JPH0517658B2 - - Google Patents
Info
- Publication number
- JPH0517658B2 JPH0517658B2 JP62026722A JP2672287A JPH0517658B2 JP H0517658 B2 JPH0517658 B2 JP H0517658B2 JP 62026722 A JP62026722 A JP 62026722A JP 2672287 A JP2672287 A JP 2672287A JP H0517658 B2 JPH0517658 B2 JP H0517658B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- cadmium
- sintered
- active material
- methylcellulose
- 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
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
- H01M4/80—Porous plates, e.g. sintered carriers
- H01M4/801—Sintered carriers
-
- 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
-
- 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
- H01M4/661—Metal or alloys, e.g. alloy coatings
-
- 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】
(イ) 産業上の利用分野
本発明はアルカリ蓄電池に用いられる焼結式カ
ドミウム電極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 sintered cadmium electrode used in alkaline storage batteries.
(ロ) 従来の技術
一般にアルカリ蓄電池に用いられる電極の製造
方法には、特開昭56−82573号公報に示されるよ
うに、活物質粉末に結着剤を加えて混練してペー
ストとし、このペーストを導電性基板などに塗
着、乾燥して製造する非焼結製法と、特開昭51−
18834号公報に示されるように、多孔性ニツケル
焼結基板に硝酸カドミウムなどの活物質の塩溶液
を含浸し、次いでアルカリ処理、水洗、乾燥する
活物質含浸工程を数回行なつて、所望量の活物質
を基板中に充填する焼結式製法がある。(B) Prior art Generally, as shown in Japanese Patent Application Laid-open No. 56-82573, the manufacturing method of electrodes used in alkaline storage batteries involves adding a binder to active material powder and kneading it into a paste. A non-sintering manufacturing method in which paste is applied to a conductive substrate and dried, and JP-A-51-
As shown in Japanese Patent No. 18834, a porous nickel sintered substrate is impregnated with a salt solution of an active material such as cadmium nitrate, and then an active material impregnation process of alkali treatment, water washing, and drying is performed several times to obtain the desired amount. There is a sintering method for filling active materials into a substrate.
前者の特開昭56−82573号公報に示される電極
はポリビニルアルコールを結着剤として用い、そ
の溶解を防止するために120〜220℃の温度で熱処
理しているが、この種非焼結式電極は結着剤で活
物質を固定するため、活物質粒子間に結着剤が存
在し、この結着剤が活物質粒子間及び活物質と導
電性基板の間の導電性を低下させるので、充分な
電極特性が得られるとは言えない。 The former electrode shown in JP-A-56-82573 uses polyvinyl alcohol as a binder and is heat-treated at a temperature of 120 to 220°C to prevent it from dissolving. Since electrodes use a binder to fix the active material, the binder exists between the active material particles, and this binder reduces the conductivity between the active material particles and between the active material and the conductive substrate. However, it cannot be said that sufficient electrode characteristics can be obtained.
これに対して後者の焼結式電極は、活物質が結
着剤などを介さず直接基板に接触しているため、
前述した非焼結式電極に於けるような導電性の低
下は無く、更に、電極内に多孔性ニツケル焼結基
板の導電性マトリツクスが存在するため、電極内
の導電性が高く、非焼結式電極に比較して優れた
電極特性を備えるものである。 In contrast, in the latter type of sintered electrode, the active material is in direct contact with the substrate without using a binder, etc.
There is no decrease in conductivity as in the non-sintered electrodes mentioned above, and furthermore, because the conductive matrix of the porous nickel sintered substrate exists within the electrode, the conductivity within the electrode is high, and the non-sintered It has superior electrode characteristics compared to formula electrodes.
ところが、この導電性の高い焼結式電極に於い
て、活物質として水酸化カドミウムや酸化カドミ
ウムなどのカドミウム活物質を用いた場合には、
充放電サイクルを重ねていくと、活物質が不活性
化し、放電不能の金属カドミウムの蓄積が生じ
て、極板容量が低下するという問題がある。これ
は導電性の高い焼結式電極に特有のものであり、
導電性の低い非焼結式電極では、前述した未放電
金属カドミウムの蓄積という現象が生じる以前に
他の要因、たとえば、活物質の脱落などによつて
サイクル寿命となつてしまう。また脱落を抑制す
るためこの種の非焼結式電極にメチルセルロース
を添加すればするほど、電極の導電性が低下し、
電極特性が悪くなる。 However, in this highly conductive sintered electrode, when a cadmium active material such as cadmium hydroxide or cadmium oxide is used as the active material,
As charge/discharge cycles are repeated, the active material becomes inactive and metal cadmium, which cannot be discharged, accumulates, resulting in a decrease in electrode plate capacity. This is unique to highly conductive sintered electrodes,
A non-sintered electrode with low conductivity reaches the end of its cycle life due to other factors, such as shedding of the active material, before the aforementioned phenomenon of accumulation of undischarged metal cadmium occurs. In addition, the more methylcellulose is added to this type of non-sintered electrode to suppress shedding, the more the conductivity of the electrode decreases.
Electrode characteristics deteriorate.
(ハ) 発明が解決しようとする問題点
本発明は充放電サイクルを重ねていくことによ
つて生じる焼結式カドミウム電極に於ける放電不
能な金属カドミウムの蓄積を抑え、電極容量の低
下を抑制して、サイクル特性に優れたアルカリ蓄
電池用焼結式カドミウム電極を提供しようとする
ものである。(c) Problems to be solved by the invention The present invention suppresses the accumulation of metal cadmium that cannot be discharged in a sintered cadmium electrode caused by repeated charge/discharge cycles, and suppresses a decrease in electrode capacity. The present invention aims to provide a sintered cadmium electrode for alkaline storage batteries with excellent cycle characteristics.
(ニ) 問題点を解決するための手段
本発明のアルカリ蓄電池用カドミウム電極は、
カドミウム活物質を充填したニツケル焼結基板の
内部に、多糖類またはその誘導体を添加したこと
を要旨とするものである。(d) Means for solving the problems The cadmium electrode for alkaline storage batteries of the present invention includes:
The gist is that a polysaccharide or a derivative thereof is added to the inside of a nickel sintered substrate filled with a cadmium active material.
(ホ) 作用
前述したように充放電サイクルを重ねていくと
焼結式カドミウム陰極の極板容量が低下するの
は、放電時に活物質である金属カドミウムの表面
に放電生成物の微細な水酸化カドミウム粒子の被
膜が形成されるようになり、この微細な水酸化カ
ドミウム粒子の被膜が内部に存在する金属カドミ
ウムと電解液との間の接触を妨げ、未放電の金属
カドミウムを残存させることになるためと考えら
れる。ここで、カドミウム活物質を充填したニツ
ケル焼結基板の内部に、多糖類またはその誘導体
を添加した構成、更に詳しくは多糖類またはその
誘導体によつて活物質表面を覆つた構成とするこ
とで、放電時に金属カドミウム上に析出する水酸
化カドミウムの生成核の発生数を抑制し、析出せ
る水酸化カドミウム粒子の微細化を防止する。し
たがつて、金属カドミウムの表面を多数の微細な
水酸化カドミウム粒子が覆い金属カドミウムと電
解液の接触が妨げられることに基づく放電不能な
金属カドミウムの生成、および蓄積を抑制しうる
ものである。(E) Effect As mentioned above, the plate capacity of a sintered cadmium cathode decreases as charge and discharge cycles are repeated due to fine hydroxylation of discharge products on the surface of the metal cadmium, which is the active material during discharge. A film of cadmium particles begins to form, and this film of fine cadmium hydroxide particles prevents contact between the metal cadmium present inside and the electrolyte, leaving undischarged metal cadmium. It is thought that this is because of this. Here, by adding a polysaccharide or a derivative thereof to the inside of a nickel sintered substrate filled with a cadmium active material, and more specifically, by covering the surface of the active material with a polysaccharide or a derivative thereof, This suppresses the number of cadmium hydroxide nuclei that precipitate on metal cadmium during discharge, and prevents the precipitated cadmium hydroxide particles from becoming finer. Therefore, it is possible to suppress the generation and accumulation of metal cadmium that cannot be discharged due to the surface of metal cadmium being covered with many fine cadmium hydroxide particles and contact between metal cadmium and electrolyte being prevented.
(ヘ) 実施例
多孔性ニツケル焼結基板に硝酸カドミウム水溶
液を含浸し、アルカリ処理、水洗及び乾燥を行な
う活物質含浸工程を6回繰り返して水酸化カドミ
ウムを基板内に所望量充填して極板を作製した
後、この極板をアルカリ水溶液中で充放電するこ
とで化成処理し、水洗及び乾燥を行ない、次いで
この化成処理後の極板をメチルセルロース1%水
溶液に浸漬した後、ブラツシングにより極板表面
部のメチルセルロースを除去し、本発明電極Aを
得る。(F) Example: A porous sintered nickel substrate is impregnated with an aqueous cadmium nitrate solution, and the active material impregnation process of alkaline treatment, water washing, and drying is repeated six times to fill the substrate with a desired amount of cadmium hydroxide to form an electrode plate. After producing the electrode plate, the electrode plate is subjected to chemical conversion treatment by charging and discharging in an aqueous alkaline solution, washed with water and dried.Then, the electrode plate after the chemical conversion treatment is immersed in a 1% aqueous solution of methylcellulose, and then the electrode plate is formed by brushing. The methylcellulose on the surface is removed to obtain electrode A of the present invention.
また比較として、メチルセルロース水溶液浸漬
とブラツシングをしない以外は前記実施例と同一
の条件で作成した比較電極B、またブラツシング
しない以外は前記実施例と同一の条件で作成した
比較電極Cを作製した。 For comparison, comparative electrode B was prepared under the same conditions as in the above example except that immersion in the methylcellulose aqueous solution and brushing were not performed, and comparative electrode C was prepared under the same conditions as in the above example except that brushing was not performed.
これらの電極A,B,Cを用いてサイクル特性
を比較検討した。この結果を、第1図に示す。
尚、サイクル条件は1/3Cの電流で160%充電し、
2Cの電流でニツケル板対極に対して−1.0V迄放
電するというものである。また容量は1サイクル
目を100%として示した。この結果より、メチル
セルロースを添加して焼結式カドミウム電極A,
Cは添加しない電極Bに比べ、サイクル特性が優
れている。これは第2図に示したように、サイク
ル数進行に伴う放電不能な金属カドミウムの生成
および蓄積量が少なく、電極の活性度が高いまま
に維持されたことに基づくものである。尚、ここ
で放電不能な金属カドミウムの量は、1回充放電
を行つたときに生成した放電不能な金属カドミウ
ムの量を、100%として示してある。 The cycle characteristics of these electrodes A, B, and C were compared and studied. The results are shown in FIG.
In addition, the cycle conditions are 160% charging at 1/3C current,
A current of 2C discharges to -1.0V against the nickel plate counter electrode. In addition, the capacity is shown with the first cycle being 100%. Based on this result, sintered cadmium electrode A with the addition of methylcellulose,
C has better cycle characteristics than electrode B, which is not added. This is because, as shown in FIG. 2, the amount of metal cadmium that cannot be discharged is generated and accumulated as the number of cycles progresses, and the activity of the electrode is maintained at a high level. Note that the amount of non-dischargeable metal cadmium is shown here, assuming that the amount of non-dischargeable metal cadmium generated when charging and discharging is performed once is 100%.
次に、これら電極A,B,Cそれぞれと化学含
浸法により得た焼結式ニツケル極板と組み合せ、
SCサイズの電池a,b,cを作製し、0℃にて
0.2Cの電流で連続充電を行つた。この時の電池内
部圧を測定し、第3図の如く、結果を得た。これ
より、メチルセルロース水溶液浸漬後のブラツシ
ングにより、電極表面部のメチルセルロースを除
去した本発明電池aは、酸素ガス吸収性能が、メ
チルセルロースを添加していない電池Bと同程度
であることが理解される。一方、メチルセルロー
スを単に添加した電池Cにおいては、焼結式カド
ミウム電極の大きな特徴である優れた酸素ガス吸
収性能が発揮されていない。この種の焼結式カド
ミウム電極における、酸素ガス吸収反応は以下の
ように表わすことができる。 Next, each of these electrodes A, B, and C is combined with a sintered nickel electrode plate obtained by a chemical impregnation method,
Fabricate SC size batteries a, b, and c and store them at 0°C.
Continuous charging was performed with a current of 0.2C. At this time, the internal pressure of the battery was measured, and the results were obtained as shown in FIG. From this, it is understood that the oxygen gas absorption performance of the battery a of the present invention in which the methylcellulose on the electrode surface was removed by brushing after immersion in the methylcellulose aqueous solution was comparable to that of the battery B to which methylcellulose was not added. On the other hand, in Battery C in which methylcellulose was simply added, the excellent oxygen gas absorption performance, which is a major feature of the sintered cadmium electrode, was not exhibited. The oxygen gas absorption reaction in this type of sintered cadmium electrode can be expressed as follows.
O2+2H2O+4e-→4OH- ……
4OH-+2Cd→2Cd(OH)2+4e- ……
このうち、反応は、主に電極表面に存在し、
電解液及び酸素ガスと接触できるニツケル焼結基
板上で進行する。したがつて、メチルセルロース
を添加することによつて電極表面のニツケル焼結
基板を覆われた電極Cを有する電池Cは、酸素ガ
ス吸収性能が低いものである。したがつて、本発
明電極Aのようにカドミウム活物質を充填したニ
ツケル焼結基板の内部にメチルセルロースを添加
した電極を有する電池aは、酸素ガス吸収性能を
高く維持することができるものであつて、放電不
能な金属カドミウムの生成および蓄積の少ないも
のであることが、以上の検討結果により知得さ
れ、本発明を完成するに至つたものである。 O 2 +2H 2 O+4e - →4OH - ... 4OH - +2Cd→2Cd(OH) 2 +4e - ... Among these, the reaction mainly occurs on the electrode surface,
The process proceeds on a nickel sintered substrate that can be contacted with electrolyte and oxygen gas. Therefore, the battery C having the electrode C in which the nickel sintered substrate on the electrode surface is covered by adding methylcellulose has low oxygen gas absorption performance. Therefore, a battery a having an electrode in which methyl cellulose is added inside a nickel sintered substrate filled with a cadmium active material like electrode A of the present invention can maintain high oxygen gas absorption performance. As a result of the above studies, it was discovered that the generation and accumulation of metal cadmium that cannot be discharged is small, and this led to the completion of the present invention.
尚、実施例において多糖類またはその誘導体と
してメチルセルロースを用いたが何らこれに限定
されず、デンプン、ペクチン、カルボキシメチル
セルロース、ヒドロキシプロピルセルロースなど
を用いても良い。 Although methylcellulose was used as the polysaccharide or its derivative in the examples, it is not limited thereto, and starch, pectin, carboxymethylcellulose, hydroxypropylcellulose, etc. may also be used.
また、多糖類またはその誘導体の添加の一例と
して、極板を水溶液へ浸漬することを開示した
が、スプレーによりふき付けたり、ローラーによ
り塗着することも可能であつて、更に、電極内部
に添加し酸素ガス吸収性能を向上させるために、
ブラツシングにより電極表面部に付着したものを
除去したが、水洗、ふき取りなどを行つて除去し
ても良い。 In addition, as an example of adding polysaccharides or derivatives thereof, immersing the electrode plate in an aqueous solution has been disclosed, but it is also possible to spray them on or apply them with a roller. In order to improve oxygen gas absorption performance,
Although the material adhering to the electrode surface was removed by brushing, it may also be removed by washing with water, wiping, or the like.
(ト) 発明の効果
本発明によれば、焼結式カドミウム電極の酸素
ガス吸収性能を低下させることなく高いままに維
持し、充放電サイクル数進行に伴う放電不能な金
属カドミウムの生成及び蓄積を主原因とする活物
質の不活性化を抑制し、これらの相乗効果で、か
かる電極を用いたアルカリ蓄電池のサイクル特性
を向上させることができ、その工業的価値はきわ
めて大きい。(G) Effects of the Invention According to the present invention, the oxygen gas absorption performance of the sintered cadmium electrode is maintained at a high level without deterioration, and the generation and accumulation of metallic cadmium that cannot be discharged as the number of charge/discharge cycles progresses. The deactivation of the active material, which is the main cause, can be suppressed, and the synergistic effect of these can improve the cycle characteristics of alkaline storage batteries using such an electrode, and its industrial value is extremely large.
第1図は電極のサイクル特性比較図、第2図は
充放電サイクル数と放電不能金属カドミウム量比
の関係を示す図、第3図は連続充電時の電池内部
圧力変化図である。
A……本発明電極、B,C……比較電極。
FIG. 1 is a comparison diagram of the cycle characteristics of the electrodes, FIG. 2 is a diagram showing the relationship between the number of charge/discharge cycles and the ratio of the amount of undischargeable metal cadmium, and FIG. 3 is a diagram of changes in battery internal pressure during continuous charging. A... Electrode of the present invention, B, C... Comparison electrode.
Claims (1)
板の内部に、多糖類またはその誘導体を添加した
ことを特徴とするアルカリ蓄電池用焼結式カドミ
ウム電極。1. A sintered cadmium electrode for an alkaline storage battery, characterized in that a polysaccharide or a derivative thereof is added to the inside of a nickel sintered substrate filled with a cadmium active material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62026722A JPS63195963A (en) | 1987-02-06 | 1987-02-06 | Sintered cadmium electrode for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62026722A JPS63195963A (en) | 1987-02-06 | 1987-02-06 | Sintered cadmium electrode for alkaline storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63195963A JPS63195963A (en) | 1988-08-15 |
| JPH0517658B2 true JPH0517658B2 (en) | 1993-03-09 |
Family
ID=12201223
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62026722A Granted JPS63195963A (en) | 1987-02-06 | 1987-02-06 | Sintered cadmium electrode for alkaline storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63195963A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3696086B2 (en) | 2000-12-28 | 2005-09-14 | 三洋電機株式会社 | Cadmium negative electrode for alkaline storage battery and method for producing the same |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2802043A (en) * | 1954-05-03 | 1957-08-06 | Nickel Cadmium Battery Corp | Alkaline electric storage battery and electrolyte therefor |
| JPS5635368A (en) * | 1979-08-29 | 1981-04-08 | Yuasa Battery Co Ltd | Preparation of cadmium plate for alkaline battery |
| JPS61158666A (en) * | 1984-12-28 | 1986-07-18 | Japan Storage Battery Co Ltd | Cadmium plate for alkaline storage battery |
-
1987
- 1987-02-06 JP JP62026722A patent/JPS63195963A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63195963A (en) | 1988-08-15 |
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