JPH0480513B2 - - Google Patents
Info
- Publication number
- JPH0480513B2 JPH0480513B2 JP58240140A JP24014083A JPH0480513B2 JP H0480513 B2 JPH0480513 B2 JP H0480513B2 JP 58240140 A JP58240140 A JP 58240140A JP 24014083 A JP24014083 A JP 24014083A JP H0480513 B2 JPH0480513 B2 JP H0480513B2
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- spherical
- powder
- positive electrode
- paste
- 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
-
- 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)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は電池用ニツケル正極およびその製造法
に関するものであり、詳しくはアルカリ電池用の
非焼結式ニツケル正極に適用されるものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a nickel positive electrode for batteries and a method for manufacturing the same, and more specifically, it is applied to a non-sintered nickel positive electrode for alkaline batteries.
従来の構成とその問題点
従来よりアルカリ電池用ニツケル正極に使用す
る非焼結式ニツケル正極、つまり水酸化ニツケル
粉末を活物質として直接使用する正極には、硫酸
ニツケルとアルカリとの中和反応で沈殿析出する
水酸化ニツケル塊状物を乾燥固化し、ついでこれ
を粉砕した粉末を使用している。この場合の粒子
形状は、粉砕工程を経ることで破断面を有するた
め、全体としては米粒状態であるが、比較的平面
で構成され角ばつた形状を有している。Conventional structure and its problems Traditionally, non-sintered nickel positive electrodes used in alkaline battery nickel positive electrodes, that is, positive electrodes that directly use nickel hydroxide powder as the active material, have been developed through a neutralization reaction between nickel sulfate and alkali. A powder obtained by drying and solidifying the precipitated nickel hydroxide lumps and then pulverizing this is used. The shape of the particles in this case has a fractured surface through the pulverization process, so that they are in the form of rice grains as a whole, but they are relatively flat and have an angular shape.
また粉砕によつて平均粒子径も1〜200μmと
広く分布し、これを活物質としてポケツト式のニ
ツケル正極や、発泡メタル式のニツケル正極(三
次元網状のスポンジ状基板内に活物質を充填ある
いは塗布するもの)に用いる場合、次のような問
題点を有していた。 In addition, the average particle diameter is widely distributed from 1 to 200 μm through pulverization, and this is used as an active material to make pocket-type nickel positive electrodes, foamed metal-type nickel positive electrodes (active material filled in a three-dimensional network sponge-like substrate, or When used in coatings), there were the following problems.
ポケツト式ニツケル正極では、微細な粒子が混
入するので、多数の微孔を有する金属ポケツトの
微孔から活物質粒子が脱落する危険性がある。ま
た発泡メタル式ニツケル正極においても同様な問
題があり、また活物質としてペースト状練合物を
用いる場合は、ペースト性状の安定化、たとえば
流動性に粒子形状と粒径のバラツキが影響を及ぼ
し、一定した流動性が得られにくく、充填性に関
係して支持体や電極基板への充填量が不安定にな
る危険性を有している。 In the pocket-type nickel positive electrode, since fine particles are mixed in, there is a risk that the active material particles may fall out from the pores of the metal pocket, which has many pores. Similar problems exist in foamed metal nickel positive electrodes, and when a paste-like mixture is used as the active material, variations in particle shape and particle size affect the stability of the paste properties, such as fluidity. It is difficult to obtain constant fluidity, and there is a risk that the amount filled into the support or electrode substrate may become unstable due to filling properties.
すなわち粉砕によつて得られる微粉末は、破断
面をもつとともにその粒子形状が不規則となり、
粒径を小さくする程、相対的に非表面積が増大す
る。このため粒子表面に吸着される液体(練液)
量も多くなり、粒径によつて吸着液体量が異なる
ことからペーストとして一定の流動性を保つこと
が難しい。発泡メタルからなる基板にペーストを
充填する際、粒子径が小さい水酸化ニツケル粉末
を用いると、ペーストとしての充填は容易になる
が、ペースト中における粉末含有率が低下して正
極としてのエネルギー密度は高まらない。 In other words, the fine powder obtained by pulverization has a fractured surface and its particle shape is irregular.
As the particle size becomes smaller, the non-surface area increases relatively. For this reason, the liquid (kneading solution) that is adsorbed on the particle surface
Since the amount of adsorbed liquid increases and the amount of adsorbed liquid varies depending on the particle size, it is difficult to maintain constant fluidity as a paste. When filling a paste into a substrate made of foamed metal, using nickel hydroxide powder with a small particle size makes it easier to fill the paste, but the powder content in the paste decreases and the energy density as a positive electrode decreases. It doesn't increase.
発明の目的
本発明は、非焼結式ニツケル正極に用いる水酸
化ニツケル粉末主体の混合物の基板あるいは支持
体からの脱落の抑制、およびこの混合物をペース
ト状態で基板または支持体に充填あるいは塗布す
る際のペースト流動性の不安定性を防止し、充填
性がよく、エネルギー密度の高いニツケル正極お
よびその製造法を提供することを目的とする。Purpose of the Invention The present invention aims to suppress the falling off of a mixture mainly composed of nickel hydroxide powder used in a non-sintered nickel positive electrode from a substrate or support, and to prevent the mixture from falling off a substrate or support in the form of a paste. The purpose of the present invention is to provide a nickel positive electrode that prevents instability of paste fluidity, has good filling properties, and has a high energy density, and a method for manufacturing the same.
発明の構成
本発明は粒子形状が球状、ほぼ球状、鶏卵状も
しくはこれらを集合したものからなり、かつ粒度
分布が狭い範囲にまとまつた水酸化ニツケル粉末
を主体とし、これに導電材等を混合した混合物を
使用することを特徴とするものである。そしてこ
の混合物を、発泡メタル式あるいはポケツト式等
の非焼結式ニツケル正極に適用するものである。Structure of the Invention The present invention mainly consists of nickel hydroxide powder, which has a particle shape of spherical, almost spherical, egg-shaped, or a combination of these, and has a narrow particle size distribution, and which is mixed with a conductive material, etc. It is characterized by the use of a mixture. This mixture is then applied to a non-sintered nickel positive electrode such as a foamed metal type or a pocket type.
前者の発泡メタル式電極の場合には第1図Aに
示すように活物質を主とする粉末1と、これを保
持する金属基板としての発泡メタル2とにより構
成される。また後者は発泡メタルの代りに多数の
微孔4を有する金属製ポケツト3を支持体とし、
これに活物質粉末主体の粉末混合物を充填したも
のである。 In the case of the former foamed metal type electrode, as shown in FIG. 1A, it is composed of a powder 1 mainly containing an active material and a foamed metal 2 as a metal substrate for holding the powder. In addition, the latter uses a metal pocket 3 having a large number of micropores 4 as a support instead of foam metal,
This is filled with a powder mixture consisting mainly of active material powder.
そして金属基板あるいは支持体に充填する活物
質粉末6は、第2図Aに示すような従来の粉砕さ
れ主として平面で構成され角ばつていて、しかも
粒子径のバラツキも多い粉末に代わつて、第2図
Bに示すように球状、ほぼ球状、鶏卵状もしくは
これらの集合物からなり、平均粒子径も1〜
100μmの間のバラツキの少ないものである。 The active material powder 6 to be filled into the metal substrate or support is replaced with the conventional pulverized powder, which is mainly composed of planes, has angular shapes, and has many variations in particle size, as shown in FIG. 2A. As shown in Figure 2B, it is spherical, almost spherical, egg-shaped, or an aggregate of these, and the average particle size is 1 to 1.
There is little variation within 100 μm.
この球状、ほぼ球状、鶏卵状もしくはこれらを
集合したものは、いずれもその表面が曲面で構成
されていて、全体に丸みをもつたものであり、そ
の比表面積も小さい。 The spherical, almost spherical, egg-shaped, or aggregation of these shapes all have curved surfaces, are rounded overall, and have a small specific surface area.
そして練液その他とでペーストを調整した際に
もペースト中での分散状態が良好で、流動性のよ
いものにでき、これを金属基板へ充填あるいは塗
着した際に、活物質粉末のつまり具合がよく、極
板の高エネルギー化が図れる。 Furthermore, even when the paste is prepared with a mixing solution or other additives, the dispersion state in the paste is good and the paste has good fluidity.When this paste is filled or applied to a metal substrate, the active material powder becomes clogged. This allows for high energy consumption of the electrode plate.
実施例の説明
実施例 1
攪拌翼を高速回転させている攪拌槽内に濃度約
1Nの硫酸ニツケル水溶液を流入させる一方、フ
レーク状のNaOH粉末を投入し、攪拌状態でPH
を約11に維持して温度は約40℃に保つ。攪拌槽の
両側から連続して各々を投入しつづけ、ゆつくり
と熟成して球状、ほぼ球状、鶏卵状もしくはこれ
らが集合して大きく成長した粒子、あるいは攪拌
により角が削りとられ球状、ほぼ球状あるいは鶏
卵状となつた粒子だけを取り出して水酸化ニツケ
ル粉末を得る。ここでの粉末の平均粒子径は1〜
100μmであつた。Description of Examples Example 1 A concentration of approximately
While 1N nickel sulfate aqueous solution is introduced, flaky NaOH powder is added and the pH is adjusted under stirring.
to about 11 and the temperature to about 40℃. Each particle is continuously added from both sides of the stirring tank, and the particles are slowly matured into spherical, almost spherical, or egg-shaped particles, or particles that have grown large by aggregation of these, or particles whose corners have been shaved off by stirring and become spherical or almost spherical. Alternatively, only the egg-shaped particles are taken out to obtain nickel hydroxide powder. The average particle size of the powder here is 1~
It was 100 μm.
この粉末100gに対してニツケル粉末20g、コ
バルト粉末5gの比率の混合物を水70c.c.でペース
ト状に練合する。これを密着性の良いポンプで吸
い上げ、発泡メタルからなる基板(厚さ1.3mm、
多孔度約95%)に吹きつけて充填し、乾燥後加圧
して厚さ約0.7mmとし、これを1.2wt%のフツ素樹
脂を含む懸濁液に浸漬して再び乾燥し、第1図A
に示すようなニツケル正極を得る。 A mixture of 20 g of nickel powder and 5 g of cobalt powder per 100 g of this powder is kneaded with 70 c.c. of water to form a paste. This is sucked up with a pump with good adhesion, and a substrate made of foam metal (1.3 mm thick,
After drying, it was pressurized to a thickness of about 0.7 mm, which was immersed in a suspension containing 1.2 wt% fluororesin and dried again. A
Obtain a nickel positive electrode as shown in .
実施例 2
約20μmの微孔を多数有する厚さ約0.1mmのニツ
ケル製ポケツトの中に実施例1と同様にして得た
水酸化ニツケル粉末とグラフアイトとの混合物を
充填し、第1図Bに示すようなポケツト式ニツケ
ル正極を得る。なお、図中5は電極内に形成され
た空間部を示す。次に実施例1と同様にして得た
ニツケル正極を40×55mmの大きさに切断し、活物
質の充填量(全体の重量−基板の重量)の分析を
350枚の極板につき調べた。Example 2 A mixture of nickel hydroxide powder and graphite obtained in the same manner as in Example 1 was filled into a nickel pocket with a thickness of about 0.1 mm and having many micropores of about 20 μm, and as shown in FIG. 1B. Obtain a pocket-type nickel positive electrode as shown in . Note that 5 in the figure indicates a space formed within the electrode. Next, the nickel positive electrode obtained in the same manner as in Example 1 was cut into pieces of 40 x 55 mm, and the amount of active material filled (total weight - weight of the substrate) was analyzed.
We investigated 350 electrode plates.
その結果を第3図のaに示す。比較として従来
使用していた塊状物を粉砕して得た粉末を用いた
場合のそれをbに示す。この結果本発明の水酸化
ニツケル粉末を用いた場合は、その粒子形状が球
状、ほぼ球状、鶏卵状もしくはこれらを集合した
ものであつていずれも丸みをもち、その比表面積
は小さく、ペーストを調整する際でも粒子表面に
吸着される練液量が少なく、ペースト中での粉末
の分散状態が良好でペーストの流動性がよい。 The results are shown in Figure 3a. For comparison, a powder obtained by pulverizing a conventionally used lump is used, and the result is shown in b. As a result, when the nickel hydroxide powder of the present invention is used, the particle shape is spherical, almost spherical, egg-shaped, or a combination of these, all of which are round, and the specific surface area is small, and the paste can be adjusted. Even when the paste is mixed, the amount of mixing solution adsorbed on the particle surface is small, the powder is well dispersed in the paste, and the paste has good fluidity.
このため、基板に対するペースト状態の活物質
充填量のバラツキは従来よりもはるかに少なく、
単位体積当り多くの活物質を充填あるいは塗着で
き、極板のエネルギー密度を高め得ることがわか
つた。 Therefore, the variation in the amount of active material filled in the paste state on the substrate is much smaller than before.
It was found that a large amount of active material can be filled or coated per unit volume, and the energy density of the electrode plate can be increased.
またポケツト式電極に用いた場合、左右1cmの
幅で5Gの振動を加えて脱落物の重量を測定した
ところ、従来粉末では10分間で充填量100gに対
し5gの脱落が生じたが、本発明による粉末を使
用した場合は充填性がよく、その脱落量は0.5g
程度ときわめて少なかつた。 In addition, when used in a pocket-type electrode, when we applied 5G vibration in a width of 1 cm on the left and right sides and measured the weight of the falling off material, we found that with conventional powder, 5 g of fallen material fell out in 10 minutes per 100 g filled amount, but with the present invention. When using powder from
The extent of this was extremely small.
発明の効果
以上の結果からも明らかなように、本発明の粒
子形状が球状、ほぼ球状、鶏卵状もしくはこれら
の集合物からなる水酸化ニツケル粉末を活物質に
使用した非焼結式電極は、その電極製造上での取
り扱いが極めて安定し、基板もしくは支持体に対
する活物質の充填容量の均一化が図れる。Effects of the Invention As is clear from the above results, the non-sintered electrode of the present invention using the nickel hydroxide powder having a spherical, almost spherical, or egg-shaped particle shape or an aggregate thereof as an active material has the following effects: Handling during electrode production is extremely stable, and the filling capacity of the active material to the substrate or support can be made uniform.
また、球状、ほぼ球状、鶏卵状もしくはこれら
を集合した丸みのある粒子形状も、前期反応浴の
PHと温度を制御しながらニツケル塩とアルカリを
攪拌しながら中和反応させる方法で容易かつ適切
に得ることができる。 In addition, particle shapes that are spherical, almost spherical, egg-shaped, or a combination of these may also be used in the early reaction bath.
It can be easily and appropriately obtained by stirring and neutralizing nickel salt and alkali while controlling the pH and temperature.
第1図Aは本発明における発泡メタル式ニツケ
ル正極を示す略図、同Bはポケツト式ニツケル正
極の概略断面図、第2図Aは従来より使用されて
いる水酸化ニツケル粉末の概略図、同Bは本発明
における球状水酸化ニツケル粉末の概略図、第3
図は本発明の実施例で得られた電極を44×55mmに
切断した場合の活物質充填量の分布を示す図であ
る。
1……水酸化ニツケルを主体とした混合粉末、
2……発泡メタル、3……金属製ポケツト、4…
…微孔、5……空間部、6……活物質。
Figure 1A is a schematic diagram showing a foamed metal type nickel positive electrode according to the present invention, Figure 2B is a schematic cross-sectional view of a pocket type nickel positive electrode, Figure 2A is a schematic diagram of a conventionally used nickel hydroxide powder, and Figure 2B is a schematic diagram of a nickel hydroxide powder used conventionally. 3 is a schematic diagram of spherical nickel hydroxide powder in the present invention.
The figure shows the distribution of the active material filling amount when the electrode obtained in the example of the present invention is cut into 44×55 mm. 1...Mixed powder mainly composed of nickel hydroxide,
2...foamed metal, 3...metal pocket, 4...
...Micropore, 5...Space, 6...Active material.
Claims (1)
を乾燥状態もしくはペースト状態で金属基板また
は支持体内部に充填あるいは塗布したニツケル正
極であつて、使用する水酸化ニツケル粉末の粒子
形状が球状、ほぼ球状、鶏卵状もしくはこれらを
集合したものであり、その表面は曲面が主体で構
成されている電池用ニツケル正極。 2 使用するニツケル粉末の平均粒子径が1〜
100μmの範囲にある特許請求の範囲第1項に記
載の電池用ニツケル正極。 3 ニツケル塩水溶液とアルカリを反応槽内に流
入あるいは投入し、攪拌しながらこれを所定のPH
値および温度に保ち、反応熟成により粒子形状を
球状、ほぼ球状、鶏卵状もしくはこれらの集合物
に成長させ、その表面は曲面主体で構成された水
酸化ニツケル粉末を主体とする粉末混合物もしく
はペーストを調整し、これを金属基板または支持
体に充填あるいは塗布した電池用ニツケル正極の
製造法。[Claims] 1. A nickel positive electrode in which a powder mixture mainly composed of nickel hydroxide powder is filled or applied in a dry state or paste state into a metal substrate or support, the particle shape of the nickel hydroxide powder used. A nickel positive electrode for batteries is spherical, almost spherical, egg-shaped, or a combination of these, and its surface is mainly composed of curved surfaces. 2 The average particle size of the nickel powder used is 1~
A nickel positive electrode for a battery according to claim 1 having a thickness in the range of 100 μm. 3 Flow or inject the nickel salt aqueous solution and alkali into the reaction tank, and bring it to the specified pH while stirring.
A powder mixture or paste mainly composed of nickel hydroxide powder is maintained at a certain temperature and the particle shape is grown into a spherical, almost spherical, egg-like shape, or an aggregate of these through reaction aging, and the surface is mainly composed of curved surfaces. A method for manufacturing a nickel positive electrode for batteries, which is prepared and filled or coated onto a metal substrate or support.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58240140A JPS60131765A (en) | 1983-12-20 | 1983-12-20 | Nickel positive electrode for batteries and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58240140A JPS60131765A (en) | 1983-12-20 | 1983-12-20 | Nickel positive electrode for batteries and its manufacturing method |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6086533A Division JP3032421B2 (en) | 1994-04-25 | 1994-04-25 | Manufacturing method of nickel positive electrode for batteries |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60131765A JPS60131765A (en) | 1985-07-13 |
| JPH0480513B2 true JPH0480513B2 (en) | 1992-12-18 |
Family
ID=17055085
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58240140A Granted JPS60131765A (en) | 1983-12-20 | 1983-12-20 | Nickel positive electrode for batteries and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60131765A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1890350A2 (en) | 1997-02-03 | 2008-02-20 | Matsushita Electric Industrial Co., Ltd. | The manufacturing method of active materials for the positive electrode in alkaline storage batteries |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0732013B2 (en) * | 1985-12-10 | 1995-04-10 | 松下電器産業株式会社 | Nickel electrode manufacturing method for alkaline batteries |
| JPS62222566A (en) * | 1986-03-24 | 1987-09-30 | Yuasa Battery Co Ltd | Nickel electrode for alkaline battery |
| JPH0724218B2 (en) * | 1988-04-11 | 1995-03-15 | 株式会社ユアサコーポレーション | Nickel electrode for alkaline battery and battery using the same |
| JPH026340A (en) * | 1988-04-13 | 1990-01-10 | Kansai Shokubai Kagaku Kk | Production of nickel hydroxide |
| US5366831A (en) * | 1991-06-14 | 1994-11-22 | Yuasa Corporation | Nickel electrode for alkaline battery |
| JPWO2005104272A1 (en) | 2004-04-23 | 2008-03-13 | 松下電器産業株式会社 | Alkaline primary battery and method for producing positive electrode material thereof |
| JP4952038B2 (en) * | 2006-04-25 | 2012-06-13 | パナソニック株式会社 | Positive electrode for alkaline storage battery and alkaline storage battery |
| JP6947541B2 (en) | 2017-06-09 | 2021-10-13 | Fdk株式会社 | Non-sintered positive electrode for alkaline secondary battery and alkaline secondary battery equipped with this non-sintered positive electrode |
| JP7495196B2 (en) | 2020-03-26 | 2024-06-04 | Fdk株式会社 | Positive electrode for alkaline secondary battery and alkaline secondary battery |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4089402A (en) * | 1976-07-01 | 1978-05-16 | Hy Grip Products Co. | Sheet feeding mechanism for an automatic typewriter |
| JPS5332048A (en) * | 1976-09-07 | 1978-03-25 | Canon Inc | Information mark display device |
| JPS5462A (en) * | 1976-12-02 | 1979-01-05 | Sumitomo Chem Co Ltd | Production of resin sheet |
| JPS604149B2 (en) * | 1977-06-10 | 1985-02-01 | 電気化学工業株式会社 | Dry spray method |
| JPS5499944A (en) * | 1978-01-25 | 1979-08-07 | Asahi Dow Ltd | Nickel pole for alkaline cell |
| JPS6040667B2 (en) * | 1978-01-27 | 1985-09-12 | 松下電器産業株式会社 | Manufacturing method of nickel electrode |
| JPS5613481A (en) * | 1979-07-13 | 1981-02-09 | Toshiba Corp | Etching apparatus |
| JPS56143671A (en) * | 1980-04-09 | 1981-11-09 | Sanyo Electric Co Ltd | Manufacture of positive active material for alkaline storage battery |
-
1983
- 1983-12-20 JP JP58240140A patent/JPS60131765A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1890350A2 (en) | 1997-02-03 | 2008-02-20 | Matsushita Electric Industrial Co., Ltd. | The manufacturing method of active materials for the positive electrode in alkaline storage batteries |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60131765A (en) | 1985-07-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0480513B2 (en) | ||
| CN103531850A (en) | Electrolyte of lead-acid storage battery | |
| JP3032421B2 (en) | Manufacturing method of nickel positive electrode for batteries | |
| CN107516728B (en) | Coated nickel hydroxide powder for positive electrode active material of alkaline secondary battery | |
| JP3077473B2 (en) | Alkaline storage battery | |
| JPS60131766A (en) | Positive plate for alkaline battery | |
| JP2529330B2 (en) | Manufacturing method of nickel electrode for alkaline battery | |
| US1215907A (en) | Paste for storage-battery plates. | |
| JPH02253557A (en) | Manufacture of hydrogen storage battery | |
| JPS57194458A (en) | Manufacture of nickel electrode for alkaline storage battery | |
| JPS6316556A (en) | Manufacturing method for non-sintered electrodes | |
| JP2983647B2 (en) | Method for producing non-sintered positive electrode for alkaline storage battery | |
| HK1046988B (en) | Mixture, comprising metal and/or alloy particles and a liquid medium and a method for producing the same | |
| JPS60170167A (en) | Manufacturing method for alkaline cell electrode | |
| JPH0366780B2 (en) | ||
| JPS5981866A (en) | Manufacture of positive nickel plate for battery | |
| JPH035023B2 (en) | ||
| JPS6157397B2 (en) | ||
| JPS6316555A (en) | Manufacture of non-sintered type electrode | |
| JPH04296453A (en) | Nickel sintered substrate for alkaline secondary battery | |
| JPH01143144A (en) | Manufacture of electrode plate for lead storage battery | |
| JPH10270017A (en) | Positive electrode plate for non-aqueous electrolyte battery and non-aqueous electrolyte battery provided therewith | |
| JPS6038473B2 (en) | Manufacturing method for electrodes for water electrolysis | |
| JPS62256367A (en) | Nickel electrode for alkaline battery | |
| JPS63164163A (en) | Nickel positive electrode for alkaline storage batteries |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |