JPH0773049B2 - Method for manufacturing battery electrode - Google Patents
Method for manufacturing battery electrodeInfo
- Publication number
- JPH0773049B2 JPH0773049B2 JP62322544A JP32254487A JPH0773049B2 JP H0773049 B2 JPH0773049 B2 JP H0773049B2 JP 62322544 A JP62322544 A JP 62322544A JP 32254487 A JP32254487 A JP 32254487A JP H0773049 B2 JPH0773049 B2 JP H0773049B2
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- filling
- active material
- roller
- substrate
- 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.)
- Expired - Lifetime
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/32—Nickel oxide or hydroxide electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/043—Processes of manufacture in general involving compressing or compaction
- H01M4/0435—Rolling or calendering
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/26—Processes of manufacture
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 (イ) 産業上の利用分野 本発明はアルカリ蓄電池等に使用される、三次元的な連
通孔を有する金属多孔体を基体として用いる電池用電極
の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a method for producing an electrode for a battery, which is used in an alkaline storage battery or the like, and which uses a porous metal body having three-dimensional communication holes as a substrate. is there.
(ロ) 従来の技術 密閉式アルカリ蓄電池等に用いられる電極の製法とし
て、近年、焼結式に代って、三次元的な連通孔を有する
金属多孔体に活物質粉末を充填して作られる非焼結式製
法が研究されている。この製法は、製造工程が簡略化さ
れるとともに製造所要時間も短縮でき、更に電極の高エ
ネルギー密度化も容易なことから、コスト低減、性能向
上に有効な製法とみなされている。(B) Conventional technology As a method for manufacturing electrodes used in sealed alkaline storage batteries, etc., in recent years, instead of the sintering method, it is made by filling a metal porous body having three-dimensional communication holes with active material powder. Non-sintered manufacturing methods have been studied. This manufacturing method is regarded as an effective manufacturing method for cost reduction and performance improvement because the manufacturing process can be simplified, the manufacturing time can be shortened, and the energy density of the electrode can be easily increased.
この代表的な製法は、具体的には次の様な工程によるも
のである。ニツケル繊維のフエルト状焼結体(以下ニツ
ケルマツトと称する、繊維径20μ、平均孔径50μ、多孔
度93%の物性を有するもの)を基体として用い、これに
平均粒径20μの水酸化ニツケル粉末を主体とする活物質
粉末と糊料液とを混合して調製したスラリーを充填し、
乾燥後、加圧圧縮して完成電極とするものである。Specifically, this typical manufacturing method is based on the following steps. A felt-like sintered body of nickel fiber (hereinafter referred to as nickel matrix, having a fiber diameter of 20μ, an average pore diameter of 50μ and a physical property of porosity of 93%) is used as a substrate, and a nickel hydroxide powder having an average particle diameter of 20μ is mainly used as the base. Fill the slurry prepared by mixing the active material powder and the paste liquid to
After drying, it is compressed under pressure to obtain a finished electrode.
この製法と従来の焼結式製法との大きな相違点は前者
が、活物質スラリーを別途製造し基体内部へ充填するの
に対し、後者は活物質原料塩溶液を基板内部に含浸さ
せ、次いで化学的、電気化学的、あるいは熱的方法で、
この原料塩を活物質に転化させることにある。後者は、
活物質密度と塩溶液密度との差が大きいため1回の充填
操作で所定量の充填が行えないため、数次にわたって充
填操作を繰り返す必要がある。前者は充填密度の低さを
補うため、後工程でプレスする必要はあるが、1回の操
作で充填を完了できるという利点がある。ところで、こ
の特徴は焼結式製法が充填量を逐次計量し精度良く所定
値に合わせることができるが、一方非焼結式製法は、充
填操作が1回のみであるため所定値に合わせるのが難し
いという問題点がある。三次元金属多孔体への活物質充
填法は、種々提案されているが、(たとえば特開昭53−
10333号公報参照)いずれも、上記問題に対しては何ら
示唆するところがない。The major difference between this manufacturing method and the conventional sintering type manufacturing method is that the former separately manufactures the active material slurry and fills it into the inside of the substrate, while the latter impregnates the active material raw material salt solution inside the substrate and then chemically , Electrochemical, or thermal methods,
This is to convert this raw material salt into an active material. The latter is
Since the difference between the active material density and the salt solution density is large, it is not possible to perform a predetermined amount of filling in one filling operation, and therefore it is necessary to repeat the filling operation for several times. The former compensates for the low packing density and therefore requires pressing in a later step, but has the advantage that the packing can be completed in a single operation. By the way, this characteristic is that the sinter-type manufacturing method can measure the filling amount one after another and accurately adjust it to a predetermined value. There is a problem that it is difficult. Various methods for filling an active material into a three-dimensional porous metal have been proposed (see, for example, JP-A-53-53).
No. 10333) Nothing suggests the above problems.
(ハ) 発明が解決しようとする問題点 本発明は前記問題点に鑑みなされたものであって、金属
多孔体に対し、活物質スラリーの充填量を精度良く設定
量に合わせることを主眼とし、かかる製造方法により得
られた電池用電極の品質の安定性、電極特性の向上を計
るものである。(C) Problems to be solved by the present invention The present invention has been made in view of the above problems, with respect to the metal porous body, the main object is to accurately match the filling amount of the active material slurry with the set amount, The quality of the battery electrode obtained by such a manufacturing method is stable and the electrode characteristics are improved.
(ニ) 問題点を解決するための手段 本発明の電池用電極の製造方法は、三次元連続空孔を有
する金属多孔体に、活物質スラリーを充填し、次いで前
記活物質スラリー中に一部没するように設置したローラ
ーにより、前記金属多孔体を所定厚み迄圧縮し、さらに
ブレードをかけることを特徴とするものである。(D) Means for Solving the Problems The method for producing a battery electrode of the present invention is a metal porous body having three-dimensional continuous pores, filled with an active material slurry, and then partially contained in the active material slurry. It is characterized in that the metal porous body is compressed to a predetermined thickness by a roller installed so as to be submerged and further a blade is applied.
(ホ) 作用 本発明者らは、三次元連続空孔を有する金属多孔体(基
体)への均一な充填を行うための条件として、基体上で
スラリーの構成体である粉体と分散媒(たとえば糊料)
の分離が起こらないことが必要であり、基体へのスラリ
ー状活物質を充填する場合、充填量の設定値はスラリー
密度、基体の多孔度、厚さとに基づくものであることを
見い出した。即ち、設定値の活物質量に対し、スラリー
組成より所要スラリー量(体積)が決定でき、さらにこ
れと基体の寸法(縦・横)、多孔度とから、基体の必要
厚さが決められる。従って、理論的には、基体単位面積
当りの重量、厚さ、スラリー組成が均一になっていれ
ば、設定値と合致した均一な充填量が得られる。しかし
現実には基体厚さや重量は、或る幅で変動するし、充填
されたスラリー中に気泡が混入することもあるため、充
填量を均等にするのは困難である。このため充填前にロ
ーラーを通し、基体厚さを一定にする方法もあるが、十
分な効果は得られない。(E) Action The inventors of the present invention set the powder and the dispersion medium (slurry constituent) on the substrate as a condition for uniformly filling the porous metal body (substrate) having three-dimensional continuous pores. (For example, paste)
It has been found that, when it is necessary to fill the substrate with the slurry-like active material, the set value of the filling amount is based on the slurry density, the porosity of the substrate, and the thickness. That is, the required amount of slurry (volume) can be determined from the slurry composition for the set amount of active material, and the required thickness of the substrate can be determined from this, the dimensions (vertical / horizontal) of the substrate, and the porosity. Therefore, theoretically, if the weight per unit area of the substrate, the thickness, and the slurry composition are uniform, a uniform filling amount that matches the set value can be obtained. However, in reality, the thickness and weight of the substrate fluctuate within a certain range, and bubbles may be mixed in the filled slurry, so that it is difficult to make the filling amount uniform. For this reason, there is also a method of making the substrate thickness constant by passing it through a roller before filling, but the sufficient effect cannot be obtained.
これに対し発明者は厚さの調整を充填後行うことを試み
その効果が大きいことを知得し本発明を完成するに至っ
た。この方法は、基体を所定の厚さより幾分厚く作り、
これに活物質スラリーを充填し、しかる後ローラーを通
して所定の厚さまで基体を圧縮するとともに、剰余の活
物質スラリーを排出させさらに基体表面に付着している
スラリーをブレードでかき落とした後、乾燥するもので
ある。On the other hand, the inventor tried adjusting the thickness after filling, and realized that the effect was great, and completed the present invention. This method makes the substrate a little thicker than a predetermined thickness,
This is filled with the active material slurry, and then the base is compressed to a predetermined thickness through a roller, the surplus active material slurry is discharged, and the slurry adhering to the surface of the base is scraped off with a blade and then dried. Is.
一旦スラリーを過剰に充填し、次いでローラーを通すこ
とが大きな効果をもたらす理由は、充填時混入した空気
がローラーで圧縮する際に排出され、充填率のバラツキ
が縮小するためではないかと推測される。It is speculated that the reason why the effect of filling the slurry once excessively and then passing it through the roller is so great is that the air mixed during filling is discharged when the roller compresses and the variation in the filling rate is reduced. .
以下に上述内容に関するテスト結果を示す。The test results relating to the above contents are shown below.
活物質スラリーは、水酸化ニツケルを主成分とし、ヘキ
サメタリン酸ナトリウム0.1wt%、ヒドロキシプロピル
セルロース(HPC)0.1wt%、水30wt%を加え、調製した
粘度3000CPのもの、基体は、平均孔径250μ、厚さ1.0mm
のスポンジ状ニツケル(金属多孔体)、充填法は、内部
に充填ロールを設置し、活物質スラリーを満たした充填
槽中に、フープ状基体を導入するものである。第1表
は、基体をスラリー充填前もしくは後に厚み調整を行い
充填率の比較を行った結果である。The active material slurry has nickel hydroxide as a main component, sodium hexametaphosphate 0.1 wt%, hydroxypropyl cellulose (HPC) 0.1 wt%, and water 30 wt% are added to prepare a viscosity of 3000 CP. The substrate has an average pore diameter of 250 μ, Thickness 1.0 mm
In the sponge-like nickel (metal porous body) filling method, a filling roll is installed inside, and the hoop-like substrate is introduced into a filling tank filled with the active material slurry. Table 1 shows the results of comparing the filling rates by adjusting the thickness of the substrate before or after the slurry filling.
第1表より、充填後調整を行ったものは、バラツキ
(σ)が小さく、充填率も高いものであることがわか
る。一方、実験の中で厚さ調整用ローラーは一旦充填し
たスラリーを基体から絞り出すが、連続稼動する場合、
この絞り出されたスラリーの固形分がローラー表面に固
着する場合がありこれを防止する必要があること、また
ローラー位置により上記充填量バラツキが変動すること
が判った。これに関し実験を行い、ローラー位置は少く
ともローラーの一部がスラリー液面に接していること、
望ましくはローラーの基体加圧部までスラリー中に没し
ていること(第2表参照)、また圧縮量は0.1mmを越え
ないのが望ましい(第3表参照)ことが判った。 From Table 1, it can be seen that the dispersions adjusted after filling have a small variation (σ) and a high filling rate. On the other hand, in the experiment, the thickness adjusting roller squeezes the once filled slurry from the substrate, but when continuously operating,
It has been found that the solid content of the squeezed slurry may stick to the roller surface in some cases and it is necessary to prevent this, and that the variation in the filling amount varies depending on the roller position. An experiment was conducted on this, and the roller position is that at least part of the roller is in contact with the slurry liquid level,
It has been found that it is desirable that the roller is pressed to the substrate pressing portion in the slurry (see Table 2), and that the compression amount should not exceed 0.1 mm (see Table 3).
以下この実験結果を第2表第3表に示す。尚、スラリー
組成、基体は、前述のものと同一である。第2表におい
て、◎はローラー表面付着物が全く無い状態であり、○
は僅かに付着物があるがローラーの連続稼動可なもので
あり、△は短時間のみローラーの稼動可能なことを示
す。第3表においてローラー位置はスラリー内に1/2没
している状態としてある。The results of this experiment are shown in Table 2 and Table 3 below. The slurry composition and the substrate are the same as those described above. In Table 2, ⊚ indicates that there is no deposit on the roller surface, and ○
Indicates that the roller can be continuously operated although there is a slight amount of deposit, and Δ indicates that the roller can be operated only for a short time. In Table 3, the roller position is in a state of being half immersed in the slurry.
ローラーがスラリー内にある方が、良好な理由は、ロー
ラー表面の濡れ状態が一定になり、基体から絞り出され
たスラリーの固形分量割合(スラリーの含水率)が、槽
中スラリーのそれと同一であり、固−液分離が起こらな
いためである。またローラーがスラリー中に完全に没し
ている場合、多少充填量が大きくなるのは、ローラーで
調厚した後基体がスプリングバツグし、この時基体の周
囲に多量のスラリーがあるとそれが再充填されるためで
ある。したがってローラー位置は、槽中スラリーに少く
とも一部は接していること、さらにでき得れば1/2ま
で、既ち基体を加圧する部分まで没するよう設置するの
が好ましい。 The reason why the roller is better in the slurry is that the wet state of the roller surface becomes constant, and the solid content ratio (slurry water content) of the slurry squeezed from the substrate is the same as that of the slurry in the tank. This is because solid-liquid separation does not occur. When the roller is completely submerged in the slurry, the filling amount increases a little because the base is spring-backed after the thickness is adjusted by the roller, and if there is a large amount of slurry around the base, it is This is because they are filled. Therefore, it is preferable that at least a part of the roller position is in contact with the slurry in the tank, and if possible, the roller position is set so as to be submerged up to a half of the existing substrate.
さらに厚みの調整幅については0.10mmを越える圧縮では
基体厚みの精度が低下するとともに、ローラー表面への
粉末付着が始まるので避ける必要がある。圧縮量1.0mm
以上で充填率が向上するのは(第3表参照)、充填され
たスラリーから水分が優先的に絞り出され含水率が低下
するためである。Further, with respect to the thickness adjustment range, it is necessary to avoid the compression of more than 0.10 mm because the accuracy of the substrate thickness decreases and the powder adheres to the roller surface. Compression amount 1.0 mm
The reason why the filling rate is improved as described above (see Table 3) is that water is preferentially squeezed out from the filled slurry to lower the water content.
この様な条件で充填を行っても、基体表面にスラリーの
薄膜ができてしまうがこの膜厚は、均等にならない。従
って、最終段階乾燥前にブレードをかけ、この膜を除去
することにより充填量バラツキはさらに縮少できる。Even if filling is performed under such conditions, a thin film of slurry is formed on the surface of the substrate, but the film thickness is not uniform. Therefore, the variation in the filling amount can be further reduced by applying a blade before the final stage drying and removing this film.
(ヘ) 実施例 本発明を実施する装置の代表的な構成を模式図として図
に示す。図中1は充填槽、2は活物質スラリー、3は基
体、4、6は案内ローラー、5は充填ローラー、7はブ
レード、8は本発明の特徴である基体厚を調整するた
め、活物質スラリー中に1/2没するよう設置した調厚ロ
ーラーである。(F) Example A typical configuration of an apparatus for carrying out the present invention is shown in the figure as a schematic diagram. In the figure, 1 is a filling tank, 2 is an active material slurry, 3 is a substrate, 4 and 6 are guide rollers, 5 is a filling roller, 7 is a blade, and 8 is an active material for adjusting the substrate thickness, which is a feature of the present invention. It is a thickness control roller installed so that it is submerged in the slurry by half.
(実施例1) 水酸化ニツケルを主成分とする粉末100部、HPC0.1部、
ヘキサメタリン酸ナトリウム0.1部、水30部からなる粘
度4000CPのスラリーを、厚さ1.0mmのスポンジ状ニツケ
ルに図に示す装置により充填した。この時の充填後の圧
縮量は0.03mmである。(Example 1) 100 parts of powder containing nickel hydroxide as a main component, 0.1 part of HPC,
A slurry having a viscosity of 4000 CP consisting of 0.1 part of sodium hexametaphosphate and 30 parts of water was filled in a sponge nickel having a thickness of 1.0 mm by the device shown in the figure. The compression amount after filling at this time is 0.03 mm.
(実施例2) 水酸化ニツケルを主成分とする粉末100部、HPC0.4部、
水55部からなる粘度2000CPのスラリーを、厚さ1.35mmの
スポンジ状ニツケルに、実施例1と同一条件で充填し
た。Example 2 100 parts of powder containing nickel hydroxide as a main component, 0.4 part of HPC,
A slurry of 55 parts of water having a viscosity of 2000 CP was filled in a sponge nickel having a thickness of 1.35 mm under the same conditions as in Example 1.
(比較例1) 実施例1で用いたのと同じ基体をあらかじめ0.97mmに圧
縮した後、充填後の圧縮工程を省略した他は実施例1と
同一条件で充填した。(Comparative Example 1) The same substrate as used in Example 1 was previously compressed to 0.97 mm and then charged under the same conditions as in Example 1 except that the compression step after filling was omitted.
(比較例2) 実施例1と同じ基体を用い、充填後の圧縮工程を省略し
た他は実施例と同一条件で充填した。これらの極板を、
全て活物質スラリー充填後同一条件でブレードをかけ、
乾燥し、次いでカレンダーローラで圧延した。(Comparative Example 2) The same substrate as in Example 1 was used, and the filling was performed under the same conditions as in Example except that the compression step after filling was omitted. These plates,
After filling all the active material slurry, apply a blade under the same conditions,
It was dried and then rolled with a calendar roller.
前記実施例の極板の充填率及び、カレンダーローラーで
圧延した後の極板伸び等について、第4表に示す。Table 4 shows the filling factor of the electrode plates of the above-mentioned examples and the elongation of the electrode plates after rolling with a calender roller.
以上のように本発明に係る電極板は充填量バラツキが少
いだけでなく、これが次工程での品質バラツキを抑制す
るという特徴を有する。 As described above, the electrode plate according to the present invention has a feature that not only the variation in the filling amount is small, but also the variation in quality in the next step is suppressed.
また、実施例2にも示したように、本発明の効果は流動
性があり、固液分離の起こりにくいスラリーであれば同
様に得られ、幅広く応用可能である。Further, as shown in Example 2, the effect of the present invention can be similarly obtained as long as the slurry has fluidity and solid-liquid separation hardly occurs, and can be widely applied.
さらに実施例では水酸化ニツケルを活物質とするニツケ
ル陽極についてのみ述べたが、本発明は三次元金属多孔
体にスラリー化した粉末状活物質を直接充填する方式の
製法であればこれに限らず応用できる。そして三次元金
属多孔体としては、実施例で示したスポンジ状ニツケル
以外に、ニツケルマツト等も使用できることは言うまで
もない。Furthermore, in the examples, only the nickel anode using nickel hydroxide as an active material is described, but the present invention is not limited to this as long as it is a method of directly filling the powdered active material slurried in the three-dimensional metal porous body. It can be applied. Needless to say, a nickel matte or the like can be used as the three-dimensional metal porous body other than the sponge-like nickel shown in the examples.
(ト) 発明の効果 本発明の電池用電極の製造方法によれば、金属多孔体へ
の活物質が均一かつ精度良く充填できるので、かかる金
属多孔体を用いた電極の電極特性を安定させることが可
能となり、その工業的価値はきわめて大きい。(G) Effect of the Invention According to the method for producing a battery electrode of the present invention, the active material can be uniformly and accurately filled in the metal porous body, so that the electrode characteristics of the electrode using the metal porous body can be stabilized. Is possible and its industrial value is extremely high.
図は本発明を模式的に示す充填方法の概念図である。 1……充填槽、2……活物質スラリー、3……基体(金
属多孔体)、4,6……案内ローラー、5……充填ローラ
ー、7……ブレード、8……調厚ローラー。The figure is a conceptual diagram of a filling method schematically showing the present invention. 1 ... Filling tank, 2 ... Active material slurry, 3 ... Substrate (porous metal body), 4,6 ... Guide roller, 5 ... Filling roller, 7 ... Blade, 8 ... Thickness adjusting roller.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 富田 正仁 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (72)発明者 浜松 太計男 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Masahito Tomita, 2-18 Keihan Hon-dori, Moriguchi City, Osaka Prefecture Sanyo Electric Co., Ltd. (72) Takeio Hamamatsu 2--18, Keihan Hon-dori, Moriguchi City, Osaka Sanyo Electric Co., Ltd.
Claims (3)
物質スラリーを充填し、次いで前記活物質スラリー中に
一部没するように設置したローラーにより、前記金属多
孔体を所定厚み迄圧縮し、更にブレードをかけることを
特徴とする電池用電極の製造方法。1. A metal porous body having three-dimensional continuous pores is filled with an active material slurry, and then the roller is installed so as to be partially submerged in the active material slurry, so that the metal porous body has a predetermined thickness. A method for producing a battery electrode, comprising compressing and further applying a blade.
こさない流動性を有するものであること特徴とする特許
請求の範囲第項記載の電池用電極の製造方法。2. The method for producing a battery electrode according to claim 1, wherein the slurry active material has a fluidity that does not cause solid-liquid separation.
金属多孔体圧縮部まで活物質スラリー中に没するように
設置したものであることを特徴とする特許請求の範囲第
項記載の電池用電極の製造方法。3. The battery according to claim 1, wherein the roller for compressing the porous metal body is installed so that the compression portion of the porous metal body is immersed in the active material slurry. For manufacturing electrodes for use.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62322544A JPH0773049B2 (en) | 1987-12-18 | 1987-12-18 | Method for manufacturing battery electrode |
| US07/225,696 US4887349A (en) | 1987-07-30 | 1988-07-29 | Method and apparatus for manufacturing electrode for battery |
| DE3826153A DE3826153A1 (en) | 1987-07-30 | 1988-08-01 | METHOD AND DEVICE FOR PRODUCING AN ELECTRODE FOR A BATTERY |
| FR8810377A FR2618949B1 (en) | 1987-07-30 | 1988-08-01 | METHOD AND DEVICE FOR MANUFACTURING A BATTERY ELECTRODE |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62322544A JPH0773049B2 (en) | 1987-12-18 | 1987-12-18 | Method for manufacturing battery electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01163965A JPH01163965A (en) | 1989-06-28 |
| JPH0773049B2 true JPH0773049B2 (en) | 1995-08-02 |
Family
ID=18144854
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62322544A Expired - Lifetime JPH0773049B2 (en) | 1987-07-30 | 1987-12-18 | Method for manufacturing battery electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0773049B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05299080A (en) * | 1992-04-24 | 1993-11-12 | Shin Kobe Electric Mach Co Ltd | Method of applying paste without bubbles to battery electrode substrate |
| US7846574B2 (en) | 2004-08-27 | 2010-12-07 | Panosonic Corporation | Positive electrode plate for alkaline storage battery and method for producing the same |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61203560A (en) * | 1985-03-05 | 1986-09-09 | Yuasa Battery Co Ltd | Method for packing active material for battery |
-
1987
- 1987-12-18 JP JP62322544A patent/JPH0773049B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01163965A (en) | 1989-06-28 |
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