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JPH0670903B2 - Nickel electrode for alkaline secondary battery - Google Patents
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JPH0670903B2 - Nickel electrode for alkaline secondary battery - Google Patents

Nickel electrode for alkaline secondary battery

Info

Publication number
JPH0670903B2
JPH0670903B2 JP60039843A JP3984385A JPH0670903B2 JP H0670903 B2 JPH0670903 B2 JP H0670903B2 JP 60039843 A JP60039843 A JP 60039843A JP 3984385 A JP3984385 A JP 3984385A JP H0670903 B2 JPH0670903 B2 JP H0670903B2
Authority
JP
Japan
Prior art keywords
nickel
electrode
weight
nickel electrode
active material
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
Application number
JP60039843A
Other languages
Japanese (ja)
Other versions
JPS61198560A (en
Inventor
昇 小谷
尚伸 美甘
明夫 清水
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.)
Maxell Ltd
Original Assignee
Hitachi Maxell Energy 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 Hitachi Maxell Energy Ltd filed Critical Hitachi Maxell Energy Ltd
Priority to JP60039843A priority Critical patent/JPH0670903B2/en
Publication of JPS61198560A publication Critical patent/JPS61198560A/en
Publication of JPH0670903B2 publication Critical patent/JPH0670903B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • 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

  • 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〕 この発明はアルカリ二次電池用のニッケル電極に関す
る。さらに詳しくは、ニッケル−カドミウム二次電池、
ニッケル−亜鉛二次電池などのアルカリ二次電池の正極
として用いられる低コストでかつ特性の優れたニッケル
電極に関する。
TECHNICAL FIELD The present invention relates to a nickel electrode for an alkaline secondary battery. More specifically, nickel-cadmium secondary battery,
The present invention relates to a nickel electrode that is used as a positive electrode of an alkaline secondary battery such as a nickel-zinc secondary battery and has low cost and excellent characteristics.

〔従来の技術〕[Conventional technology]

従来、アルカリ二次電池用のニッケル電極は、ニッケル
粉末を焼結して作製した多孔性のニッケル焼結体を電極
基体として用い、これを硝酸ニッケル溶液に浸漬し、そ
の後、熱分解して活物質とする焼結式で製造されていた
(たとえばS.U.Falk & A.J.Salkind“Alkaline Storag
e Batteries"John Wiley & Sons Inc.(1969))。
Conventionally, a nickel electrode for an alkaline secondary battery uses a porous nickel sintered body produced by sintering nickel powder as an electrode substrate, soaking it in a nickel nitrate solution, and then thermally decomposing it for activation. Manufactured by sintering as a material (eg SUFalk & AJSalkind “Alkaline Storag
e Batteries "John Wiley & Sons Inc. (1969)).

この焼結式で製造された電極は、高率放電などに良好な
特性を有するものの、コストが高いという欠点があっ
た。その理由は、電極基体として用いるニッケル焼結体
を作るために高温還元雰囲気炉が必要なこと、さらには
活物質充填工程を数回繰り返す必要があることなどか
ら、設備費、光熱費、人件費などを多く要することにあ
った。
The electrode manufactured by this sintering method has good characteristics such as high rate discharge, but has a drawback of high cost. The reason is that a high-temperature reducing atmosphere furnace is required to make a nickel sintered body used as an electrode substrate, and the active material filling process needs to be repeated several times. There was a lot of cost.

そのため、現在はまだ実用化にいたっていないが、焼結
式電極の特性を維持しながら、コストの安いニッケル電
極を得る目的で、活物質と導電助剤と結着剤を適当量混
合し、ペースト状にして、これをパンチングメタルなど
の集電体に塗布するペースト式が提案され、注目をあび
ている。しかしながら、良好な結着剤が見出されていな
いため、電極強度が充分なものや、充放電サイクルを繰
り返しても活物質の脱落がないものは得られていない。
Therefore, although it has not yet been put to practical use at present, while maintaining the characteristics of the sintered electrode, in order to obtain a low cost nickel electrode, an active material, a conductive auxiliary agent and a binder are mixed in appropriate amounts, A paste method of forming a paste and applying it to a current collector such as punching metal has been proposed and attracts attention. However, since a good binder has not been found, neither one having sufficient electrode strength nor one in which the active material does not fall off even when the charge / discharge cycle is repeated is not obtained.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

以上のように、焼結式による場合は電極性能面で優れて
いるものの、製造面、コスト面で問題があり、一方、ペ
ースト式による場合は低コストに製造できるという利点
を有するものの、電極強度や充放電サイクルの繰り返し
による活物質の脱落という点において問題があり、現在
のところ、いずれの方式によっても満足すべきものは得
られていない。
As described above, although the sintering method is excellent in electrode performance, it has a problem in manufacturing and cost. On the other hand, the paste method has an advantage that it can be manufactured at low cost. There is a problem in that the active material comes off due to repeated charging and discharging cycles, and at present, no satisfactory method has been obtained by any of the methods.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上述した従来技術の問題点を解決するもので、
結着剤としてスルホン化したのち金属カルボン酸塩で中
和したエチレン−プロビレン−エチリデンノルボルネル
ターポリマー(以下、スルホン化EPDMという)を特定割
合で用い、かつ活物質に対する導電助剤の量を特定範囲
に規定することによって、ペースト式で、かつ電極特性
の優れたニッケル電極が得られるようにしたものであ
る。
The present invention solves the above-mentioned problems of the prior art,
Ethylene-propylene-ethylidene norbornel terpolymer (hereinafter referred to as sulfonated EPDM), which was sulfonated and then neutralized with a metal carboxylate as a binder, was used in a specific ratio, and the amount of the conductive additive to the active material was specified. By defining the range, it is possible to obtain a paste type nickel electrode having excellent electrode characteristics.

すなわち、本発明は活物質、導電助剤、結着剤を含むペ
ースト状配合剤を多孔性の電極基体に塗布または充填し
て製造するアルカリ二次電池用のニッケル電極におい
て、結着剤としてスルホン化EPDMをニッケル電極中1〜
10重量%用い、かつ活物質と導電助剤との割合を重量比
で70:30〜40:60にしたことを特徴とするアルカリ二次電
池用のニッケル電極に関する。
That is, the present invention provides a sulfone as a binder in a nickel electrode for an alkaline secondary battery, which is manufactured by applying or filling a paste-like compounding agent containing an active material, a conductive additive, and a binder to a porous electrode substrate. EPDM in nickel electrode
The present invention relates to a nickel electrode for an alkaline secondary battery, which is used in an amount of 10% by weight and a weight ratio of an active material to a conductive auxiliary agent is 70:30 to 40:60.

上記スルホン化EPDVは、結着力が非常に優れていて、従
来同様のニッケル電極中1〜10重量%という使用量で強
力な結着作用を発揮し、電極強度を高め、かつ充放電サ
イクルの繰り返しにおいても活物質の脱落を防止する。
The above-mentioned sulfonated EPDV has a very excellent binding force, and exerts a strong binding action at a usage amount of 1 to 10% by weight in a nickel electrode similar to the conventional one, enhances the electrode strength, and repeats charge / discharge cycles. Also, prevent the active material from falling off.

しかしながら、活物質表面に強力な皮膜を形成するた
め、電極の電子伝導性が低下し、ニッケル粉末、コバル
ト粉末などの導電助剤を従来同様に10〜20重量%程度添
加しただけでは、充分な電子伝導性が発揮されない。そ
こで、導電助剤の使用割合を多くし、前記のように活物
質に対して導電助剤を重量比で70:30〜40:60にすること
によって導電性を高め、電極特性を高めて実用性あるニ
ッケル電極を提供したものである。
However, since a strong film is formed on the surface of the active material, the electron conductivity of the electrode is lowered, and it is sufficient to add about 10 to 20% by weight of a conductive auxiliary agent such as nickel powder or cobalt powder as in the conventional case. Electronic conductivity is not exhibited. Therefore, by increasing the use ratio of the conductive auxiliary agent and increasing the conductive auxiliary agent to the active material in a weight ratio of 70:30 to 40:60 as described above, the conductivity is increased and the electrode characteristics are improved to be practical. The present invention provides a nickel electrode having good properties.

本発明を完成するにあたって、本発明者らは、当初、上
記スルホン化EPDMの優れた結着作用に着目し、単に結着
剤を従来使用のテフロン(商品名、デュポン社製フッ素
樹脂)に代えて使用し、ニッケル電極を製造したが、電
極強度の強い電極が得られるものの、電池に組み込んだ
際に内部抵抗が高く、充電中の作動電圧が高くなり、充
電効率が低下するなど、所望の電極特性が得られなかっ
た。
In completing the present invention, the present inventors initially focused on the excellent binding action of the above-mentioned sulfonated EPDM, and simply replaced the conventional binder with Teflon (trade name, fluorocarbon resin manufactured by DuPont). Although a nickel electrode was produced by using it, the electrode with strong electrode strength was obtained, but when it was incorporated into a battery, the internal resistance was high, the operating voltage during charging was high, and the charging efficiency was reduced. The electrode characteristics were not obtained.

そのため、本発明者らはその原因を究明すべく、さらに
研究を重ね、上記のように内部抵抗が高くなる原因が、
スルホン化EPDMの皮膜形成能が大きく、活物質表面に強
力な皮膜を形成するため電極の電子伝導性が低下し、ニ
ッケル粉末、コバルト粉末などの導電助剤を従来同様に
10〜20重量%程度添加しただけでは、充分な電子伝導性
が発揮されないためであることを見出し、導電助剤の量
を前記のように多くすることによって実用に供すること
ができる電極を提供したのである。
Therefore, the inventors of the present invention have conducted further studies to investigate the cause, and the cause of the increase in internal resistance as described above is
Sulfonated EPDM has a large film forming ability and forms a strong film on the surface of the active material, which reduces the electron conductivity of the electrode.
It was found that sufficient addition of about 10 to 20% by weight does not provide sufficient electron conductivity, and provided an electrode that can be put to practical use by increasing the amount of the conductive additive as described above. Of.

本発明において、結着剤として用いるスルホン化EPDM
は、耐アルカリ性も優れており、活物質の結着効果は前
述したとおり非常に大きく、しかもゴム弾性を有するの
で、形成される皮膜は柔軟性を有していて、渦巻状の電
極とする際には特に好適であり、結着剤として優れたも
のである。
Sulfonated EPDM used as a binder in the present invention
Has excellent alkali resistance, the binding effect of the active material is very large as described above, and also has rubber elasticity, so that the formed film has flexibility, and when it is used as a spiral electrode, It is particularly suitable for use as a binder and is an excellent binder.

このスルホン化EPDMの使用量としては、多すぎると活物
質粒子間の電子伝導が得られず、重負荷放電特性が損な
われ、少なすぎると結着効果が充分に発揮されないの
で、ニッケル電極中1〜10重量%にする。
If the amount of the sulfonated EPDM used is too large, electron conduction between the active material particles cannot be obtained, the heavy load discharge characteristics are impaired, and if it is too small, the binding effect is not sufficiently exhibited. Up to 10% by weight.

そして、上記スルホン化EPDMは、スルホン化率0.2〜20
モル%のものが上述した特性が特に優れていて好まし
く、スルホン化後の中和のための金属カルボン酸塩とし
ては、たとえばステアリン酸亜鉛、ステアリン酸バリウ
ム、ステアリン酸カルシウム、酢酸亜鉛、ラウリン酸亜
鉛などが使用される。
The sulfonated EPDM has a sulfonation rate of 0.2 to 20.
Those having a mol% are particularly preferable because of the excellent properties described above, and examples of metal carboxylates for neutralization after sulfonation include zinc stearate, barium stearate, calcium stearate, zinc acetate, zinc laurate and the like. Is used.

本発明の実施に際し、活物質としては水酸化ニッケルま
たはオキシ水酸化ニッケルが用いられる。この活物質を
主剤とするペースト状配合剤は、通常、上記活物質と、
ニッケル、コバルト、銀などの金属の粉末あるいは短繊
維、カーボン粉末、カーボン短繊維などの導電助剤と、
結着剤としてのスルホン化EPDMとヘキサン−メチルアル
コール混合液を混合することによって調製される、上記
コバルトは導電助剤としての作用以外にも充放電特性の
向上に寄与するという重要な役割を有している。上記ペ
ースト状配合剤には上記成分以外にも充電効率を向上さ
せるなどの目的で、水酸化リチウム、水酸化カルシウ
ム、水酸化カドミウムなどを添加してもよい。
In carrying out the present invention, nickel hydroxide or nickel oxyhydroxide is used as the active material. The paste-like compounding agent containing the active material as the main ingredient is usually the above active material,
Metallic powder such as nickel, cobalt, silver, or short fibers, carbon powder, short carbon fibers and other conductive aids,
Prepared by mixing sulfonated EPDM as a binder and a hexane-methyl alcohol mixed solution, the cobalt has an important role of contributing to the improvement of charge / discharge characteristics in addition to the action as a conductive additive. is doing. In addition to the above components, lithium paste, calcium hydroxide, cadmium hydroxide and the like may be added to the above paste-like compounding agent for the purpose of improving charging efficiency.

上記ペースト状配合剤の調製に際して、活物質と導電助
剤との割合は重量比で70:30〜40:60にされる。これは導
電助剤の量が前記範囲より少なくなると活物質粒子間の
電子伝導が充分に行なわれなくなり、正極の導電性が低
下して、内部抵抗が高くなり、充電効率が低下するから
であり、また導電助剤の量が前記範囲より多くなるとそ
のぶん活物質量が低下し、それによって電池の溶接効率
が低下するからである。
When preparing the above-mentioned paste-like compounding agent, the weight ratio of the active material to the conductive additive is 70:30 to 40:60. This is because if the amount of the conductive additive is less than the above range, electron conduction between the active material particles is not sufficiently performed, the conductivity of the positive electrode is reduced, the internal resistance is increased, and the charging efficiency is reduced. Also, if the amount of the conductive additive exceeds the above range, the amount of the active material is reduced, and the welding efficiency of the battery is reduced accordingly.

電極基体には、たとえばニッケル発泡体などの金属発泡
体、金属繊維チョップの焼結体、ニッケル平織金網など
の金属平織金網、樹脂繊維の上に金属メッキを施したも
のなどニッケル電極の製造に際して通常用いられる導電
性の多孔性基体が用いられる。
For the electrode substrate, for example, a metal foam such as a nickel foam, a sintered body of a metal fiber chop, a metal plain woven wire mesh such as a nickel plain woven wire mesh, or a resin fiber on which metal plating is applied The conductive porous substrate used is used.

〔実施例〕〔Example〕

つぎに実施例をあげて本発明をさらに詳細に説明する。 Next, the present invention will be described in more detail with reference to examples.

実施例1 水酸化ニッケル粉末60重量部と、金属ニッケル粉末35重
量部と、金属コバルト粉末5重量部を混合し、結着剤と
して濃度2重量%スルホン化EPDM(スルホン化率5モル
%、ステアリン酸亜鉛で中和)のヘキサン−メチルアル
コール(容量比95:5)溶液を添加し、ペースト状配合剤
を調製した。この電極中における結着剤量は5重量%と
なる。また、活物質と導電助剤との割合は重量比で60:4
0である。このペースト状配合剤を多孔性の電極基体
(厚さ0.8mm、空孔率80容量%のニッケル発泡体よりな
る電極基体)に摺り込むようにして充填し、乾燥後、厚
さ約0.5mmに加圧成形してニッケル電極を製造した。
Example 1 60 parts by weight of nickel hydroxide powder, 35 parts by weight of metallic nickel powder, and 5 parts by weight of metallic cobalt powder were mixed, and a concentration of 2% by weight of sulfonated EPDM (sulfonation rate: 5 mol%, stearin) was used as a binder. A hexane-methyl alcohol (volume ratio 95: 5) solution of zinc acid neutralized) was added to prepare a pasty compounding agent. The amount of binder in this electrode is 5% by weight. The weight ratio of the active material to the conductive additive is 60: 4.
It is 0. The paste-like compounding agent is slid into a porous electrode base (electrode base made of nickel foam having a thickness of 0.8 mm and a porosity of 80% by volume), and after drying, pressed to a thickness of about 0.5 mm. A nickel electrode was manufactured by molding.

このようにして製造されたニッケル電極を正極として用
い、カドミウム電極を負極として用いて、第1図に示す
ような構造で直径14.5mm、高さ50.0mmの円筒形ニッケル
−カドミウム二次電池(公称容量500mAh)を作製した。
Using the nickel electrode thus manufactured as a positive electrode and the cadmium electrode as a negative electrode, a cylindrical nickel-cadmium secondary battery having a structure as shown in FIG. 1 and having a diameter of 14.5 mm and a height of 50.0 mm (nominal) A capacity of 500 mAh) was produced.

第1図において、1は前記のようにして作製されたニッ
ケル電極で、厚さ0.5mm、幅40mm、長さ65mmの板状をし
ている。2はポリアミド不織布からなるセパレータであ
り、平均厚さ0.2mmで、各電極幅より約2mm大きい幅を有
している。3は負極としてのカドミウム電極で、このカ
ドミウム電極3は酸化カドミウムを水溶性バインダーを
用いて芯体に塗着したペースト式極板からなり、厚さ約
0.5mm、幅40mm、長さ85mmで、ニッケル電極の電気容量
の約1.5倍の電気容量を持っている。そして、このカド
ミウム電極3はセパレータ2を介在させて前記のニッケ
ル電極1と重ね合わせ、渦巻状に巻回されて外装缶9内
に収容されている。4はニッケル電極1のリードで、5
はカドミウム電極3のリードであり、6は金属製の封口
板で、この封口板6は上側部分6aと下側部分6bとからな
り、その下側部分6bに前記ニッケル電極側のリード4の
一端がスポット溶接されている。そして、この電池は電
池内圧が異常に上昇したときの安全性を確保するための
防爆弁7を有し、絶縁パッキング8と外装缶9をかしめ
るクリンプシールで密閉構造を保持しており、電池内に
は濃度30重量%の水酸化カリウム水溶液よりなる電解液
が封入されている。
In FIG. 1, reference numeral 1 denotes the nickel electrode manufactured as described above, which has a plate shape with a thickness of 0.5 mm, a width of 40 mm and a length of 65 mm. 2 is a separator made of polyamide nonwoven fabric, having an average thickness of 0.2 mm and having a width that is about 2 mm larger than the width of each electrode. Reference numeral 3 is a cadmium electrode as a negative electrode. The cadmium electrode 3 is composed of a paste type electrode plate in which cadmium oxide is applied to a core body using a water-soluble binder and has a thickness of about
It is 0.5 mm wide, 40 mm wide, and 85 mm long, and has a capacitance about 1.5 times the capacitance of nickel electrodes. The cadmium electrode 3 is superposed on the nickel electrode 1 with the separator 2 interposed therebetween, is spirally wound, and is housed in the outer can 9. 4 is a lead of the nickel electrode 1, 5
Is a lead of the cadmium electrode 3, 6 is a sealing plate made of metal, and this sealing plate 6 is composed of an upper part 6a and a lower part 6b, and the lower part 6b has one end of the lead 4 on the nickel electrode side. Are spot welded. Further, this battery has an explosion-proof valve 7 for ensuring safety when the internal pressure of the battery rises abnormally, and has a sealed structure with a crimp seal that crimps the insulating packing 8 and the outer can 9. An electrolytic solution consisting of an aqueous potassium hydroxide solution having a concentration of 30% by weight is enclosed therein.

比較例1 結着剤としてスルホン化EPDMに代えてテフロンを用いた
ほかは実施例1と同様にしてニッケル電極を製造した。
このニッケル電極を正極として用い、実施例1の場合と
同様にしてニッケル−カドミウム二次電池を作製した。
Comparative Example 1 A nickel electrode was produced in the same manner as in Example 1 except that Teflon was used as the binder instead of the sulfonated EPDM.
Using this nickel electrode as a positive electrode, a nickel-cadmium secondary battery was produced in the same manner as in Example 1.

比較例2 ニッケルの焼結体に硝酸ニッケルを含浸させ、加熱して
硝酸ニッケルを熱分解させてニッケル電極を製造した。
このニッケル電極を正極として用いたほかは実施例1の
場合と同様にしてニッケル−カドミウム二次電池を作製
した。
Comparative Example 2 A nickel electrode was manufactured by impregnating a nickel sintered body with nickel nitrate and heating it to thermally decompose the nickel nitrate.
A nickel-cadmium secondary battery was produced in the same manner as in Example 1 except that this nickel electrode was used as the positive electrode.

上記のように本発明の実施例1のニッケル電極を正極に
用いた電池を電池Aとし、従来技術に従いテフロンを結
着剤とした比較例1のペースト式ニッケル電極を正極に
用いた電池を電池Bとし、比較例2の焼結式ニッケル電
極を正極に用いた電池を電池Cとし、これらの電池A、
B、Cについて充放電サイクル特性を調べた。その結果
を第2図に示す。電池Aと電池B、Cの相違はニッケル
電極の違いのみであって、その他はすべて同じである。
そして、充放電サイクル特性試験の試験条件は放電電流
100mA、充電電流100mAで7.5時間充電し、充放電時のカ
ット電圧は充電時1.6V、放電時1.0Vである。
As described above, the battery using the nickel electrode of Example 1 of the present invention as the positive electrode was designated as battery A, and the battery using the paste type nickel electrode of Comparative Example 1 using Teflon as the binder according to the conventional technique as the positive electrode was designated as battery A. B, a battery using the sintered nickel electrode of Comparative Example 2 as a positive electrode is referred to as battery C, and these batteries A,
The charge / discharge cycle characteristics of B and C were examined. The results are shown in FIG. The difference between the battery A and the batteries B and C is only the difference in the nickel electrode, and the others are the same.
The test conditions for the charge / discharge cycle characteristic test are the discharge current.
Charged for 7.5 hours at 100mA and charging current of 100mA, the cut voltage during charging / discharging is 1.6V during charging and 1.0V during discharging.

第2図に示すように、本発明のニッケル電極を正極に用
いた電池Aは充放電サイクル数が増加しても放電容量が
大きく、比較例2の焼結式ニッケル電極を正極に用いた
電池Cと同等の充放電サイクル特性を有しており、比較
例1のペースト式ニッケル電極を正極に用いた電池Bに
比べて、充放電サイクル特性がはるかに優れていた。
As shown in FIG. 2, the battery A using the nickel electrode of the present invention as the positive electrode has a large discharge capacity even if the number of charge / discharge cycles increases, and the battery using the sintered nickel electrode of Comparative Example 2 as the positive electrode. It had a charge / discharge cycle characteristic equivalent to that of C, and was far superior in charge / discharge cycle characteristic to Battery B using the paste type nickel electrode of Comparative Example 1 as a positive electrode.

以上のように、本発明のニッケル電極は、焼結式ニッケ
ル電極に匹敵する充放電サイクル特性を有するが、その
製造に際しては、ペースト式で製造でき、焼結式ニッケ
ル電極を製造する場合に比べて製造工程を簡略化でき、
製造コストを大幅に低減できる。
As described above, the nickel electrode of the present invention has charge / discharge cycle characteristics comparable to those of the sintered nickel electrode, but in the production thereof, it can be produced by the paste method, and compared with the case of producing the sintered nickel electrode. Can simplify the manufacturing process,
Manufacturing cost can be significantly reduced.

実施例2 水酸化ニッケル粉末70重量部、金属ニッケル粉末25重量
部、金属コバルト粉末5重量部としたほかは実施例1と
同様にしてニッケル電極を製造した。
Example 2 A nickel electrode was produced in the same manner as in Example 1 except that 70 parts by weight of nickel hydroxide powder, 25 parts by weight of metallic nickel powder and 5 parts by weight of metallic cobalt powder were used.

実施例3 水酸化ニッケル粉末50重量部、金属ニッケル粉末45重量
部、金属コバルト粉末5重量部としたほかは実施例1と
同様にしてニッケル電極を製造した。
Example 3 A nickel electrode was produced in the same manner as in Example 1 except that 50 parts by weight of nickel hydroxide powder, 45 parts by weight of metallic nickel powder and 5 parts by weight of metallic cobalt powder were used.

実施例4 水酸化ニッケル粉末40重量部、金属ニッケル粉末55重量
部、金属コバルト粉末5重量部としたほかは実施例1と
同様にしてニッケル電極を製造した。
Example 4 A nickel electrode was produced in the same manner as in Example 1 except that 40 parts by weight of nickel hydroxide powder, 55 parts by weight of metallic nickel powder and 5 parts by weight of metallic cobalt powder were used.

比較例3 水酸化ニッケル粉末30重量部、金属ニッケル粉末65重量
部、金属コバルト粉末5重量部としたほかは実施例1と
同様にしてニッケル電極を製造した。
Comparative Example 3 A nickel electrode was produced in the same manner as in Example 1 except that 30 parts by weight of nickel hydroxide powder, 65 parts by weight of metallic nickel powder and 5 parts by weight of metallic cobalt powder were used.

比較例4 水酸化ニッケル粉末80重量部、金属ニッケル粉末15重量
部、金属コバルト粉末5重量部としたほかは実施例1と
同様にしてニッケル電極を製造した。
Comparative Example 4 A nickel electrode was produced in the same manner as in Example 1 except that 80 parts by weight of nickel hydroxide powder, 15 parts by weight of metallic nickel powder and 5 parts by weight of metallic cobalt powder were used.

これら実施例2〜4のニッケル電極および比較例3〜4
のニッケル電極をそれぞれ正極として実施例1と同様の
ニッケル−カドミウム二次電池を製造した。
The nickel electrodes of Examples 2 to 4 and Comparative Examples 3 to 4
A nickel-cadmium secondary battery similar to that of Example 1 was manufactured by using each of the nickel electrodes described in 1 above as a positive electrode.

これらの電池ならびに実施例1のニッケル電極を正極に
用いた電池について、前記と同様に充放電サイクル試験
を行ない、充放電サイクルが1回のときの放電容量と、
充放電サイクル数が500回に達したときの放電容量の保
持率(充放電サイクル数が1回のときの放電容量に対す
る保持率)を調べた結果を第1表に示す。
The battery and the battery using the nickel electrode of Example 1 as the positive electrode were subjected to the charge / discharge cycle test in the same manner as described above, and the discharge capacity when the charge / discharge cycle was once,
Table 1 shows the results of examining the retention rate of the discharge capacity when the number of charge / discharge cycles reached 500 (retention rate with respect to the discharge capacity when the number of charge / discharge cycles was 1).

第1表に示すように、活物質に対する導電助剤の割合が
重量比で40:60より多くなると、比較例3に示すよう
に、サイクル数が多くなった場合の保持率は良好なもの
の、電池内に仕込める放電容量が低下し、電池の容量効
率が低下することになり、逆に活物質に対す導電助剤の
割合が重量比で70:30より少なくなると、比較例4に示
すように、電池の溶接効率は向上するものの、サイクル
を重ねるごとに保持率が低下するようになる。
As shown in Table 1, when the weight ratio of the conductive additive to the active material was more than 40:60, as shown in Comparative Example 3, although the retention rate was good when the number of cycles was large, When the discharge capacity that can be charged in the battery is reduced and the capacity efficiency of the battery is reduced, and conversely the ratio of the conductive additive to the active material is less than 70:30 by weight, as shown in Comparative Example 4. In addition, although the welding efficiency of the battery is improved, the retention rate becomes lower as the cycle is repeated.

なお、本発明によって得られるニッケル電極は、実施例
に例示したニッケル−カドミウム二次電池のみならず、
たとえばニッケル−亜鉛二次電池、ニッケル−鉄二次電
池などのアルカリ二次電池にも応用できる。
The nickel electrode obtained by the present invention is not limited to the nickel-cadmium secondary battery illustrated in the examples,
For example, it can be applied to alkaline secondary batteries such as nickel-zinc secondary batteries and nickel-iron secondary batteries.

〔発明の効果〕〔The invention's effect〕

以上説明したように、本発明ではスルホン化EPDMを結着
剤に用いることによって、電極強度を高め、活物質の脱
落を防止することができ、充放電サイクル特性の向上が
達成できた。そしてペースト式電極製造の長所を充分に
生かすことができ、簡単な方法で、経済有利に、かつ製
造工程上有利に特性の優れたニッケル電極を製造するこ
とができた。
As described above, in the present invention, by using the sulfonated EPDM as the binder, the electrode strength can be increased, the active material can be prevented from falling off, and the charge / discharge cycle characteristics can be improved. Further, the advantages of the paste-type electrode production can be fully utilized, and the nickel electrode having excellent characteristics can be produced with a simple method, economically, and in the production process.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明のニッケル電極を用いた円筒形ニッケル
−カドミウム二次電池の一例を示す断面図、第2図は本
発明のニッケル電極を用いた円筒形ニッケル−カドミウ
ム二次電池と従来のニッケル電極を用いた円筒形ニッケ
ル−カドミウム二次電池の充放電サイクル特性を示す図
である。 1……ニッケル電極、2……セパレータ、 3……カドミウム電極
FIG. 1 is a cross-sectional view showing an example of a cylindrical nickel-cadmium secondary battery using the nickel electrode of the present invention, and FIG. 2 is a cylindrical nickel-cadmium secondary battery using the nickel electrode of the present invention and a conventional battery. It is a figure which shows the charging / discharging cycle characteristic of a cylindrical nickel-cadmium secondary battery using a nickel electrode. 1 ... Nickel electrode, 2 ... Separator, 3 ... Cadmium electrode

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】活物質、導電助剤、結着剤を含むペースト
状配合剤を多孔性の電極基体に塗布または充填して製造
するアルカリ二次電池用のニッケル電極において、結着
剤としてスルホン化したのち金属カルボン酸塩で中和さ
れたエチレン−プロピレン−エチリデンノルボルネルタ
ーポリマーをニッケル電極中1〜10重量%用い、活物質
と導電助剤を重量比で70:30〜40:60にしたことを特徴と
するアルカリ二次電池用のニッケル電極。
1. A nickel electrode for an alkaline secondary battery, which is produced by applying or filling a paste-like compounding agent containing an active material, a conductive auxiliary agent, and a binder to a porous electrode substrate to produce sulfone as a binder. 1-10% by weight of ethylene-propylene-ethylidene norbornel terpolymer neutralized with a metal carboxylate in a nickel electrode was used, and the active material and the conductive additive were added at a weight ratio of 70: 30-40: 60. A nickel electrode for an alkaline secondary battery characterized by the above.
JP60039843A 1985-02-27 1985-02-27 Nickel electrode for alkaline secondary battery Expired - Lifetime JPH0670903B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60039843A JPH0670903B2 (en) 1985-02-27 1985-02-27 Nickel electrode for alkaline secondary battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60039843A JPH0670903B2 (en) 1985-02-27 1985-02-27 Nickel electrode for alkaline secondary battery

Publications (2)

Publication Number Publication Date
JPS61198560A JPS61198560A (en) 1986-09-02
JPH0670903B2 true JPH0670903B2 (en) 1994-09-07

Family

ID=12564243

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60039843A Expired - Lifetime JPH0670903B2 (en) 1985-02-27 1985-02-27 Nickel electrode for alkaline secondary battery

Country Status (1)

Country Link
JP (1) JPH0670903B2 (en)

Also Published As

Publication number Publication date
JPS61198560A (en) 1986-09-02

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