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JPS608585B2 - Manufacturing method for alkaline storage battery sintered electrodes - Google Patents
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JPS608585B2 - Manufacturing method for alkaline storage battery sintered electrodes - Google Patents

Manufacturing method for alkaline storage battery sintered electrodes

Info

Publication number
JPS608585B2
JPS608585B2 JP50126514A JP12651475A JPS608585B2 JP S608585 B2 JPS608585 B2 JP S608585B2 JP 50126514 A JP50126514 A JP 50126514A JP 12651475 A JP12651475 A JP 12651475A JP S608585 B2 JPS608585 B2 JP S608585B2
Authority
JP
Japan
Prior art keywords
substrate
impregnation
active material
salt
salts
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
Application number
JP50126514A
Other languages
Japanese (ja)
Other versions
JPS5249431A (en
Inventor
広志 米村
茂 山下
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP50126514A priority Critical patent/JPS608585B2/en
Publication of JPS5249431A publication Critical patent/JPS5249431A/en
Publication of JPS608585B2 publication Critical patent/JPS608585B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 本発明はアルカリ蓄電池用特にニッケル‘カドミウム蓄
電池用競綾式電極の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing competitively woven electrodes for alkaline storage batteries, particularly for nickel-cadmium storage batteries.

一般にこの種の焼結電極は見頚比重の小さいニッケル粉
末を増粘剤及び水と混合し、この混合物をニッケル又は
ニッケルメッキした金網或いはパンチングメタル等の芯
体に塗布したる後、還元雰囲気中において800〜10
00q0に加熱し増粘剤及び水を分解して多孔性ニッケ
ル暁結基板となし、この基板多孔部に夫々規定量の陰・
陽活物質を含浸せしめて陰・陽電極板となすものである
。この含浸工程においては含浸液としての陰・陽活物質
の塩類(陰極側はカドミウム塩、陽極側はニッケル塩)
例えば硝酸塩、硫酸塩塩化物の水溶液を暁緒基板に含浸
せしめ、次にアルカリ洛中で化学置換、電解或いは熱分
解により上記塩類を活物質たる水酸化物に転化しトこれ
を水洗4乾燥するという含浸工程を数回線返して規定量
の活物質を得るものである。上記含浸工程においてはい
ずれも基板表面に活物質の層即ち陰極側では水酸化カド
ミウム、陽極側では水酸化ニッケル等の水酸化物が沈着
する。
Generally, this type of sintered electrode is made by mixing nickel powder with a small specific gravity with a thickener and water, applying this mixture to a core of nickel or nickel-plated wire mesh, punched metal, etc., and then placing it in a reducing atmosphere. 800-10 in
The thickener and water are heated to 00q0 to decompose the thickener and water to form a porous nickel composite substrate, and the porous portions of this substrate are filled with specified amounts of shadow and water.
It is impregnated with a positive active material to form negative and positive electrode plates. In this impregnation process, salts of negative and positive active materials are used as impregnating liquid (cadmium salt on the cathode side, nickel salt on the anode side).
For example, an impregnation method involves impregnating a chloride substrate with an aqueous solution of nitrates, sulfates, and chlorides, then converting the salts into hydroxides as active materials by chemical substitution, electrolysis, or thermal decomposition in an alkali solution, and then washing and drying the salts with water. The process is repeated several times to obtain a specified amount of active material. In all of the above impregnation steps, a layer of active material is deposited on the substrate surface, that is, a hydroxide such as cadmium hydroxide on the cathode side and nickel hydroxide on the anode side.

この沈着物は多孔性基板の孔部をふさぐと共にこれらは
不落性であるため次の水洗にも除去されずに残り、その
ため次回の含浸工程では含浸量のバラツキを生じる原因
となる。更に、この基板表面に沈着した活物質が電池の
充電時または保在中に電極より脱落し電解溶液中に縁動
して自己放電を生じる原因ともなる。
These deposits block the pores of the porous substrate, and since they are non-falling, they remain unremoved even in the next washing with water, which causes variations in the amount of impregnation in the next impregnation step. Furthermore, the active material deposited on the surface of the substrate falls off from the electrodes during charging or storage of the battery and moves into the electrolytic solution, causing self-discharge.

そこで、これらの欠点を除くために従来上記含浸工程に
おいて化学置換等により水酸化物となしたものを水洗す
る際にブラッシングを行なって基板表面の沈着物を刷子
等により除去する方法が探られている。しかしながら、
この方法によれば各水洗時に一々ブラッシングを行うた
めに工数がかかり、含浸工程が繁雑となると共に電極表
面に傷をつけるばかりでなく基板多孔部の活物質までも
除去する懸念がある。
Therefore, in order to eliminate these drawbacks, a method has been explored in which the deposits on the substrate surface are removed with a brush or the like by brushing when washing the hydroxide formed by chemical substitution etc. in the above impregnation process with water. There is. however,
According to this method, it takes a lot of man-hours to perform brushing each time the electrode is washed with water, making the impregnation process complicated, and there is a concern that not only the electrode surface will be damaged but also the active material in the porous portions of the substrate will be removed.

又、他の方法として特公昭39−14323号公報に示
されているように含浸液より取出した暁結基板を直ちに
水中或いは流水中に1〜2秒間浸潰し、この瞬間的な水
中浸債により基板表面の沈着物を除去する方法が提案さ
れているが実際生産上において浸糟時間を瞬間的(1〜
2秒間)に均一に保つことは困難であり、又長時間浸債
すると基板多孔部の塩類をも溶解除去することになりバ
ラッキを生じると共に含浸量の減少をきたすことになる
Alternatively, as shown in Japanese Patent Publication No. 39-14323, the substrate taken out from the impregnating liquid is immediately immersed in water or running water for 1 to 2 seconds, and this instantaneous immersion in water causes A method has been proposed to remove deposits on the substrate surface, but in actual production, the immersion time is instantaneous (1 to 10 minutes).
It is difficult to maintain uniformity for 2 seconds), and if soaked for a long time, salts in the porous parts of the substrate will also be dissolved and removed, resulting in unevenness and a decrease in the amount of impregnation.

本発明は斯る点に鑑みなされたものであり、その要旨と
するところは活物質塩を含浸せる基板を水中に浸債する
代わりもと含浸液と同一組成を有するが含浸液に比して
低濃度の塩溶液中に浸債せしめる点にあり、この操作に
よって濃度差による拡散により基板表面に付着せる塩類
の濃度を低減せしめて基板表面よりの離脱を容易となし
て除去するものでありも基板表面の沈着物除去に要する
時間を数十秒に保ち均一な浸簿時間及び除去ができ実用
可能ならしめるものである。
The present invention has been made in view of these points, and its gist is that instead of immersing a substrate impregnated with an active material salt in water, a substrate having the same composition as the original impregnating liquid, but with a lower concentration than the original impregnating liquid. The method involves immersing the bond in a low-concentration salt solution, and through this operation, the concentration of salts adhering to the substrate surface is reduced by diffusion due to the concentration difference, making it easier to remove from the substrate surface. The time required to remove deposits from the substrate surface can be kept to several tens of seconds, and uniform immersion time and removal can be achieved, making it practical.

即ち「本発明はニッケル微粉末を焼結してなる多孔性焼
結基板に竜池活物質の塩類(陰極側にはカドミウム塩「
陽極側にはニッケル塩)を含浸したる後「 この基板を
上記含浸液と同一組成を有するが含浸液に比して低濃度
の塩溶液中に数十秒嬢潰して〜 これら濃度差による拡
散により基板表面に付着せる塩類の濃度を低減せしめて
基板表面より除去し、しかる後アルカリ裕中において化
学置換、電解或いは熱分解により基板多孔部の塩類を水
酸化物に転化することを特徴とするアルカリ蓄電池用の
陰陽各焼結電極の製造法に在る。
That is, ``the present invention is a porous sintered substrate made by sintering fine nickel powder, and salts of Tatsuike active material (cadmium salt on the cathode side).
After impregnating the anode side with nickel salt), the substrate was placed in a salt solution having the same composition as the above impregnating solution but at a lower concentration than the impregnating solution for several tens of seconds.Diffusion due to these concentration differences occurred. It is characterized by reducing the concentration of salts adhering to the substrate surface and removing them from the substrate surface, and then converting the salts in the porous parts of the substrate into hydroxides by chemical substitution, electrolysis, or thermal decomposition in an alkaline bath. A method for manufacturing Yin and Yang sintered electrodes for alkaline storage batteries.

ここで含浸塩溶液の拡散速度は含浸塩溶液と浸溝塩溶液
との濃度差により決定されるものであり「例えば含浸塩
溶液が比重1.7の硝酸ニッケルの場合には適当な浸債
時間の確保、親定含浸回数で所望含浸量の確保、利用率
の維持、含浸量のバラッキを生じず基板表面の沈着物の
溶解・洗浄除去の各点から検討して浸贋塩溶液は比重革
Here, the diffusion rate of the impregnating salt solution is determined by the concentration difference between the impregnating salt solution and the immersing salt solution. The specific gravity of the impregnated salt solution was determined by considering the following points: ensuring the desired amount of impregnation with a fixed number of impregnations, maintaining the utilization rate, and dissolving and cleaning deposits on the substrate surface without causing variations in the amount of impregnation. .

30〜1.50の硝酸ニッケルが適当である。30-1.50 nickel nitrate is suitable.

尚、上記浸贋塩溶液である硝酸ニッケルの比重が1.3
0以下であると拡散速度が早く浸濃時間は短く限定され
るため均一性を得ることが困難であると共に利用率の低
下をきたす。
In addition, the specific gravity of nickel nitrate, which is the above imitation salt solution, is 1.3.
If it is less than 0, the diffusion rate is fast and the immersion time is limited to a short time, making it difficult to obtain uniformity and lowering the utilization rate.

又比重1.50以上の場合には拡散速度が遅くなり「充
分な浸債時間、含浸量及び利用率の確保は出来るが基板
表面に在する沈着物の熔解・洗浄効果は減少し沈着物除
去が不充分となる。次に本発明の一実施例を示せばニッ
ケル微粉末を焼結してなる65×41×0.6(肋)の
多孔性焼結基板を温度70oo〜8000「比重1.7
0〜1.74の硝酸ニッケルに2時間浸潰して活物質海
を含浸したる後、室温、比重1.40の硝酸ニッケルに
3現砂間浸潰し、ついで中間乾燥「アルカリ処理(化学
層襖入水洗「乾燥の一連の工程を3〜4回行い基板中に
規定量の活物質(水酸化ニッケル)を充填して陽極板と
なす。
In addition, if the specific gravity is 1.50 or more, the diffusion rate becomes slow, and although sufficient soaking time, impregnation amount, and utilization rate can be ensured, the effect of melting and cleaning deposits on the substrate surface decreases, making it difficult to remove deposits. Next, in an embodiment of the present invention, a porous sintered substrate of 65 x 41 x 0.6 (ribs) made by sintering fine nickel powder is heated at a temperature of 70 oo to 8000 with a specific gravity of 1. .7
After soaking in nickel nitrate with a specific gravity of 0 to 1.74 for 2 hours to impregnate the active material sea, it was soaked in nickel nitrate with a specific gravity of 1.40 at room temperature for 3 hours, and then subjected to intermediate drying ``alkali treatment (chemical layer fusuma). A series of steps including water washing and drying is performed 3 to 4 times, and a specified amount of active material (nickel hydroxide) is filled into the substrate to form an anode plate.

陰極板の場合も含浸塩として硝酸カドミウムを利用し浸
債塩として含浸塩より低濃度の硝酸カドミウムを用いて
同機の操作を行えばよい。下表は陽極板の製造に際して
基板表面の塩類を除去する手段として本発明法と従来法
(水を利用)とを適用した場合の各値を比較して示すも
のであり、第1表は浸債液と浸債時間による含浸量の比
較し第2表は浸債液のみを代え他は同一条件下で測定し
た場合の含浸量バラッキ及び利用率を比較したものであ
る。
In the case of the cathode plate as well, cadmium nitrate may be used as the impregnating salt, and the same operation may be performed using cadmium nitrate having a lower concentration than the impregnating salt as the bonding salt. The table below compares each value when the method of the present invention and the conventional method (using water) are applied as a means for removing salts from the substrate surface during the manufacture of anode plates. Table 2 compares the amount of impregnation depending on the bond solution and soaking time. Table 2 compares the variation in the amount of impregnation and the utilization rate when measurements were made under the same conditions except for the soaking solution.

第1表 第2表 上記表より明らかなように本発明法を適用すれば従来法
(水を利用)に比して浸債時間を実用可能な程度に十分
確保できると共に含浸量のバラツキも極めて4・ごく且
利用率も低下することはない。
As is clear from Table 1, Table 2, and the above table, by applying the method of the present invention, compared to the conventional method (using water), it is possible to secure a sufficient soaking time to a practical extent, and the variation in the amount of impregnation is also extremely small. 4. The usage rate will not decline.

この理由は従来法によれば基板多孔部に含浸されたもの
までが洗い流される懸念があるので浸債時間を短かくす
る必要があるためであり「且周知のようにこの種電極に
おいては基板多孔部に含浸された含浸量と、含浸液によ
る基板の腐蝕量との和が活物質となるものであり、従来
法のように基板多孔部内の含浸塩が洗い流される場合に
は含浸量に加えて腐蝕量までが低減しその結果として前
述の第2表で明確なるように利用率も悪い。又極板表面
状態も水中に浸燈したものと大差がなかった。尚、本願
とは逆に基板多孔部に先づ低濃度の活物質塩を合浸し、
ついで高濃度の活物質塩を含浸させることにより一回の
含浸工程時の含嬢量を増大させることを目的とする製法
が提案されているが「 この製法では先に含浸され基板
表面に付着せる低濃度の活物質塩は濃度が低減されず逆
に濃度が増大せしめられることになって基板表面よりの
除去は困難となるものである。
The reason for this is that with the conventional method, there is a concern that even the material impregnated into the porous parts of the substrate may be washed away, so it is necessary to shorten the soaking time. The active material is the sum of the amount of impregnation impregnated into the substrate and the amount of corrosion of the substrate by the impregnating liquid, and when the impregnated salt in the porous parts of the substrate is washed away as in the conventional method, in addition to the amount of impregnation. Even the amount of corrosion was reduced, and as a result, the utilization rate was poor as shown in Table 2 above.Also, the surface condition of the electrode plate was not much different from that of the electrode plate immersed in water.Contrary to the present application, the substrate First, a low concentration of active material salt is soaked in the porous part,
A manufacturing method has been proposed in which the active material salt is then impregnated with a high concentration of active material salt to increase the amount of impregnation in a single impregnation process. The active material salt at a low concentration does not reduce its concentration, but rather increases its concentration, making it difficult to remove it from the substrate surface.

上述した如く本発明によれば露池活物質の含浸工程にお
ける含浸量のバラッキを非常に小さくして規定量の活物
質を基板多孔部に規定舎浸回数で充填しうると共に基板
表面に存する付着物の除去操作に数十秒の時間が確保で
き、水中或いは流水中で瞬間的(1〜2秒間)に行う場
合に比し均一な浸濃時間と除去ができ実用可能な競結電
極の製造法を提供するものである。
As described above, according to the present invention, it is possible to significantly reduce the variation in the amount of impregnation in the step of impregnating the active material in a dew pond, to fill the porous portions of the substrate with a specified amount of the active material in a specified number of times, and to reduce the amount of impregnation present on the surface of the substrate. Manufacture of a practical competitively connected electrode that can secure several tens of seconds for kimono removal operation and achieve more uniform immersion time and removal compared to instantaneous (1 to 2 seconds) underwater or running water removal operation. It provides law.

Claims (1)

【特許請求の範囲】[Claims] 1 多孔性焼結基板に所定活物質の塩類を含浸したる後
、該含浸液と同一組成を有するが含浸液に比して低濃度
の塩溶液中に浸漬してこれら濃度差による拡散により前
記基板表面に付着せる塩類の濃度を低減せしめて基板表
面より除去し、ついで基板多孔部の塩類を水酸化物に転
化せしめることを特徴とするアルカリ蓄電池焼結電極の
製造法。
1. After a porous sintered substrate is impregnated with salts of a predetermined active material, it is immersed in a salt solution having the same composition as the impregnating solution but at a lower concentration than that of the impregnating solution. A method for producing a sintered electrode for an alkaline storage battery, which comprises reducing the concentration of salts adhering to the surface of a substrate, removing them from the surface of the substrate, and then converting the salts in the porous portions of the substrate into hydroxides.
JP50126514A 1975-10-17 1975-10-17 Manufacturing method for alkaline storage battery sintered electrodes Expired JPS608585B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50126514A JPS608585B2 (en) 1975-10-17 1975-10-17 Manufacturing method for alkaline storage battery sintered electrodes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50126514A JPS608585B2 (en) 1975-10-17 1975-10-17 Manufacturing method for alkaline storage battery sintered electrodes

Publications (2)

Publication Number Publication Date
JPS5249431A JPS5249431A (en) 1977-04-20
JPS608585B2 true JPS608585B2 (en) 1985-03-04

Family

ID=14937081

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50126514A Expired JPS608585B2 (en) 1975-10-17 1975-10-17 Manufacturing method for alkaline storage battery sintered electrodes

Country Status (1)

Country Link
JP (1) JPS608585B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61156774U (en) * 1985-03-20 1986-09-29

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61156774U (en) * 1985-03-20 1986-09-29

Also Published As

Publication number Publication date
JPS5249431A (en) 1977-04-20

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