1993-10-29 Fukui Byora Kk Collecting bar for alkaline dry battery and manufacture thereof
JP2001085018A (en) * 1999-09-10 2001-03-30 Fukui Byora Co Ltd Negative electrode current collector of alkaline dry battery

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61133568A (en) * 1984-12-04 1986-06-20 Fuji Elelctrochem Co Ltd Cylindrical alkaline battery
JPS6337568A (en) * 1986-07-31 1988-02-18 Arukari Kandenchi Gijutsu Kenkyu Kumiai Alkaline cell
JPH05135776A (en) * 1991-11-13 1993-06-01 Hitachi Maxell Ltd Cylindrical alkaline battery
JPH05182658A (en) * 1991-12-28 1993-07-23 Sanyo Electric Co Ltd Manufacture of negative electrode collector for zinc alkaline battery
JPH05283080A (en) * 1992-03-31 1993-10-29 Fukui Byora Kk Collecting bar for alkaline dry battery and manufacture thereof
JP2001085018A (en) * 1999-09-10 2001-03-30 Fukui Byora Co Ltd Negative electrode current collector of alkaline dry battery

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