JP2003017044A - Method of manufacturing positive electrode for alkali battery - Google Patents
Method of manufacturing positive electrode for alkali batteryInfo
- Publication number
- JP2003017044A JP2003017044A JP2001199758A JP2001199758A JP2003017044A JP 2003017044 A JP2003017044 A JP 2003017044A JP 2001199758 A JP2001199758 A JP 2001199758A JP 2001199758 A JP2001199758 A JP 2001199758A JP 2003017044 A JP2003017044 A JP 2003017044A
- Authority
- JP
- Japan
- Prior art keywords
- positive electrode
- cobalt
- mass
- battery
- mixture
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
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- Y02E60/12—
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、アルカリ電池用正
極の製造方法に係り、さらに詳しくは高品質化したアル
カリ電池用正極の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a positive electrode for an alkaline battery, and more particularly to a method for producing a high quality positive electrode for an alkaline battery.
【0002】[0002]
【従来の技術】たとえば携帯形のラジオやカセットレコ
ーダーなどの携帯形電子機器類の電源として、亜鉛アル
カリ電池などが使用されている。そして、この種のアル
カリ電池は、電池要素(起電部)をインサイドアウト形
構造とした構成、あるいは電池要素(起電部)を積層板
化した構成がある。なお、電池要素をインサイドアウト
形構造とした場合は、低コストを図ることも知られてい
る。2. Description of the Related Art For example, zinc alkaline batteries are used as a power source for portable electronic devices such as portable radios and cassette recorders. In addition, this type of alkaline battery has a configuration in which the battery element (electromotive portion) has an inside-out structure or a configuration in which the battery element (electromotive portion) is a laminated plate. It is also known that the cost can be reduced when the battery element has an inside-out type structure.
【0003】すなわち、一般的には、正極活物質である
水酸化ニッケル系粒子及び導電剤を含む正極合剤製の中
空筒状の成形体を正極とし、その正極中空内に有底筒状
のセパレータを介挿・配置し、この有底筒状セパレータ
内に亜鉛を主成分とするゲル状の負極物質を充填するイ
ンサイドアウト形構造を採っている。そして、インサイ
ドアウト形構造を採ることにより、シート状の正極、セ
パレータおよび負極の積層体を捲回するスパイラル形構
造を採る場合に較べて、生産性の向上などが図られ、結
果的に、低コストで高容量の亜鉛アルカリ電池を提供で
きる。That is, generally, a hollow cylindrical molded body made of a positive electrode mixture containing nickel hydroxide-based particles as a positive electrode active material and a conductive agent is used as a positive electrode, and a hollow cylinder having a bottom is formed in the hollow of the positive electrode. An inside-out type structure is adopted in which a separator is inserted and arranged, and a gelled negative electrode material containing zinc as a main component is filled in the bottomed tubular separator. Further, by adopting the inside-out type structure, productivity is improved compared to the case where a spiral type structure in which a laminate of a sheet-shaped positive electrode, a separator and a negative electrode is wound is adopted. It is possible to provide a high-capacity zinc alkaline battery at low cost.
【0004】ところで、この種のアルカリ電池用正極
は、一般的に、次のような手順で製造されている。すな
わち、平均粒径5〜15μmの水酸化ニッケル系粒子
(正極活物質)90質量部当たり、たとえば黒鉛粉末な
どの導電剤5〜10質量部、たとえば苛性カリ30〜4
5質量%水溶液からなるアルカリ電解液2〜5質量部、
及びCMC(カルボキシメチルセルロース)などのバイ
ンダー0.01〜 1質量部の混合成分を撹拌・混合
する。こうして得た正極合剤混合物(組成物)を加圧成
形して、所要の正極、たとえば円筒状の正極ペレットを
作製している。なお、正極活物質として、コバルト化合
物層を表面に設けて導電性を付与した水酸化ニッケル系
粒子を使用することもある。By the way, this type of positive electrode for an alkaline battery is generally manufactured by the following procedure. That is, for 90 parts by mass of nickel hydroxide particles (positive electrode active material) having an average particle size of 5 to 15 μm, for example, 5 to 10 parts by mass of a conductive agent such as graphite powder, for example, 30 to 4 caustic potash.
2 to 5 parts by mass of an alkaline electrolyte composed of a 5% by mass aqueous solution,
And 0.01 to 1 part by mass of a binder such as CMC (carboxymethyl cellulose) are mixed by stirring. The positive electrode mixture mixture (composition) thus obtained is pressure-molded to produce a desired positive electrode, for example, a cylindrical positive electrode pellet. As the positive electrode active material, nickel hydroxide-based particles provided with a cobalt compound layer on the surface to impart conductivity may be used.
【0005】[0005]
【発明が解決しようとする課題】上記のように、電池要
素がスパイラル形構造を採る場合に較べて、電池要素が
インサイドアウト形構造を採った場合は、アルカリ電池
の生産性や低コスト化の点で有利である。しかし、イン
サイドアウト形構造は、スパイラル形構造の場合に較べ
て正極と負極との対向面積が小さく、また、電池内容積
も決まっているため、大幅な電池容量アップが難しいと
いう問題がある。As described above, when the battery element has the inside-out structure, the productivity and cost of the alkaline battery can be reduced as compared with the case where the battery element has the spiral structure. It is advantageous in terms. However, the inside-out structure has a problem that it is difficult to significantly increase the battery capacity because the facing area between the positive electrode and the negative electrode is smaller than that of the spiral structure and the internal volume of the battery is fixed.
【0006】上記アルカリ電池の高容量化手段として、
前記正極の製造工程において、正極活物質比を極端に高
めると、正極合剤の均一な成分系形成が困難となり、結
果的に、正極容量のバラツキなどを招来する恐れが増
え、正極の量産性や歩留まり性、あるいは製造・製作し
た電池の信頼性が損なわれる。また、正極合剤中の正極
活物質比のアップは、一方で、正極活物質の利用率低下
となり、重負荷放電特性などの劣化を招来する。As a means for increasing the capacity of the alkaline battery,
In the manufacturing process of the positive electrode, if the ratio of the positive electrode active material is extremely increased, it becomes difficult to form a uniform component system of the positive electrode mixture, and as a result, there is a risk of causing variations in the positive electrode capacity and the mass productivity of the positive electrode. And yield, or the reliability of the manufactured / manufactured battery is impaired. On the other hand, an increase in the ratio of the positive electrode active material in the positive electrode mixture, on the other hand, results in a lower utilization rate of the positive electrode active material, leading to deterioration in heavy load discharge characteristics and the like.
【0007】なお、アルカリ電池の主用途は、通常、重
負荷放電の態様を採っているが、アルカリ電池を電源と
する電子機器類において、その使用態様の選択によっ
て、駆動負荷を低減し、中負荷放電の使用態様を採る場
合がある。こうした駆動負荷の低減を行うとき、問題を
起こさずに中負荷放電が行えれば、省エネルギーないし
省資源の上で有利と言える。つまり、優れた重負荷放電
特性を有し、かつ活物質を増加などさせることなく、中
負荷放電特性の優れたアルカリ電池が出現すれば、汎用
性の高い携帯形電源の提供となる。The main use of alkaline batteries is usually in the form of heavy load discharge, but in electronic devices using alkaline batteries as a power source, the driving load can be reduced by selecting the mode of use. A usage mode of load discharge may be adopted. It can be said that it is advantageous in terms of energy saving and resource saving if medium load discharge can be performed without causing a problem when such a driving load is reduced. That is, if an alkaline battery that has excellent heavy load discharge characteristics and excellent medium load discharge characteristics without increasing the active material appears, a highly versatile portable power supply can be provided.
【0008】本発明は、上記事情に対処してなされたも
ので、高率放電特性に優れたアルカリ電池の構成に適す
るアルカリ電池用正極の製造方法の提供を目的とする。The present invention has been made in view of the above circumstances, and an object thereof is to provide a method for producing a positive electrode for an alkaline battery, which is suitable for the structure of an alkaline battery having an excellent high rate discharge characteristic.
【0009】[0009]
【課題を解決するための手段】請求項1の発明は、コバ
ルト化合物層を表面に設けた水酸化ニッケル系粒子、ア
ルカリ電解液、及びバインダーを含む正極組成成分を撹
拌・混合する工程と、前記撹拌・混合した組成物に圧縮
破砕処理を施して得た粒子を分級し顆粒状混合成分を得
る工程と、前記顆粒混合成分を成形する工程とを有する
ことを特徴とするアルカリ電池用正極の製造方法であ
る。According to the invention of claim 1, a step of stirring and mixing positive electrode composition components containing nickel hydroxide particles having a cobalt compound layer on the surface thereof, an alkaline electrolyte, and a binder, Manufacture of a positive electrode for an alkaline battery, which comprises a step of classifying particles obtained by subjecting a stirred and mixed composition to compression crushing treatment to obtain a granular mixed component, and a step of molding the granular mixed component Is the way.
【0010】請求項2の発明は、請求項1記載のアルカ
リ電池用正極の製造方法において、混合組成分が炭素系
の導電剤を含有していることを特徴とする。The invention of claim 2 is characterized in that, in the method for producing a positive electrode for an alkaline battery according to claim 1, the mixed composition contains a carbon-based conductive agent.
【0011】請求項3の発明は、請求項1もしくは請求
項2記載のアルカリ電池用正極の製造方法において、顆
粒状正極合剤の粒度分布が14〜60メッシュであるこ
とを特徴とする。A third aspect of the present invention is the method for producing a positive electrode for an alkaline battery according to the first or second aspect, characterized in that the particle size distribution of the granular positive electrode mixture is 14 to 60 mesh.
【0012】請求項4の発明は、請求項1ないし請求項
3いずれか一記載のアルカリ電池用正極の製造方法にお
いて、コバルト化合物層がオキシ水酸化コバルト、三酸
化二コバルト、一酸化コバルト、水酸化コバルト及び金
属コバルトの少なくとも1種で形成されていることを特
徴とする。According to a fourth aspect of the present invention, in the method for producing the positive electrode for an alkaline battery according to any one of the first to third aspects, the cobalt compound layer has cobalt oxyhydroxide, dicobalt trioxide, cobalt monoxide and water. It is characterized by being formed of at least one of cobalt oxide and metallic cobalt.
【0013】請求項1ないし4の発明は、次のよう知見
に基づいてなされたものである。すなわち、本発明者
は、アルカリ電池用の正極組成成分を撹拌・混合して成
形体化するに当たり、撹拌・混合・調製した組成物に圧
縮・破砕処理を施し、得た粒子を分級した後顆粒化し
て、この顆粒化した組成成分を素材として成形すると、
正極の製造操作が容易化し生産性が向上する一方、充填
率及び強度がアップして高容量化や負荷放電特性の向上
・改善された正極が容易に得られることを見出した。つ
まり、アルカリ電池用の正極の製造において、圧縮・破
砕処理、分級・顆粒化、及びこの顆粒体の成形が、正極
の特性、さらには電池の特性向上に大きく作用すること
を確認し、本発明に至ったものである。The inventions of claims 1 to 4 are based on the following knowledge. That is, the present inventor, when stirring and mixing positive electrode composition components for alkaline batteries to form a molded body, the composition prepared by stirring, mixing, and subjecting to compression and crushing, and classifying the obtained particles, granules are obtained. When this is granulated and molded with this granulated composition component as a material,
It has been found that the manufacturing operation of the positive electrode is facilitated and the productivity is improved, while the filling rate and strength are increased to easily obtain a positive electrode having a high capacity and improved / improved load discharge characteristics. That is, it was confirmed that, in the production of a positive electrode for an alkaline battery, compression / crushing treatment, classification / granulation, and molding of this granule greatly affect the characteristics of the positive electrode and further the characteristics of the battery. It came to.
【0014】請求項1ないし4の発明において、正極合
剤の主体を成す水酸化ニッケル系は、たとえば水酸化ニ
ッケル、オキシ水酸化ニッケル、水酸化ニッケル−オキ
シ水酸化ニッケル混合系(混成系)、あるいはこれらと
亜鉛やコバルトとの共晶体である。そして、これら水酸
化ニッケル系粒子としては、一般的に、平均粒径5〜1
5μm程度のものが使用される。In the first to fourth aspects of the present invention, the nickel hydroxide-based material that mainly constitutes the positive electrode mixture is, for example, nickel hydroxide, nickel oxyhydroxide, or a nickel hydroxide-nickel oxyhydroxide mixed system (mixed system). Alternatively, they are a eutectic of zinc and cobalt. And as these nickel hydroxide type | system | group particles, generally, an average particle diameter is 5 to 1
The one having a thickness of about 5 μm is used.
【0015】請求項1ないし4の発明において、正極活
物質を成す水酸化ニッケル系粒子の表面に設けられたコ
バルト化合物層は、たとえばオキシ水酸化コバルト、三
酸化二コバルト、一酸化コバルト、水酸化コバルト及び
金属コバルトなどから選ばれた少なくとも1種である。
ここで、コバルト化合物層は、全体的に、ほぼ均一な膜
厚で設けられていることが好ましいが、部分的であって
もよい。In the invention of claims 1 to 4, the cobalt compound layer provided on the surface of the nickel hydroxide particles forming the positive electrode active material is, for example, cobalt oxyhydroxide, dicobalt trioxide, cobalt monoxide, or hydroxide. At least one selected from cobalt and metallic cobalt.
Here, the cobalt compound layer is preferably provided with a substantially uniform film thickness as a whole, but it may be provided partially.
【0016】また、要すれば添加配合する導電剤は、た
とえば天然黒鉛、合成黒鉛、ケッチェンブラックやアセ
チレンブラックなどのカーボンブラックの粒子である。
そして、正極合剤中に占める導電剤量は、3〜15質量
%程度、好ましくは5〜12質量%、より好ましくは7
〜10質量%の範囲内で選ばれる。ここで、正極合剤中
に占める導電剤量が、3質量%未満では、十分な集電効
率を得ることが難しく、高率放電特性が低下する傾向が
ある。また、15質量%を超えると、結果的に、正極活
物質量の低減となるため、電池容量の低下を招来する。If necessary, the conductive agent to be added and compounded is, for example, natural graphite, synthetic graphite, carbon black particles such as Ketjen black and acetylene black.
The amount of the conductive agent in the positive electrode mixture is about 3 to 15% by mass, preferably 5 to 12% by mass, more preferably 7% by mass.
It is selected within the range of 10 to 10% by mass. Here, if the amount of the conductive agent in the positive electrode mixture is less than 3% by mass, it is difficult to obtain sufficient current collecting efficiency, and the high rate discharge characteristics tend to deteriorate. On the other hand, if it exceeds 15% by mass, the amount of the positive electrode active material is reduced, resulting in a decrease in battery capacity.
【0017】請求項1ないし4の発明において、アルカ
リ電解液は、たとえば水酸化カリウム、水酸化ナトリウ
ムなどのアルカリ物質を30〜45質量%程度の濃度に
水で溶解して調製したものである。そして、この配合比
は、コバルト化合物層を設けた水酸化ニッケル系粒子9
0質量部当たり、2〜5質量部程度がよい。In the invention of claims 1 to 4, the alkaline electrolyte is prepared by dissolving an alkaline substance such as potassium hydroxide or sodium hydroxide in water to a concentration of about 30 to 45% by mass. The mixing ratio is such that the nickel hydroxide-based particles 9 provided with the cobalt compound layer 9
About 2 to 5 parts by mass is preferable per 0 parts by mass.
【0018】また、バインダーは、たとえばポリビニル
アルコール、ポリアクリル酸塩、CMC、メチルセルロ
ース、アルギン酸などが挙げられ、特に、ポリアクリル
酸塩は、アルカリに対する耐薬品性に優れているため好
ましい。そして、この配合比は、コバルト化合物層を設
けた水酸化ニッケル系粒子90質量部当たり、 0.0
1〜1質量部程度がよい。The binder includes, for example, polyvinyl alcohol, polyacrylic acid salt, CMC, methyl cellulose, alginic acid and the like, and polyacrylic acid salt is particularly preferable because it has excellent chemical resistance against alkali. And this compounding ratio is 0.0 with respect to 90 mass parts of nickel hydroxide type particles provided with the cobalt compound layer.
About 1 to 1 part by mass is preferable.
【0019】請求項1ないし4の発明において、正極合
剤組成分の撹拌・混合は、たとえば万能撹拌ミキサーな
どの汎用混合容器を用いて行われる。この撹拌・混合の
条件は、正極合剤組成分及び組成比の選択によって適宜
選択する。また、前記撹拌・混合後の圧縮・破砕は、た
とえば二段形、三段形あるいは四段形など複数段形ロー
ラーコンパクターなどにより行い、被圧縮物の厚さが1
mm以下になるように圧縮を行う。その後、グラニュレ
ータなどの破砕機によって被圧縮物を破砕する。In the inventions of claims 1 to 4, stirring and mixing of the positive electrode mixture composition is performed using a general-purpose mixing container such as a universal stirring mixer. The stirring and mixing conditions are appropriately selected depending on the selection of the positive electrode mixture composition content and composition ratio. The compression / crushing after the stirring / mixing is performed by a multi-stage roller compactor such as a two-stage type, a three-stage type or a four-stage type, and the thickness of the object to be compressed is 1
The compression is performed so as to be less than or equal to mm. Then, the object to be compressed is crushed by a crusher such as a granulator.
【0020】請求項1ないし4の発明において、圧縮破
砕された正極合剤組成物粒子ないし粉末は、篩い分け手
段などによって選択・採取される。つまり、粒度分布
100〜1800μm、好ましくは150〜1500
μm程度の範囲内で選択・採取される。そして、篩い分
けした正極合剤組成物粒子は、平均粒度分布14〜60
メッシュ(平均粒径250〜1300μm)程度の顆粒
状である。In the invention of claims 1 to 4, the compressed and crushed positive electrode mixture composition particles or powder are selected and collected by a sieving means or the like. That is, the particle size distribution
100 to 1800 μm, preferably 150 to 1500
Selected and sampled within the range of about μm. Then, the sieved positive electrode mixture composition particles have an average particle size distribution of 14 to 60.
It is in the form of granules having a mesh size (average particle size of 250 to 1300 μm).
【0021】ここでの圧縮破砕、及び分級の処理によっ
て、筒状や板状の正極成形においては、充填密度が高
く、機械的な強度も優れた筒状や板状の正極成形体が煩
雑な操作を要せずに、歩留まりよく、また、量産的に製
造できる。なお、成形体の機械的な強度の向上は、筒状
の場合など破損性が大幅に改善され、取扱操作、たとえ
ば電池組立工程などでの不良化もなくなり、歩留まりの
向上が図られる。In the cylindrical or plate-shaped positive electrode molding by the compression crushing and classification processes, the cylindrical or plate-shaped positive electrode molded body having a high packing density and excellent mechanical strength is complicated. It can be manufactured with high yield and in mass production without requiring any operation. In addition, the mechanical strength of the molded body is greatly improved, such as in the case of a tubular shape, the breakage is significantly improved, the handling operation, for example, the defectiveness in the battery assembly process is eliminated, and the yield is improved.
【0022】[0022]
【発明の実施態様】以下、図1を参照して実施例につい
て説明する。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments will be described below with reference to FIG.
【0023】正極の作製Preparation of positive electrode
【0024】高次コバルト層が表面に形成された水酸化
ニッケル粒子90質量部に、黒鉛粉末5.4質量部及び
バインダー0.1質量部を加え、汎用混合容器を用いて
10分間撹拌混合する。その後、40質量%の水酸化カ
リウム水溶液4.5質量部を加え、汎用混合容器で30
分間混合して正極合剤混合物を得る。次いで、この正極
合剤混合物をローラ径105mmのローラーコンパクタ
ーにより、被圧縮物の厚さが1mm以下になるように調
整して圧縮した。その後、この被圧縮物を破砕機によっ
て破砕した。次いで、振動篩機によって平均粒度分布1
4〜60メッシュ(平均粒径250〜1300μm)の
顆粒状の正極合剤を得た。To 90 parts by mass of nickel hydroxide particles having a high-order cobalt layer formed on the surface thereof, 5.4 parts by mass of graphite powder and 0.1 part by mass of a binder were added, and mixed by stirring for 10 minutes using a general-purpose mixing container. . Thereafter, 4.5 parts by mass of 40% by mass potassium hydroxide aqueous solution was added, and the mixture was mixed with a general-purpose mixing container to 30
Mix for minutes to obtain a positive electrode mixture mixture. Next, this positive electrode mixture mixture was adjusted by a roller compactor having a roller diameter of 105 mm so that the thickness of the object to be compressed would be 1 mm or less and compressed. Then, this object to be compressed was crushed by a crusher. Then, using a vibrating screener, average particle size distribution 1
A granular positive electrode mixture having 4 to 60 mesh (average particle size 250 to 1300 μm) was obtained.
【0025】次に、前記顆粒状正極合剤を素材として、
外径13.3mm、内径9.0mm、高さ(長さ)1
3.7mmの中空円筒状に加圧成形して、正極合剤ペレ
ットを作製した。この加圧成形工程においては、素材が
顆粒状であることに伴って、素材の取扱操作も容易で、
成形工程での損傷発生もなくて量産的であった。また、
成形体(正極合剤ペレット)を切断し、内部の組織状態
を検討したところ、緻密で、かつ正極活物質粒子及び導
電材などが良好な分散系を形成しており、機械的な強度
の向上も認められた。表1に、上記成形体50個の平均
密度(g/cm3)、及び平均圧潰強度(N)を示す。Next, using the granular positive electrode mixture as a material,
Outer diameter 13.3 mm, inner diameter 9.0 mm, height (length) 1
A positive electrode material mixture pellet was prepared by pressure molding into a 3.7 mm hollow cylinder. In this pressure molding process, the material is easy to handle because the material is granular.
It was mass-produced without any damage in the molding process. Also,
When the molded body (positive electrode material mixture pellets) was cut and the internal microstructure was examined, it was found to be dense and a positive dispersion of positive electrode active material particles and conductive materials was formed, improving mechanical strength. Was also recognized. Table 1 shows the average density (g / cm3) and the average crush strength (N) of the 50 molded articles.
【0026】[0026]
【表1】 [Table 1]
【0027】負極の作製Fabrication of negative electrode
【0028】インジウム0.01質量部、ビスマス0.
01質量部およびアルミニウム0.003質量部を含む
平均粒径100〜300μmの亜鉛合金粉末64.58
質量部に、ポリアクリル酸(ゲル化剤)0.381質量
部を加え、汎用混合容器で5分間撹拌・混合して均一な
混合系を得る。一方、酸化亜鉛3.5質量%を溶解した
35質量%の水酸化カリウム水溶液35質量部に、水酸
化テトラブチルアンモニウム0.0006質量部を加
え、10分間撹拌・混合して充分に分散させる。次い
で、この分散系に、前記亜鉛合金粉末系の混合物を4分
間かけて徐々に加えるとともに、200×105Pa
(150mmHg)以下の減圧状態で撹拌・混合し、さ
らに、13.3×105Pa(10mmHg)以下の減
圧状態で5分間撹拌・混合して、ほぼ均一な組成系のゲ
ル状負極を作製する。0.01 parts by weight of indium and 0.
Zinc alloy powder 64.58 having an average particle size of 100 to 300 μm and containing 01 parts by mass and 0.003 parts by mass of aluminum
0.381 parts by mass of polyacrylic acid (gelling agent) is added to parts by mass, and the mixture is stirred and mixed for 5 minutes in a general-purpose mixing container to obtain a uniform mixed system. On the other hand, 0.0006 parts by mass of tetrabutylammonium hydroxide is added to 35 parts by mass of a 35% by mass potassium hydroxide aqueous solution in which 3.5% by mass of zinc oxide is dissolved, and stirred and mixed for 10 minutes to sufficiently disperse. Then, to this dispersion, the zinc alloy powder-based mixture was gradually added over 4 minutes, and at the same time, 200 × 10 5 Pa was added.
The mixture is stirred and mixed under a reduced pressure of (150 mmHg) or less, and further stirred and mixed for 5 minutes under a reduced pressure of 13.3 × 10 5 Pa (10 mmHg) or less to prepare a gelled negative electrode having a substantially uniform composition system. .
【0029】電池の組立Battery assembly
【0030】次に、上記作製した正極合剤ペレット、お
よびゲル状負極を使用して、常套的な手法によって、図
1に概略構成を断面的に示す単一3形の亜鉛アルカリ電
池を組み立てた。図1において、1は正極端子を兼ねる
有底円筒状の金属缶(外装缶)であり、金属缶1の円筒
中空内には、正極合剤ペレットを3個積み重ねた状態
で、再度加圧成形した正極合剤2が充填・装着されてい
る。また、正極合剤2の中空部には、有底円筒状のセパ
レータ3が装着され、そのセパレータ3の内側にゲル状
負極4が充填されている。Next, using the positive electrode material mixture pellets prepared above and the gelled negative electrode, a single 3 type zinc alkaline battery whose schematic structure is shown in cross section in FIG. 1 was assembled by a conventional method. . In FIG. 1, reference numeral 1 denotes a bottomed cylindrical metal can (exterior can) that also serves as a positive electrode terminal. In the hollow of the metal can 1, three positive electrode material mixture pellets are stacked and again pressure-molded. The prepared positive electrode mixture 2 is filled and mounted. Further, a bottomed cylindrical separator 3 is mounted in the hollow portion of the positive electrode mixture 2, and a gelled negative electrode 4 is filled inside the separator 3.
【0031】そして、前記ゲル状負極4内には、真鍮性
の負極集電棒5の一端側が挿入・配置されており、この
負極集電棒5のゲル状負極4から突出する他端側の外周
面、および金属缶1の開口内周面の間に、ポリアミド樹
脂製の二重環状の絶縁性ガスケット6が配設される。な
お、この絶縁性ガスケット6の二重環状の間には、リン
グ状の金属板7が嵌着・配置されている。In the gelled negative electrode 4, one end side of a brass negative electrode current collector rod 5 is inserted and arranged, and the outer peripheral surface of the negative electrode current collector rod 5 on the other end side protruding from the gelled negative electrode 4 is inserted. , And a double annular insulating gasket 6 made of polyamide resin is arranged between the inner peripheral surface of the opening of the metal can 1. A ring-shaped metal plate 7 is fitted and arranged between the double rings of the insulating gasket 6.
【0032】また、負極端子を兼ねる帽子形の金属封口
板8が、負極集電棒5の先端部に当接する配置・構成と
なっている。ここで、金属缶1の開口端縁部は、内側に
屈曲されて絶縁性ガスケット6を介して、金属封口板8
によって金属缶1の開口端縁を密封した構成を採ってい
る。Further, the cap-shaped metal sealing plate 8 also serving as the negative electrode terminal is arranged and configured to abut the tip portion of the negative electrode current collector rod 5. Here, the opening edge portion of the metal can 1 is bent inward and the metal sealing plate 8 is inserted through the insulating gasket 6.
The metal can 1 has a configuration in which the opening edge is sealed.
【0033】比較例Comparative Example
【0034】実施例の亜鉛アルカリ電池用正極の製造・
構成において、正極合剤組成分の撹拌・混合後の圧縮破
砕、及び分級の処理・工程を省略した他は、実施例の場
合と同様の条件で、正極合剤ペレットを作製する。この
正極合剤ペレットを使用し、実施例の場合と同じ条件で
正極単3形の亜鉛アルカリ電池を作製する。なお、正極
合剤ペレット成形体50個の平均密度(g/cm3)、
及び平均圧潰強度(N)を表1に併せて示す。Production of Positive Electrode for Zinc Alkaline Battery of Example
In the constitution, the positive electrode material mixture pellets are produced under the same conditions as in the example except that the compression crushing after stirring and mixing the positive electrode material mixture composition and the classification treatment and process are omitted. Using this positive electrode material mixture pellet, a positive electrode AA zinc alkaline battery is manufactured under the same conditions as in the example. The average density (g / cm3) of 50 positive electrode material mixture pellet molded bodies,
The average crush strength (N) is also shown in Table 1.
【0035】上記組み立てた両亜鉛アルカリ電池50個
について、約48時間のエージング後20℃の温度雰囲
気下で、電池容量を測定・評価したときの平均値を表2
にそれぞれ示す。表2から分かるように、実施例の場合
は、比較例に較べて5%程度向上していた。Table 2 shows the average values when the battery capacities of 50 assembled zinc-alkali batteries were measured and evaluated in a temperature atmosphere of 20 ° C. after aging for about 48 hours.
Are shown respectively. As can be seen from Table 2, in the case of the example, it was improved by about 5% as compared with the comparative example.
【0036】[0036]
【表2】 [Table 2]
【0037】また、0.9Vまでの1500mA定電流
連続放電時間(重負荷放電特性)、及び10Ω定抵抗連
続放電時間(中負荷放電特性)をそれぞれ調べた。その
結果、実施例の場合は、比較例の場合と同程度の重負荷
放電特性を有する一方、中負荷放電特性が比較例に較べ
5%程度向上していた。Further, the constant current continuous discharge time up to 0.9 V (heavy load discharge characteristic) and the constant resistance continuous resistance time of 10Ω (medium load discharge characteristic) were examined. As a result, in the case of the example, while having the heavy load discharge characteristic similar to that of the comparative example, the medium load discharge characteristic was improved by about 5% as compared with the comparative example.
【0038】なお、上記実施例において、正極合剤組成
分中の黒鉛粉末を省略した他は、同一の条件で正極合剤
ペレットを成形した場合も、上記実施例の場合と同様
に、充填密度及び機械的な強度が向上され、高性能を呈
する正極を歩留まりよく得ることができた。また、この
正極合剤ペレットで正極を組み立てた亜鉛アルカリ電池
は、上記実施例の場合と同様に高容量で、かつ優れた重
・中負荷放電特性を呈した。It should be noted that, in the above-mentioned examples, the graphite powder in the positive electrode mixture composition was omitted, and also when the positive electrode mixture pellets were molded under the same conditions, the packing density was the same as in the above-mentioned examples. Moreover, the mechanical strength was improved, and a positive electrode exhibiting high performance could be obtained with good yield. Further, the zinc alkaline battery in which a positive electrode was assembled with the positive electrode material mixture pellets had a high capacity and exhibited excellent heavy / medium load discharge characteristics as in the case of the above-mentioned examples.
【0039】本発明は、上記実施例に限定されるもので
なく、発明の趣旨を逸脱しない範囲でいろいろの変形を
採ることができる。たとえば、上記では、筒状の単3形
亜鉛アルカリ電池用正極の製造を説明したが、筒状の単
1形、単2形、単4形、単5形、あるいは扁平形などの
製造にも適用できる。The present invention is not limited to the above embodiments, and various modifications can be made without departing from the spirit of the invention. For example, in the above, the manufacture of the cylindrical positive electrode for the AA zinc alkaline battery is described, but it is also applicable to the manufacture of the cylindrical single 1, single 2, single 4, single 5 or flat type. Applicable.
【0040】[0040]
【発明の効果】請求項1ないし4の発明によれば、正極
合剤組成物粒子(粉末)の圧縮破砕、及び分級の処理に
よって、充填密度が高く、機械的な強度も優れた筒状や
板状の正極成形体が容易に、歩留まりよく、また、量産
的に製造できる。そして、成形体の充填密度が向上する
ことにより、正極容量のアップとなって電池容量の向上
に寄与し、一方、機械的な強度が向上することにより、
筒状の場合など破損性が大幅に改善され、電池組立工程
などでの不良化もなくなり、歩留まりの向上が図られ
る。According to the first to fourth aspects of the present invention, by compressing and crushing the positive electrode mixture composition particles (powder) and classifying the mixture, a high packing density and excellent mechanical strength can be obtained. A plate-shaped positive electrode molded body can be easily manufactured with high yield and can be mass-produced. Then, by improving the packing density of the molded body, the positive electrode capacity is increased to contribute to the improvement of the battery capacity, while the mechanical strength is improved,
In the case of a tubular shape, the breakage is greatly improved, defects in the battery assembly process are eliminated, and the yield is improved.
【図面の簡単な説明】[Brief description of drawings]
【図1】実施例に係る亜鉛アルカリ電池の要部構成を示
す断面図。FIG. 1 is a cross-sectional view showing a main configuration of a zinc alkaline battery according to an embodiment.
1……金属缶(外装缶) 2……正極合剤 3……セパレータ 4……ゲル状負極 5……負極集電体 6……絶縁性ガスケット 7……リング状金属板 8……金属封口板 1 ... Metal can (exterior can) 2 ... Positive electrode mixture 3 …… Separator 4 ... Gel negative electrode 5 ... Negative electrode current collector 6 ... Insulating gasket 7: Ring-shaped metal plate 8: Metal sealing plate
Claims (4)
ニッケル系粒子、アルカリ電解液、及びバインダーを含
む正極組成成分を撹拌・混合する工程と、 前記撹拌・混合した組成物に圧縮破砕処理を施して得た
粒子を分級し顆粒状混合成分を得る工程と、 前記顆粒状混合成分を成形する工程と、を有することを
特徴とするアルカリ電池用正極の製造方法。1. A step of stirring and mixing positive electrode composition components including nickel hydroxide-based particles having a cobalt compound layer on the surface, an alkaline electrolyte, and a binder, and compression crushing treatment of the stirred and mixed composition. A method for producing a positive electrode for an alkaline battery, comprising: a step of classifying the particles obtained by the application to obtain a granular mixed component; and a step of molding the granular mixed component.
ていることを特徴とする請求項1記載のアルカリ電池用
正極の製造方法。2. The method for producing a positive electrode for an alkaline battery according to claim 1, wherein the positive electrode composition component contains a carbon-based conductive agent.
メッシュであることを特徴とする請求項1もしくは請求
項2記載のアルカリ電池用正極の製造方法。3. The particle size distribution of the granular positive electrode mixture is 14 to 60.
It is a mesh, The manufacturing method of the positive electrode for alkaline batteries of Claim 1 or Claim 2 characterized by the above-mentioned.
ト、三酸化二コバルト、一酸化コバルト、水酸化コバル
ト及び金属コバルトの少なくとも1種で形成されている
ことを特徴とする請求項1ないし請求項3いずれか一記
載のアルカリ電池用正極の製造方法。4. The cobalt compound layer is formed of at least one of cobalt oxyhydroxide, dicobalt trioxide, cobalt monoxide, cobalt hydroxide and metallic cobalt. The method for manufacturing the positive electrode for an alkaline battery according to any one of claims.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001199758A JP2003017044A (en) | 2001-06-29 | 2001-06-29 | Method of manufacturing positive electrode for alkali battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001199758A JP2003017044A (en) | 2001-06-29 | 2001-06-29 | Method of manufacturing positive electrode for alkali battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003017044A true JP2003017044A (en) | 2003-01-17 |
Family
ID=19037001
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001199758A Pending JP2003017044A (en) | 2001-06-29 | 2001-06-29 | Method of manufacturing positive electrode for alkali battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2003017044A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6991875B2 (en) | 2002-08-28 | 2006-01-31 | The Gillette Company | Alkaline battery including nickel oxyhydroxide cathode and zinc anode |
-
2001
- 2001-06-29 JP JP2001199758A patent/JP2003017044A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6991875B2 (en) | 2002-08-28 | 2006-01-31 | The Gillette Company | Alkaline battery including nickel oxyhydroxide cathode and zinc anode |
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