JPH0217910B2 - - Google Patents
Info
- Publication number
- JPH0217910B2 JPH0217910B2 JP56112435A JP11243581A JPH0217910B2 JP H0217910 B2 JPH0217910 B2 JP H0217910B2 JP 56112435 A JP56112435 A JP 56112435A JP 11243581 A JP11243581 A JP 11243581A JP H0217910 B2 JPH0217910 B2 JP H0217910B2
- Authority
- JP
- Japan
- Prior art keywords
- cadmium
- paste
- weight
- amount
- parts
- 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
- H01M4/04—Processes of manufacture in general
- H01M4/0438—Processes of manufacture in general by electrochemical processing
- H01M4/044—Activating, forming or electrochemical attack of the supporting material
- H01M4/0445—Forming after manufacture of the electrode, e.g. first charge, cycling
-
- 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
- H01M4/246—Cadmium 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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
-
- 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
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
- H01M4/72—Grids
- H01M4/74—Meshes or woven material; Expanded metal
- H01M4/742—Meshes or woven material; Expanded metal perforated material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/52—Removing gases inside the secondary cell, e.g. by absorption
- H01M10/526—Removing gases inside the secondary cell, e.g. by absorption by gas recombination on the electrode surface or by structuring the electrode surface to improve gas recombination
-
- 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
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/027—Negative 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
- H01M4/043—Processes of manufacture in general involving compressing or compaction
-
- 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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/669—Steels
-
- 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)
- Composite Materials (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
本発明はカドミウム負極の製造法に係り、高率
放電特性、サイクル寿命特性、ガス吸収特性など
の電池性能の改善を図ることを目的とする。
カドミウム負極の製造法には大別すると、焼結
式、プレス式、ペースト式の3種類がある。焼結
式はニツケル粉末を焼結して得た多孔性焼結基板
の細孔中に活物質を充填したもので、高率放電特
性にすぐれるが、製造工程が煩雑であるため高価
になるという欠点を有する。プレス式は活物質粉
末に導電剤を混合したのち、所定形状にプレス成
形したもので、安価につくれるという長所はある
が、高率放電特性およびサイクル寿命特性に劣る
という欠点を有する。ペースト式は高率放電特性
が焼結式に近く、かつ安価につくれるとして近年
注目されているもので、活物質粉末を主体とする
混合粉末材料に結着剤溶液を加え、混練してペー
スト状となし、このペーストを多孔性芯金の両面
に塗着するものである。このペーストの組成とし
て従来より一般的に行なわれているものは、酸化
カドミウム、導電剤としてニツケル粉末、更に補
強剤として合成樹脂製短繊維などを混合し、これ
に結着剤溶液を加えている。この補強剤としての
短繊維は芯金の孔部を通じて芯金の両面に連結
し、かつ活物質粉末相互間に存在するため、活物
質の芯金からの剥離を防止でき、電極としての機
械的強度を高めるうえで有効である。一方、この
ペースト式電極の活物質利用率を向上させる努力
が近年なされている。従来、ペースト式カドミウ
ム負極の活物質利用率は60〜70%程度であるが、
この利用率向上のために既にペースト塗着後の未
化成極板にカドミウムめつきを行なうことが提案
されている。このカドミウムめつきによる利用率
の向上はたしかに認められるが、サイクル寿命特
性やガス吸収特性の向上は確認されず、課題が残
されていた。
本発明は従来のペースト式電極の製造法の改良
に係り、ペースト塗着乾燥後の未化成極板にカド
ミウムめつきを行なう方法での組成改良であり、
サイクル寿命特性やガス吸収特性の向上を図つた
ものである。以下実施例をもつて説明する。
酸化カドミウム100重量部に炭素粉末として、
例えば黒鉛粉末2重量部を加えて混合粉末とし、
これに塩化ビニル樹脂とアクリル酸樹脂との共重
合物からなる合成樹脂製短繊維を0.5重量部加え
る。次に結着剤であるポリビニルアルコールを1
g溶解した30c.c.のエチレングリコール溶液を加え
て混練し、ペーストを作製する。このペーストを
厚さ0.8mmのニツケルめつき穿孔鋼板の両面に塗
着し、次に乾燥してエチレングリコールを逸散さ
せたのち、加圧により多孔度を40〜65%に調節し
て未化成極板とする。次にこの未化成極板を硫酸
カドミウム溶液中でカドミウムを対極として電解
還元し、金属カドミウムを電着させる。この電着
カドミウム量は未化成極板中の酸化カドミウムの
電気量の20〜55%の電気量とする。この電解還元
後に水洗、乾燥し、必要に応じてさらにプレス
し、完成極板とする。この完成極板を所定の寸法
に切断して単位極板Aとする。
比較のために、従来の電極を2種類作製した。
従来品Bは前記実施例とは導電剤が異るもので、
導電剤としてニツケル粉を用いたもので、その他
は実施例と同じものである。従来品cは導電剤に
炭素粉を使用し、未化成極板をアルカリ電解液中
で酸化カドミウムの一部をカドミウムに電解還元
したものである。この2種の従来品と、本発明品
Aとについて活物質利用率を比較測定をした。こ
の場合、電極中の総カドミウム量はA、B、Cと
も同一であり、かつ完成極板時点での総カドミウ
ム分のうち金属カドミウム量も同一量に調整して
測定した。利用率の測定は濃度30%のか性カリ水
溶液中で100%充電した後、各放電率にて放電し
た放電容量から算出した。その結果を下表に示
す。
The present invention relates to a method for manufacturing a cadmium negative electrode, and aims to improve battery performance such as high rate discharge characteristics, cycle life characteristics, and gas absorption characteristics. There are three types of manufacturing methods for cadmium negative electrodes: sintering method, press method, and paste method. The sintered type is made by sintering nickel powder and filling the pores of a porous sintered substrate with active material, which has excellent high-rate discharge characteristics, but is expensive due to the complicated manufacturing process. It has the following drawback. The press type mixes the active material powder with a conductive agent and then press-forms it into a predetermined shape, and has the advantage of being inexpensive to manufacture, but has the disadvantage of poor high rate discharge characteristics and cycle life characteristics. The paste type has attracted attention in recent years as it has high rate discharge characteristics close to that of the sintered type and can be produced at low cost.The paste type is made by adding a binder solution to a mixed powder material consisting mainly of active material powder and kneading it to form a paste. This paste is applied to both sides of the porous metal core. The conventional composition of this paste is to mix cadmium oxide, nickel powder as a conductive agent, and short synthetic resin fibers as a reinforcing agent, and add a binder solution to this mixture. . The short fibers as a reinforcing agent are connected to both sides of the core metal through the holes in the core metal, and are present between the active material powders, so they can prevent the active material from peeling off from the core metal, and can be used mechanically as an electrode. It is effective in increasing strength. On the other hand, efforts have been made in recent years to improve the active material utilization rate of this paste type electrode. Conventionally, the active material utilization rate of paste-type cadmium negative electrodes is around 60 to 70%.
In order to improve this utilization rate, it has already been proposed to plate the unformed electrode plate with cadmium after applying the paste. Although an improvement in the utilization rate due to this cadmium plating was certainly observed, no improvement in cycle life characteristics or gas absorption characteristics was confirmed, and issues remained. The present invention relates to an improvement of the conventional method of manufacturing paste-type electrodes, and is a composition improvement in a method of plating cadmium on an unformed electrode plate after applying a paste and drying it.
This is intended to improve cycle life characteristics and gas absorption characteristics. This will be explained below using examples. 100 parts by weight of cadmium oxide as carbon powder,
For example, add 2 parts by weight of graphite powder to make a mixed powder,
To this is added 0.5 part by weight of synthetic resin short fibers made of a copolymer of vinyl chloride resin and acrylic acid resin. Next, add 1 portion of polyvinyl alcohol as a binder.
Add 30 c.c. of dissolved ethylene glycol solution and knead to make a paste. This paste was applied to both sides of a nickel-plated perforated steel plate with a thickness of 0.8 mm, then dried to dissipate the ethylene glycol, and the porosity was adjusted to 40-65% by pressure to form an unformed Use it as a pole plate. Next, this unformed electrode plate is electrolytically reduced in a cadmium sulfate solution using cadmium as a counter electrode to electrodeposit metal cadmium. The amount of electrodeposited cadmium is 20 to 55% of the amount of electricity of cadmium oxide in the unformed electrode plate. After this electrolytic reduction, it is washed with water, dried, and further pressed if necessary to obtain a completed electrode plate. This completed electrode plate is cut into a predetermined size to form a unit electrode plate A. For comparison, two types of conventional electrodes were fabricated.
Conventional product B has a different conductive agent from the above example,
Nickel powder was used as a conductive agent, and the rest was the same as in the example. Conventional product c uses carbon powder as a conductive agent and electrolytically reduces a portion of cadmium oxide to cadmium in an unformed electrode plate in an alkaline electrolyte. The active material utilization rates of these two conventional products and product A of the present invention were compared and measured. In this case, the total amount of cadmium in the electrodes A, B, and C was the same, and the amount of metallic cadmium among the total cadmium at the time of the completed electrode plate was also adjusted to the same amount for measurement. The utilization rate was calculated from the discharge capacity discharged at each discharge rate after 100% charging in a caustic potassium aqueous solution with a concentration of 30%. The results are shown in the table below.
【表】
上表から明らかなように発明品Aは従来品Bと
同程度の活物質利用率がみられる。
次に上述の単位極板を用い、焼結式正極と、ポ
リアミド樹脂製不織布からなるセパレータとを組
合わせて、公称容量500mAhの密閉形ニツケルカ
ドミウム蓄電池を作製した。いずれの電池も前記
活物質利用率測定と同じ負極を用いており、本発
明品はA、従来品はB、Cの2種である。この電
池を使用して高率放電特性、サイクル寿命特性、
ガス吸収特性について試験を行なつた。第1図は
高率放電特性で、本発明品Aは従来品Bと同等か
若干優れており、Cとは明らかに差異がみとめら
れる。第2図はサイクル寿命特性である。寿命試
験条件は常温にて充電を1/2C(250mA)で3時
間、放電を1C(500mA)で1.0V迄の充放電のく
り返しとした。
この結果、本発明品Aは1500回迄殆んど容量低
下がみられないのに対し、従来品B、Cでは徐々
に容量低下の傾向がみられ、明らかに本発明品A
のサイクル寿命特性が良好なことがわかる。第3
図は、ガス吸収性能の比較である。この密閉形ニ
ツケル・カドミウム蓄電池においては過充電時に
正極から酸素ガスが発生し、この酸素ガスを負極
のカドミウムにて吸収させることによつて密閉化
がなされており、このガス吸収能力が大きい程、
充電率を大きくすることが可能となり急速充電が
できる。そこで一般にガス吸収性能がきびしくな
る低温で特性を調べた。すなわち、充電は0℃
で、各充電率0.25、0.5、0.75、1Cで行ない、その
時の電池内圧力を測定した。第3図から明らかな
ように、本発明品Aは従来品B、Cにくらべて圧
力値が低く、ガス吸収能力が大きいことを示して
いる。
以上のように本発明品は高率放電特性、サイク
ル寿命特性、ガス吸収性能において従来品よりも
すぐれているが、その理由として次のことが考え
られる。すなわち、本発明品は負極ペースト中に
導電剤として炭素粉末を使用し、ペースト塗着乾
燥後の未化成極板にカドミウムを電着させている
が、この電着カドミウムは炭素粉末の表面のみな
らず、補強剤として添加されている合成樹脂製短
繊維表面にも析出している。すなわち、短繊維表
面には炭素粉が点在しており、この炭素粉を核と
してカドミウムの析出が生じ、比較的多くの電着
カドミウムが繊維表面に存在している。これは従
来品Bのように導電剤としてニツケル粉を使用し
た場合とくらべると明らかに相違しており、ニツ
ケル粉の場合は短繊維表面上にはニツケル粉の存
在は殆んどみられず、従つて繊維表面上へのカド
ミウムの析出はみられない。次に炭素粉末と合成
樹脂短繊維との組成比率について検討した。その
結果、酸化カドミウム100重量部に対し、炭素粉
末0.3〜6重量部、合成樹脂製短繊維0.1〜2重量
部の組成をベースにペーストを作製し、ペースト
塗着、乾燥後に電解還元によつてカドミウムを電
着させると、前記のような本発明の効果が得られ
た。なお、カドミウムの電着量は酸化カドミウム
量に対し、電気量として少くとも20%あれば効果
のあることがわかつた。また、炭素粉末は0.3重
量部より少量の場合、短繊維表面への付着が少な
くてカドミウムの析出が極めて少量となり効果が
乏しくなる。一方6重量部よりも多量となると酸
化カドミウム量の充填密度が減少し、活物質量の
少ない電極となるため好ましくない。また、短繊
維については0.1重量部よりも少量では繊維量と
して少ないため、繊維上の電着カドミウムの絶対
量が少なくなつて本発明の効果が薄れてくる。一
方短繊維量が2重量部を越えると短繊維間同士の
からみが強くなつてペースト中に均一に分散され
にくくなり均一な電極となりにくい。
本発明の効果は前述のごとく、好ましい量配合
し、ペースト中に均一分散させた短繊維上に付着
した炭素粉末の表面を核としてカドミウムの電着
が比較的多く生じるので、多孔性芯金の孔部を通
じて電極の表裏両面にまたがつて繊維の導電ネツ
トワークが形成され、この繊維上の電着カドミウ
ムの存在によつて、高率放電特性、サイクル寿命
特性、ガス吸収性能等の電池性能を向上させた負
極が得られるものである。[Table] As is clear from the above table, invention product A has an active material utilization rate comparable to that of conventional product B. Next, using the unit electrode plates described above, a sealed nickel-cadmium storage battery with a nominal capacity of 500 mAh was manufactured by combining a sintered positive electrode and a separator made of a nonwoven fabric made of polyamide resin. Both batteries used the same negative electrode as in the measurement of the active material utilization rate, and the present invention was of type A, and the conventional products were of two types, B and C. Using this battery, high rate discharge characteristics, cycle life characteristics,
Tests were conducted on gas absorption properties. FIG. 1 shows high rate discharge characteristics, and product A of the present invention is equivalent to or slightly superior to conventional product B, and clearly different from product C. Figure 2 shows the cycle life characteristics. The life test conditions were charging at 1/2C (250mA) for 3 hours at room temperature, and discharging at 1C (500mA) to 1.0V. As a result, inventive product A shows almost no capacity decrease until 1500 cycles, whereas conventional products B and C tend to gradually decrease in capacity, clearly inventive product A.
It can be seen that the cycle life characteristics are good. Third
The figure shows a comparison of gas absorption performance. In this sealed nickel-cadmium storage battery, oxygen gas is generated from the positive electrode during overcharging, and the sealing is achieved by absorbing this oxygen gas with the cadmium of the negative electrode.The greater the gas absorption capacity, the more
It is possible to increase the charging rate and enable rapid charging. Therefore, we investigated the properties at low temperatures, where gas absorption performance is generally severe. In other words, charging is at 0℃
The battery was charged at various charging rates of 0.25, 0.5, 0.75, and 1C, and the pressure inside the battery was measured at each charging rate. As is clear from FIG. 3, product A of the present invention has a lower pressure value than conventional products B and C, indicating that it has a greater gas absorption capacity. As described above, the product of the present invention is superior to conventional products in high rate discharge characteristics, cycle life characteristics, and gas absorption performance, and the following may be the reason for this. In other words, the product of the present invention uses carbon powder as a conductive agent in the negative electrode paste, and cadmium is electrodeposited on the unformed electrode plate after the paste has been applied and dried. Moreover, it is also deposited on the surface of short synthetic resin fibers added as reinforcing agents. That is, carbon powder is scattered on the surface of the short fibers, and cadmium is precipitated using the carbon powder as nuclei, so that a relatively large amount of electrodeposited cadmium is present on the fiber surface. This is clearly different from the case where nickel powder is used as a conductive agent as in conventional product B. In the case of nickel powder, the presence of nickel powder is hardly seen on the surface of the short fibers, Therefore, no precipitation of cadmium on the fiber surface is observed. Next, the composition ratio of carbon powder and short synthetic resin fibers was investigated. As a result, a paste was prepared based on the composition of 100 parts by weight of cadmium oxide, 0.3 to 6 parts by weight of carbon powder, and 0.1 to 2 parts by weight of short synthetic resin fibers. When cadmium was electrodeposited, the effects of the present invention as described above were obtained. It has been found that it is effective if the amount of cadmium electrodeposited is at least 20% of the amount of cadmium oxide. Furthermore, if the amount of carbon powder is less than 0.3 parts by weight, less adhesion to the surface of the short fibers results in very little cadmium being precipitated and the effect is poor. On the other hand, if the amount is more than 6 parts by weight, the packing density of cadmium oxide decreases, resulting in an electrode with a small amount of active material, which is not preferable. Furthermore, if the amount of short fibers is less than 0.1 part by weight, the amount of fibers will be small, and the absolute amount of electrodeposited cadmium on the fibers will decrease, reducing the effect of the present invention. On the other hand, if the amount of short fibers exceeds 2 parts by weight, the entanglement between the short fibers becomes strong and it becomes difficult to disperse them uniformly in the paste, making it difficult to form a uniform electrode. As mentioned above, the effect of the present invention is that a relatively large amount of cadmium is electrodeposited on the surface of the carbon powder adhered to the short fibers which are blended in a preferable amount and uniformly dispersed in the paste. A conductive network of fibers is formed across the front and back surfaces of the electrode through the holes, and the presence of electrodeposited cadmium on these fibers improves battery performance such as high rate discharge characteristics, cycle life characteristics, and gas absorption performance. An improved negative electrode can be obtained.
第1図は本発明によるカドミウム負極の放電率
特性を示す図、第2図はサイクル寿命特性を示す
図、第3図はガス吸収特性を示す。
Aは本発明品、B,Cは従来品。
FIG. 1 shows the discharge rate characteristics of the cadmium negative electrode according to the present invention, FIG. 2 shows the cycle life characteristics, and FIG. 3 shows the gas absorption characteristics. A is a product of the present invention, B and C are conventional products.
Claims (1)
0.3〜6重量部、合成樹脂製短繊維0.1〜2重量部
を配合した混合粉末に結着剤溶液を加えてペース
ト状となし、該ペーストを多孔性芯金の両面に塗
着、乾燥したのち、電解によりカドミウムを電着
させてなることを特徴とするカドミウム負極の製
造法。1 Carbon powder for 100 parts by weight of cadmium oxide
A binder solution is added to a mixed powder containing 0.3 to 6 parts by weight and 0.1 to 2 parts by weight of short synthetic resin fibers to form a paste, and the paste is applied to both sides of the porous core and dried. , a method for producing a cadmium negative electrode characterized by electrodepositing cadmium by electrolysis.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56112435A JPS5814465A (en) | 1981-07-17 | 1981-07-17 | Manufacture of cadmium negative electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56112435A JPS5814465A (en) | 1981-07-17 | 1981-07-17 | Manufacture of cadmium negative electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5814465A JPS5814465A (en) | 1983-01-27 |
| JPH0217910B2 true JPH0217910B2 (en) | 1990-04-23 |
Family
ID=14586556
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56112435A Granted JPS5814465A (en) | 1981-07-17 | 1981-07-17 | Manufacture of cadmium negative electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5814465A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60218773A (en) * | 1984-04-12 | 1985-11-01 | Sanyo Electric Co Ltd | Sealed alkaline storage battery |
| JP4797459B2 (en) * | 2005-06-23 | 2011-10-19 | パナソニック株式会社 | Electrode plate and battery manufacturing method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54139031A (en) * | 1978-04-20 | 1979-10-29 | Matsushita Electric Industrial Co Ltd | Method of producing cadmium cathods plate for alkaline storage battery |
| JPS5678072A (en) * | 1979-11-30 | 1981-06-26 | Sanyo Electric Co Ltd | Positive plate for alkaline storage battery |
-
1981
- 1981-07-17 JP JP56112435A patent/JPS5814465A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5814465A (en) | 1983-01-27 |
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