JPH0677452B2 - Nickel positive electrode plate for alkaline storage battery and manufacturing method thereof - Google Patents
Nickel positive electrode plate for alkaline storage battery and manufacturing method thereofInfo
- Publication number
- JPH0677452B2 JPH0677452B2 JP60213182A JP21318285A JPH0677452B2 JP H0677452 B2 JPH0677452 B2 JP H0677452B2 JP 60213182 A JP60213182 A JP 60213182A JP 21318285 A JP21318285 A JP 21318285A JP H0677452 B2 JPH0677452 B2 JP H0677452B2
- Authority
- JP
- Japan
- Prior art keywords
- main component
- nickel
- cobalt
- hydroxide
- layer
- 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
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims description 132
- 229910052759 nickel Inorganic materials 0.000 title claims description 64
- 238000003860 storage Methods 0.000 title claims description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 claims description 62
- ASKVAEGIVYSGNY-UHFFFAOYSA-L cobalt(ii) hydroxide Chemical compound [OH-].[OH-].[Co+2] ASKVAEGIVYSGNY-UHFFFAOYSA-L 0.000 claims description 62
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 claims description 51
- 239000000758 substrate Substances 0.000 claims description 37
- 150000001869 cobalt compounds Chemical class 0.000 claims description 27
- 238000005470 impregnation Methods 0.000 claims description 26
- 239000000126 substance Substances 0.000 claims description 21
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 claims description 20
- 229910000428 cobalt oxide Inorganic materials 0.000 claims description 19
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
- 239000000243 solution Substances 0.000 claims description 13
- 238000002161 passivation Methods 0.000 claims description 9
- 239000007774 positive electrode material Substances 0.000 claims description 8
- 230000001590 oxidative effect Effects 0.000 claims description 6
- 150000001868 cobalt Chemical class 0.000 claims description 5
- 229910044991 metal oxide Inorganic materials 0.000 claims description 4
- 150000004706 metal oxides Chemical class 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 150000002815 nickel Chemical class 0.000 claims description 3
- 239000003929 acidic solution Substances 0.000 claims description 2
- 239000011149 active material Substances 0.000 description 102
- 238000000034 method Methods 0.000 description 35
- 238000002474 experimental method Methods 0.000 description 21
- 230000000694 effects Effects 0.000 description 15
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 11
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 11
- 239000007864 aqueous solution Substances 0.000 description 10
- 230000007423 decrease Effects 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 238000012856 packing Methods 0.000 description 10
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 9
- 229910017052 cobalt Inorganic materials 0.000 description 8
- 239000010941 cobalt Substances 0.000 description 8
- 238000011049 filling Methods 0.000 description 8
- 229910000480 nickel oxide Inorganic materials 0.000 description 6
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 6
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- -1 cobalt oxyhydroxide Chemical compound 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- OSOVKCSKTAIGGF-UHFFFAOYSA-N [Ni].OOO Chemical compound [Ni].OOO OSOVKCSKTAIGGF-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 229940011182 cobalt acetate Drugs 0.000 description 1
- 229940044175 cobalt sulfate Drugs 0.000 description 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229910000483 nickel oxide hydroxide Inorganic materials 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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、水酸化ニッケルを主成分とする2つの層の間
にサンドイッチ構造的に水酸化コバルトあるいはコバル
ト酸化物を主成分とする層を形成したアルカリ蓄電池用
ニッケル正極板、あるいはさらに前記構造の正極活物質
の表面にも水酸化コバルトあるいはコバルト酸化物を主
成分とする層を形成したアルカリ蓄電池用ニッケル正極
板に関するものである。TECHNICAL FIELD OF THE INVENTION The present invention forms a layer containing cobalt hydroxide or cobalt oxide as a sandwich structure between two layers containing nickel hydroxide as a main component. The present invention relates to a nickel positive electrode plate for an alkaline storage battery, or a nickel positive electrode plate for an alkaline storage battery in which a layer containing cobalt hydroxide or cobalt oxide as a main component is formed on the surface of the positive electrode active material having the above structure.
従来の技術・発明が解決しようとする問題点 従来、アルカリ蓄電池に用いられるニッケル正極板は、
カーボニルニッケル粉末を還元雰囲気下で焼結した多孔
性焼結ニッケル基板中にニッケル塩を主成分とする酸性
溶液を含浸し、濃縮後、熱アルカリ溶液に浸漬してニッ
ケル基板の孔中に水酸化ニッケルを主成分とする正極活
物質を充填するという方法によって作製されている。最
近ではアルカリ蓄電池を用いる機器の小型化などが進
み、市場の要求としては蓄電池の単位体積当りの容量密
度の増加を望む声が強まっているが、従来のニッケル正
極板ではこのような市場の要求を満たすことが出来なか
った。また焼結式極板の他では、スポンジ状ニッケルに
水酸化ニッケルを主成分とする正極活物質粉末を物理的
に充填する発泡式ニッケル正極板があるが、この場合、
活物質粉末の充填量を多くした状態では活物質利用率が
低下して、実質的な容量密度は期待するほど増加が見ら
れず、また放電時の電位特性が低下するといった問題が
ある。Problems to be Solved by Conventional Techniques and Inventions Conventionally, nickel positive electrode plates used for alkaline storage batteries are
Porous sintered nickel substrate obtained by sintering carbonyl nickel powder in a reducing atmosphere is impregnated with an acidic solution containing nickel salt as the main component, concentrated, and then immersed in a hot alkaline solution to hydrate the pores of the nickel substrate. It is manufactured by a method of filling a positive electrode active material containing nickel as a main component. Recently, with the miniaturization of equipment using alkaline storage batteries, there is a growing demand for market to increase the capacity density per unit volume of storage batteries. I could not meet. In addition to the sintered electrode plate, there is a foamed nickel positive electrode plate in which sponge nickel is physically filled with a positive electrode active material powder containing nickel hydroxide as a main component.
When the filling amount of the active material powder is increased, there is a problem that the utilization factor of the active material decreases, the substantial capacity density does not increase as expected, and the potential characteristic during discharge deteriorates.
ニッケル正極板の容量を高める方法としては、正極活物
質量を増加することと活物質利用率を高めることの2つ
が考えられるが、焼結式正極板の場合、正極活物質の増
加については従来の極板ではすでに限界に近く、さらに
増加させた場合、容量は若干増加するものの放電時の電
位特性が低下することになり適切とは言えない。一方、
活物質利用率を高める方法としては、一般に酸性のニッ
ケル塩の含浸液にコバルト塩を数%添加し、含浸工程後
の活物質中に水酸化コバルトを均一に分散することが行
なわれている。この方法によると、活物質の利用率だけ
でなく、高温特性も向上するが、利用率向上の効果自体
はそれほど大きくなく、ニッケル正極板の高容量化には
不充分であった。There are two possible methods for increasing the capacity of the nickel positive electrode plate: increasing the amount of the positive electrode active material and increasing the utilization rate of the active material. The electrode plate is already close to the limit, and when it is further increased, the capacity is slightly increased, but the potential characteristic at the time of discharge is deteriorated, which is not appropriate. on the other hand,
As a method of increasing the utilization rate of the active material, generally, several percent of cobalt salt is added to an impregnating solution of acidic nickel salt, and cobalt hydroxide is uniformly dispersed in the active material after the impregnation step. According to this method, not only the utilization factor of the active material but also the high temperature characteristics are improved, but the effect of the utilization factor improvement itself is not so large, and it was not sufficient to increase the capacity of the nickel positive electrode plate.
最近、ニッケル正極板の性能を向上させる方法として、
主に3つの公知技術が提案されている。Recently, as a method of improving the performance of the nickel positive electrode plate,
Mainly three known techniques have been proposed.
公知技術1としては例えば特開昭51−121743号、特開昭
51−121744号があり、これらの技術は水酸化ニッケルを
保持した極板をpH3.5〜6.0の硫酸コバルトあるいはpH4.
0〜6.8の酢酸コバルト含浸液に浸漬し、該コバルト塩を
水酸化コバルトに変化させることにより、極板容量が増
加するというものである。Known techniques 1 include, for example, Japanese Patent Laid-Open Nos. 51-121743 and Sho.
51-121744, these technologies use electrode plates holding nickel hydroxide as cobalt sulfate of pH 3.5 to 6.0 or pH 4.
By immersing in a cobalt acetate impregnating solution of 0 to 6.8 and changing the cobalt salt into cobalt hydroxide, the capacity of the electrode plate is increased.
公知技術2としては例えば特開昭59−163753号があり、
この技術は水酸化ニッケルを保持した極板を硝酸コバル
トを含む硝酸塩水溶液に浸漬し、次いでアルカリ処理を
行ない、水酸化コバルト単独の層を0.5〜5wt%活物質表
面に形成させるという公知技術1と類似の操作及び効果
を持つものである。A known technique 2 is, for example, Japanese Patent Laid-Open No. 59-163753.
In this technique, the electrode plate holding nickel hydroxide is dipped in a nitrate aqueous solution containing cobalt nitrate and then alkali-treated to form a layer of cobalt hydroxide alone on the surface of the active material of 0.5 to 5 wt%. It has a similar operation and effect.
これらの技術は活物質の構造がマクロ的に2層構造であ
って、水酸化コバルトの層が水酸化ニッケルの外側に形
成されているものである。In these techniques, the structure of the active material is a macroscopic two-layer structure, and a cobalt hydroxide layer is formed on the outside of nickel hydroxide.
公知技術3としては例えば特公昭57−5018号があり、こ
の技術はコバルトを主成分とする含浸液を1回以上用い
て正極板を作製することにより、未化成つまりプリチャ
ージを行なっていないカドミウム負極板を相手極として
電池を組み立てた場合に、正極のコバルトはほとんどが
充電出来るにもかかわらず、放電においてはそのうち20
〜25%程度しか出来ないため、その放電できないコバル
トの容量が負極をプリチャージしたのと同様の作用をす
るものである。しかしその内容はコバルト塩を主成分と
する含浸液を用いる時期や含浸するコバルト化合物の最
適な量については明記されていない。つまり、コバルト
塩を主成分とする含浸液を用いるのが最初でも最後でも
良く、またコバルト化合物の含有量についても活物質利
用率が低下してしまうような量の多い範囲(後述)でも
良いことになる。Known technology 3 is, for example, Japanese Examined Patent Publication No. 57-5018, and this technology is to form a positive electrode plate by using an impregnating solution containing cobalt as a main component one or more times, so that cadmium that has not been preformed, that is, precharged When a battery is assembled using the negative electrode plate as the counter electrode, although most of the positive electrode cobalt can be charged, 20% of it can be discharged.
Since only ~ 25% can be produced, the capacity of cobalt that cannot be discharged has the same effect as precharging the negative electrode. However, the content thereof does not specify the timing of using the impregnating liquid containing a cobalt salt as a main component and the optimum amount of the cobalt compound to be impregnated. That is, the impregnating liquid containing a cobalt salt as a main component may be used at the beginning or at the end, and the content of the cobalt compound may be within a range where the utilization rate of the active material is low (described later). become.
上記したような従来の公知技術1,2および3による正極
板は従来の活物質中に水酸化コバルトを均一に分散させ
た正極板に比べ、活物質利用率は向上する。しかし、こ
の効果は多孔性金属基板への活物質充填密度及び放電レ
ートがそれほど高くない場合に有効であるが、活物質充
填密度の高い場合においては、この効果は半減し、特に
高率放電ではその効果がほとんど認められなくなるとい
う欠点があった。The positive electrode plate according to the above-described conventional known techniques 1, 2 and 3 has a higher utilization ratio of the active material than the conventional positive electrode plate in which cobalt hydroxide is uniformly dispersed in the active material. However, this effect is effective when the active material packing density and the discharge rate on the porous metal substrate are not so high, but when the active material packing density is high, this effect is halved, especially at high rate discharge. There was a drawback that the effect was hardly recognized.
本発明は上記したような公知技術1,2および3の提案に
関係するものであるが、全く新しい事実を実験によって
見い出し、上記したような公知技術の欠点を克服したも
ので、特に活物質充填密度の高い状態において、活物質
利用率および放電電位特性が著しく向上する正極板を提
供するものである。即ち、本発明は水酸化コバルトの形
成状態を詳細に調べた結果、水酸化コバルトを主成分と
する層を公知技術1,2のように水酸化ニッケルの外側に
形成させるような2層構造ではなく、水酸化ニッケルを
主成分とする2つの層の間に水酸化コバルトを主成分と
する層や、その水酸化コバルトを酸化せしめてコバルト
酸化物を主成分とする層を形成せしめたサンドイッチ構
造を3層以上形成させることにより、従来の製法では得
られなかった活物質充填密度の高い状態で活物質利用率
と放電電位特性及び各々の放電レート依存性の良好なニ
ッケル正極板を得ることができることを見い出したこと
に基づくものである。さらに本発明では活物質の構造の
他、用いる多孔性金属基板の状態にも検討を加えた結
果、その基板表面に不働態皮膜を形成させると活物質充
填密度の高い状態において活物質利用率及び放電電位特
性また各々の放電レート依存性がさらに一層良好になる
ことも見い出したものである。The present invention is related to the proposals of the above-mentioned known techniques 1, 2 and 3, but it is an object of the invention to discover a completely new fact by experiments and overcome the above-mentioned drawbacks of the known technique. It is intended to provide a positive electrode plate in which the utilization factor of the active material and the discharge potential characteristic are remarkably improved in a high density state. That is, according to the present invention, as a result of detailed examination of the formation state of cobalt hydroxide, in the two-layer structure in which a layer containing cobalt hydroxide as a main component is formed outside nickel hydroxide as in the known arts 1 and 2. , A sandwich structure in which a layer containing cobalt hydroxide as the main component or a layer containing cobalt oxide as the main component is formed by oxidizing the cobalt hydroxide between two layers containing nickel hydroxide as the main component. By forming three or more layers of nickel, it is possible to obtain a nickel positive electrode plate having a high active material utilization rate and discharge potential characteristics and good discharge rate dependence of each in a state of high active material packing density, which has not been obtained by the conventional manufacturing method. It is based on discovering what can be done. Furthermore, in the present invention, in addition to the structure of the active material, as a result of investigating the state of the porous metal substrate to be used, when the passive film is formed on the substrate surface, the active material utilization rate and It has also been found that the discharge potential characteristics and the respective discharge rate dependencies are further improved.
問題点を解決するための手段 即ち、本発明は多孔性金属基板上に第1層目としてまず
水酸化ニッケルを主成分とする層を形成し、次にその上
に第2層目として水酸化コバルトを主成分とする層か、
あるいはその水酸化コバルトを主成分とする層を化学的
もしくは電気化学的に酸化してコバルト酸化物を主成分
とする層となし、さらにその上に第3層目として水酸化
ニッケルを主成分とする層を形成した正極板、つまり水
酸化ニッケルを主成分とする2つの層の間にサンドイッ
チ構造的に水酸化コバルトもしくはコバルト酸化物を主
成分とする層を形成することによって、従来では得るこ
とができなかった、活物質充填密度の高い状態でも活物
質利用率、放電電位特性及び各々の放電レート依存性が
良好なニッケル正極板を得ることができるようにしたも
のである。さらに前記のサンドイッチ構造の正極板の表
面に第4層目として水酸化コバルトを主成分とする層を
形成することによって、活物質利用率をさらに数%高め
ることができるようにしたものである。この場合、1CA
の放電電流での活物質利用率はほぼ100%に近い値にな
る。また用いる多孔性金属基板の表面に金属酸化物の不
働態皮膜を形成することによって、活物質利用率及び放
電電位特性の放電レート依存性をさらに小さくすること
ができる。Means for Solving the Problems That is, according to the present invention, a layer mainly containing nickel hydroxide is first formed as a first layer on a porous metal substrate, and then a second layer is formed on the porous metal substrate as a second layer. A layer based on cobalt,
Alternatively, the layer containing cobalt hydroxide as a main component is chemically or electrochemically oxidized to form a layer containing cobalt oxide as a main component, and a third layer containing nickel hydroxide as a main component is further formed thereon. What has been obtained in the past by forming a positive electrode plate on which is formed a layer, that is, by forming a layer containing cobalt hydroxide or cobalt oxide as a main component in a sandwich structure between two layers containing nickel hydroxide as a main component. It has been made possible to obtain a nickel positive electrode plate having good active material utilization rate, discharge potential characteristics, and respective discharge rate dependency even in a state where the active material packing density is high. Further, by forming a fourth layer containing cobalt hydroxide as a main component on the surface of the positive electrode plate having the sandwich structure, the utilization rate of the active material can be further increased by several percent. In this case, 1 CA
The active material utilization rate at the discharge current of is close to 100%. Further, by forming a passivation film of a metal oxide on the surface of the porous metal substrate to be used, the discharge rate dependence of the active material utilization rate and the discharge potential characteristics can be further reduced.
実施例 本発明に関する実験及び実施例を以下に示す。Examples The experiments and examples relating to the present invention are shown below.
実験1 硝酸ニッケルを主成分とする含浸液を用いて化学含浸法
の操作を数回繰り返して焼結式ニッケル基板中に第1層
目の水酸化ニッケルを主成分とする層を形成した。次に
種々の濃度の硝酸コバルト溶液を用いて化学含浸法の操
作を1回行なって第2層目の水酸化コバルト単独の層を
形成した後、この水酸化コバルトを電気化学的に酸化し
てオキシ水酸化コバルト等のコバルト酸化物の層を形成
した。さらにその上に第1層目と同様の方法で第3層目
の水酸化ニッケルを主成分とする層を形成した。このよ
うにして作製したニッケル正極板(極板群Aとする)の
活物質利用率を比重1.250(20℃)KOH溶液中で測定し
た。なお、一部の濃度の硝酸コバルト含浸液について
は、第2層目の水酸化コバルト単独の層を形成した後、
この水酸化コバルトを電気化学的に酸化することなく、
第3層目の水酸化ニッケルを主成分とする層を形成した
極板(極板群Bとする)も作製し、同様の方法で活物質
利用率を測定した。第1図に活物質として充填した水酸
化ニッケル量に対する第2層目のコバルト化合物の割合
と活物質利用率の関係を示す。極板の理論容量は含浸し
た水酸化ニッケルと水酸化コバルトの量を基準とし、各
々が1電子反応に従うものとして算出した。ニッケル焼
結基板としてはカーボニルニッケル粉末と水及び糊料を
混練してニッケルスラリーとなし、該ニッケルスラリー
を鉄にニッケルメッキした金属板に塗布後、還元雰囲気
下において900℃でニッケルを焼結したものを用いた。
第1図において、第2層目の水酸化コバルトを電気化学
的に酸化した極板群Aの場合、コバルト化合物の量が0.
6〜10.0モル%の範囲で活物質利用率が高くなってい
る。これはニッケルに比べてコバルトの水酸化物とオキ
シ水酸化物等のコバルト酸化物との可逆電位が卑であ
り、充放電の電位特性から推定して、充電時は水酸化ニ
ッケルより先に水酸化コバルトがオキシ水酸化コバルト
等のコバルト酸化物に充電され、放電時は逆にオキシ水
酸化ニッケルの放電が先行すること、またオキシ水酸化
コバルト等のコバルト酸化物は導電性が良好であるなど
のことから、第2層目のコバルト単独の層が集電体的な
効果を持つことによって活物質利用率が高くなったもの
と考えられるが、コバルト化合物の量が多くなった場合
に逆に活物質利用率が低下している原因については不明
である。一方、第2層目の水酸化コバルト単独の層を電
気化学的に酸化しなかった極板群Bの場合には、活物質
利用率はほとんど高くなっておらず、先の極板群Aの場
合の結果とは相当異なっている。この理由としては第3
層目の水酸化ニッケルを主成分とする層の形成におい
て、硝酸ニッケルの溶液を含浸した時に、第2層目の水
酸化コバルト単独の層が溶解し、続く中和工程で水酸化
ニッケル中に水酸化コバルトが分散するために集電体的
な効果が減少し、その結果、活物質利用率が高くならな
かったものと思われる。このことからコバルト化合物単
独の層を形成する場合、その前後の水酸化ニッケルを主
成分とする層と出来るだけ混じり合わないようにするこ
とが必要であると考えられるので、化学含浸法によって
正極板を作製する場合には、第2層目の水酸化コバルト
単独の層を形成した後、酸化して含浸液に溶解し難いコ
バルト酸化物に変化させることが必要である。しかし化
学含浸法以外の方法で活物質を充填する場合には、例え
ば発泡式極板のように物理的に活物質を充填する場合は
この限りではなく、水酸化コバルトを酸化しなくても活
物質の充填密度が高い状態で、活物質利用率が高いこと
を確認している。Experiment 1 The operation of the chemical impregnation method was repeated several times using an impregnating liquid containing nickel nitrate as the main component to form a first layer containing nickel hydroxide as the main component in the sintered nickel substrate. Next, the operation of the chemical impregnation method was performed once using cobalt nitrate solutions of various concentrations to form a second layer of cobalt hydroxide alone, and this cobalt hydroxide was electrochemically oxidized. A layer of cobalt oxide such as cobalt oxyhydroxide was formed. Further, a third layer containing nickel hydroxide as a main component was formed thereon in the same manner as the first layer. The utilization ratio of the active material of the nickel positive electrode plate (referred to as electrode plate group A) thus produced was measured in a KOH solution having a specific gravity of 1.250 (20 ° C.). For some cobalt nitrate impregnation solutions, after forming the second layer of cobalt hydroxide alone,
Without electrochemically oxidizing this cobalt hydroxide,
An electrode plate (referred to as electrode plate group B) having a third layer containing nickel hydroxide as a main component was also prepared, and the active material utilization rate was measured by the same method. FIG. 1 shows the relationship between the ratio of the cobalt compound in the second layer and the utilization rate of the active material with respect to the amount of nickel hydroxide filled as the active material. The theoretical capacity of the electrode plate was calculated on the basis of the amounts of impregnated nickel hydroxide and cobalt hydroxide, and each one follows a one-electron reaction. As a nickel sintered substrate, carbonyl nickel powder, water and a paste are kneaded to form a nickel slurry, and the nickel slurry is applied to a nickel-plated metal plate of iron, and then nickel is sintered at 900 ° C. in a reducing atmosphere. I used one.
In FIG. 1, in the case of the electrode group A obtained by electrochemically oxidizing the second layer of cobalt hydroxide, the amount of cobalt compound was 0.
The active material utilization rate is high in the range of 6 to 10.0 mol%. This is because the reversible potential of cobalt hydroxide and cobalt oxides such as oxyhydroxide is less than that of nickel. Cobalt oxide is charged to cobalt oxide such as cobalt oxyhydroxide, and when discharging, nickel oxyhydroxide is discharged first, and cobalt oxide such as cobalt oxyhydroxide has good conductivity. From this, it is considered that the second layer of cobalt alone has a high current utilization factor due to the collector-like effect. However, when the amount of cobalt compound is increased, The cause of the decrease in active material utilization is unknown. On the other hand, in the case of the electrode plate group B in which the second layer of the cobalt hydroxide alone was not electrochemically oxidized, the active material utilization rate was hardly increased, and The results are quite different. The third reason is
In the formation of the layer containing nickel hydroxide as the main component, when the solution of nickel nitrate was impregnated, the second layer of cobalt hydroxide alone was dissolved, and in the subsequent neutralization step, nickel hydroxide was added to nickel hydroxide. It is considered that the current collector-like effect was reduced because the cobalt hydroxide was dispersed, and as a result, the active material utilization rate did not increase. From this, when forming a layer of cobalt compound alone, it is considered necessary to prevent it from mixing with the layer containing nickel hydroxide as the main component before and after it, so that the positive electrode plate should be prepared by the chemical impregnation method. In the case of manufacturing, it is necessary to form a second layer of cobalt hydroxide alone and then oxidize it to change it into a cobalt oxide that is difficult to dissolve in the impregnating liquid. However, this does not apply when the active material is filled by a method other than the chemical impregnation method, for example, when the active material is physically filled like a foamed electrode plate, and the active material is not required to be oxidized even if cobalt hydroxide is not oxidized. It has been confirmed that the active material utilization rate is high with a high packing density of the material.
なお、本実験では水酸化コバルトを酸化するのを電気化
学的に行なったが、これ以外の方法としては過酸化水素
水、次亜塩素酸ソーダ、過硫酸カリウムなどの酸化剤を
用いた場合や空気雰囲気下の熱処理によって酸化させた
場合も同様の結果が得られた。In this experiment, cobalt hydroxide was electrochemically oxidized, but other methods such as hydrogen peroxide solution, sodium hypochlorite, and potassium persulfate were used. Similar results were obtained when oxidized by heat treatment in an air atmosphere.
実験2 実験1で作製した極板群Aの中で活物質利用率の向上が
見られる試料のうちから、第2層目のコバルト化合物の
量が最も少ない0.6モル%の試料と最も多い10.0モル%
の試料を用い、化学含浸法の操作を1回行なってさらに
第4層目に水酸化コバルト単独の層を形成した正極板
(極板群C1およびC2とする)を作製し、実験1と同様に
して活物質利用率を測定した。第2図に活物質として充
填した水酸化ニッケル量に対する第4層目の水酸化コバ
ルトの割合と活物質利用率の関係を示す。第2図からわ
かるように、第2層目のコバルト化合物の量が0.6モル
%の極板群C1の場合、第4層目の水酸化コバルト量が0.
8〜7.0モル%の範囲で活物質利用率が高く、ほぼ100%
になっている。一方、第2層目のコバルト化合物の量が
10.0モル%の極板群C2の場合、利用率が100%近くにな
っているのは、第4層目の水酸化コバルト量が0.4〜6.0
モル%の範囲である。前記の実験1と今回の実験2の結
果からコバルト含有量の最適値を求めると、活物質とし
て充填された水酸化ニッケル量に対する第2層目のコバ
ルト化合物の含有量は0.6〜10.0モル%、第4層目のコ
バルト化合物の含有量は0.4〜7.0モル%の範囲で活物質
利用率の高い正極板が得られる。Experiment 2 Among the samples prepared in Experiment 1 in which the utilization rate of the active material was improved in the electrode plate group A, the sample containing 0.6 mol% of the smallest amount of cobalt compound in the second layer and the largest amount of 10.0 mol %
Using the above sample, the chemical impregnation method was performed once to prepare a positive electrode plate (electrode plates C1 and C2) on which a layer of cobalt hydroxide alone was formed as the fourth layer. Then, the utilization rate of the active material was measured. FIG. 2 shows the relationship between the ratio of cobalt hydroxide in the fourth layer to the amount of nickel hydroxide filled as the active material and the utilization rate of the active material. As can be seen from Fig. 2, in the case of the electrode plate group C1 in which the amount of the cobalt compound in the second layer is 0.6 mol%, the amount of cobalt hydroxide in the fourth layer is 0.
High utilization rate of active material in the range of 8 to 7.0 mol%, almost 100%
It has become. On the other hand, if the amount of cobalt compound in the second layer is
In the case of the electrode plate group C2 of 10.0 mol%, the utilization rate is close to 100% because the amount of cobalt hydroxide in the fourth layer is 0.4 to 6.0.
It is in the range of mol%. When the optimum value of the cobalt content is obtained from the results of the above Experiment 1 and this Experiment 2, the content of the cobalt compound in the second layer is 0.6 to 10.0 mol% with respect to the amount of nickel hydroxide filled as the active material, When the content of the cobalt compound in the fourth layer is in the range of 0.4 to 7.0 mol%, a positive electrode plate having a high utilization ratio of the active material can be obtained.
実験3 本実験では、前記実験1,2で説明した本発明品と公知技
術で述べた従来品の活物質利用率に及ぼす活物質充填密
度の影響について調べた。Experiment 3 In this experiment, the influence of the active material packing density on the active material utilization rate of the product of the present invention described in Experiments 1 and 2 and the conventional product described in the known art was examined.
本発明による正極板としては、実験1で作製した極板群
A(3層構造)の内、第2層目のコバルト化合物の量が
活物質として充填した水酸化ニッケル量に対し3モル%
である正極板(試料A′とする)と、実験2で作製した
試料C1,C2と同様の4層構造であり、第2層目のコバル
ト化合物の量が活物質として充填した水酸化ニッケル量
に対し3モル%であり、第4層目の水酸化コバルトの量
が同じく2モル%である正極板(試料C′とする)を用
いた。また従来品としては焼結基板上に水酸化ニッケル
の活物質層を形成した後、その表面に水酸化コバルトの
層を形成した正極板(試料Dとする)を用いた。表面の
水酸化コバルトの量は水酸化ニッケル量に対し3モル%
になるように調整した。As the positive electrode plate according to the present invention, in the electrode plate group A (three-layer structure) produced in Experiment 1, the amount of the cobalt compound in the second layer was 3 mol% with respect to the amount of nickel hydroxide filled as the active material.
And a positive electrode plate (referred to as sample A ′) and a four-layer structure similar to samples C1 and C2 prepared in Experiment 2, and the amount of the cobalt compound in the second layer is the amount of nickel hydroxide filled as the active material. On the other hand, a positive electrode plate (referred to as sample C ′) in which the amount of cobalt hydroxide in the fourth layer was 2 mol% was used. As a conventional product, a positive electrode plate (referred to as sample D) was used in which a nickel hydroxide active material layer was formed on a sintered substrate and then a cobalt hydroxide layer was formed on the surface thereof. The amount of cobalt hydroxide on the surface is 3 mol% with respect to the amount of nickel hydroxide
I adjusted it to be.
第3図は前記各試料極板の活物質充填密度と活物質利用
率との関係を示したものである。なお、横軸の活物質充
填密度は含浸した水酸化ニッケルと水酸化コバルトが各
々1電子反応に従うものとして算出した。FIG. 3 shows the relationship between the active material packing density of each sample electrode plate and the active material utilization rate. The active material packing density on the horizontal axis was calculated assuming that the impregnated nickel hydroxide and cobalt hydroxide each undergo a one-electron reaction.
第3図から明らかなように公知技術を基にして作製した
試料Dは活物質充填密度の増大にともなって活物質利用
率の低下が認められるのに対し、本発明による試料A′
及びC′では活物質利用率の低下がほとんど無く、従来
品よりも正極板の高容量化に適していることがわかる。
これは本発明品における活物質の集電性が従来品よりも
良好で且つ均一であることによるものと考えられる。As is clear from FIG. 3, the sample D prepared based on the known technique shows a decrease in the active material utilization rate with an increase in the active material packing density, whereas the sample A ′ according to the present invention.
It can be seen that C and C'are more suitable for increasing the capacity of the positive electrode plate than the conventional product, since there is almost no decrease in the active material utilization rate.
It is considered that this is because the current collector of the active material of the present invention is better and more uniform than the conventional one.
実験4 実験1〜3では第2層目及び第4層目のコバルト化合物
単独の層を形成するために硝酸コバルト単独の含浸液を
用いたが、本実験ではこの含浸液が硝酸コバルトと硝酸
ニッケルの混合物である場合について前記極板群Aと類
似の構造を持つ極板の活物質利用率を測定し、第2層目
及び第4層目として最低限必要なコバルト化合物の含有
率について求めた。試料極板としては活物質として充填
した水酸化ニッケル量に対する第2層目のコバルト化合
物の量を4モル%として極板(極板群Eとする)を化学
含浸法によって作製した。第2層目の活物質組成と活物
質利用率の関係を第4図に示す。第4図からわかるよう
に、活物質利用率は活物質組成によって影響を受けてお
り、活物質組成がコバルト化合物100モル%の時に活物
質利用率は最も高く、コバルト化合物の含有率が低下す
るに従い活物質利用率も低くなっている。そして活物質
組成がコバルト化合物70モル%の付近で活物質利用率の
低下が大きく、それ以下の含有率では第2層目のコバル
ト化合物を主成分とする層を形成した効果がほとんど無
い状態になっている。このことから活物質組成としては
少なくとも70モル%以上のコバルト化合物を含有し、出
来れば100モル%の組成であることが望ましい。Experiment 4 In Experiments 1 to 3, the impregnating solution of cobalt nitrate alone was used to form the second and fourth layers of the cobalt compound alone. In this experiment, the impregnating solution was cobalt nitrate and nickel nitrate. The active material utilization rate of the electrode plate having a structure similar to that of the electrode plate group A was measured for the case of the mixture of No. 1, and the content of the minimum required cobalt compound for the second layer and the fourth layer was determined. . As the sample electrode plate, an electrode plate (referred to as electrode plate group E) was prepared by the chemical impregnation method with the amount of the cobalt compound in the second layer being 4 mol% with respect to the amount of nickel hydroxide filled as the active material. FIG. 4 shows the relationship between the active material composition of the second layer and the active material utilization rate. As can be seen from FIG. 4, the active material utilization rate is influenced by the active material composition, and when the active material composition is 100 mol% of the cobalt compound, the active material utilization rate is the highest and the content rate of the cobalt compound decreases. As a result, the utilization rate of active materials is also decreasing. When the active material composition is around 70 mol% of the cobalt compound, the active material utilization rate is largely reduced, and when the content ratio is less than that, the effect of forming the second layer containing the cobalt compound as the main component is hardly obtained. Has become. From this, it is desirable that the active material composition contains at least 70 mol% or more of the cobalt compound, and if possible, the composition is 100 mol%.
実験5 本実験では含浸工程におけるニッケル焼結体の活物質化
の影響について検討するために2種類のニッケル焼結基
板を用意し、それに同一の含浸液を用い、同一の方法で
活物質を充填した極板の性能を調べた。用いたニッケル
焼結基板の1つは実験1〜4で用いたのと同じである、
ニッケルスラリーを金属性の集電体に塗布した後、還元
雰囲気下900℃で焼結した物(基板1とする)と、もう
1つは還元雰囲気下900℃で水蒸気を添加しながら焼結
した後、空気雰囲気下200℃で熱処理を行ない、ニッケ
ル焼結体の表面にニッケル酸化物の不働態皮膜を形成し
た物(基板2とする)である。この2つのニッケル焼結
基板を用い、実験1の極板群A(3層構造)と同様にし
て第2層目のコバルト化合物の量を4モル%とした正極
板を作製し、活物質利用率及び放電中間電位の放電レー
ト依存性を調べた結果が各々第5図と第6図である。な
お、ニッケル焼結体の表面にニッケル酸化物の不働態皮
膜を形成していない基板1を用いた極板をA1、ニッケル
酸化物を形成した基板2を用いた極板をA2とする。第5
図の活物質利用率の比較ではA1とA2の差は0.2CAの低率
放電においてはほとんど無いが、3CA,10CAのような高率
放電になるに従いその差は拡大している。これは第6図
の放電中間電位も同様の傾向であり、ニッケル焼結体表
面にニッケル酸化物の不働態皮膜を形成した極板A2はそ
うでないA1に比べ、従来考えられていたニッケル焼結体
の活物質化による極板強度の低下防止の他に、放電レー
ト依存性が小さく、高率放電での活物質利用率及び放電
電位特性の低下が少ないという新たな効果が見い出され
た。これはニッケル焼結体の表面に不働態皮膜を形成し
ない試料A1の場合、酸性の含浸液に腐蝕されてニッケル
鎖が細くなり導電性が低下することや、ニッケル焼結体
の表面積が減少して活物質との接触面積が減少すること
などによって、特に高率放電ほど性能低下が大きく現れ
ているためであると考えられる。このようなニッケル焼
結体の活物質化は化学含浸の工程中だけでなく、正極板
の充電における貴な電位でも起こることが知られてお
り、電池の実使用におけるニッケル焼結体の活物質化に
よって、極板性能が変化し、電池性能が徐々に低下する
ことが予想される。これに対し、不働態皮膜を形成した
試料A2では、酸性の含浸液によるニッケル焼結体の腐蝕
及び前記の正極板の充電によるニッケル焼結体の活物質
化が起こらないため、本来の良好な極板性能が持続して
得られる。つまり、本発明のサンドイッチ構造が本来持
つ効果を安定して得るためには、ニッケル焼結体の表面
にニッケル酸化物の不働態皮膜を形成して、活物質の含
浸工程及び正極板の充電によるニッケル焼結体の活物質
化を防ぐことが効果的である。Experiment 5 In this experiment, two types of nickel sintered substrates were prepared in order to study the effect of the nickel sintered body becoming an active material in the impregnation process, and the same impregnating liquid was used for filling the active material by the same method. The performance of the prepared electrode plate was investigated. One of the nickel sintered substrates used was the same as used in Experiments 1-4.
The nickel slurry was applied to a metallic current collector and then sintered at 900 ° C in a reducing atmosphere (referred to as substrate 1), and the other was sintered at 900 ° C in a reducing atmosphere while adding water vapor. After that, heat treatment was performed at 200 ° C. in an air atmosphere to form a nickel oxide passivation film on the surface of the nickel sintered body (referred to as a substrate 2). Using these two nickel sintered substrates, a positive electrode plate was prepared in which the amount of the cobalt compound in the second layer was 4 mol% in the same manner as in electrode plate group A (three-layer structure) of Experiment 1, and the active material was used. The results of examining the discharge rate dependence of the discharge rate and the discharge intermediate potential are shown in FIGS. 5 and 6, respectively. The electrode plate using the substrate 1 on which the nickel oxide passivation film is not formed on the surface of the nickel sintered body is A1, and the electrode plate using the substrate 2 on which the nickel oxide is formed is A2. Fifth
In the comparison of the active material utilization rates in the figure, there is almost no difference between A1 and A2 in the low rate discharge of 0.2 CA, but the difference increases as the high rate discharge of 3 CA, 10 CA is achieved. This is also the case with the discharge intermediate potential shown in Fig. 6. The electrode plate A2 with a nickel oxide passivation film formed on the surface of the nickel sintered body has a conventionally thought of nickel sintering compared to A1 without it. In addition to the prevention of the reduction of the electrode plate strength due to the active material of the body, a new effect was found that the discharge rate dependence was small, and the active material utilization rate and the discharge potential characteristics at a high rate discharge were small. This is because in the case of sample A1 that does not form a passive film on the surface of the nickel sintered body, it is corroded by the acidic impregnating solution and the nickel chain becomes thin and the conductivity decreases, and the surface area of the nickel sintered body decreases. It is considered that this is because the performance decrease is more remarkable especially at higher rate discharges due to a decrease in the contact area with the active material. It is known that such conversion of the nickel sintered body into the active material occurs not only during the chemical impregnation step, but also at the noble potential during charging of the positive electrode plate. It is expected that the electrode performance will change and the battery performance will gradually decrease. On the other hand, in the sample A2 on which the passivation film was formed, the corrosion of the nickel sintered body by the acidic impregnating solution and the activation of the nickel sintered body as the active material due to the charging of the positive electrode plate did not occur. The electrode plate performance can be obtained continuously. That is, in order to stably obtain the inherent effect of the sandwich structure of the present invention, a passive film of nickel oxide is formed on the surface of the nickel sintered body, and the active material is impregnated and the positive electrode plate is charged. It is effective to prevent the nickel sintered body from becoming an active material.
以上5つの実験の結果を基に、本発明による正極板と従
来品を実施例によって比較する。多孔性金属基板として
実験4で用いた焼結基板1及び2の2種類(多孔度85
%)とフォーム状ニッケル多孔体(多孔度95%)の計3
種類を用意した。Based on the results of the above five experiments, the positive electrode plate according to the present invention and the conventional product will be compared by examples. Two types of sintered metal substrates 1 and 2 (porosity 85
%) And foamed nickel porous body (porosity 95%) in total 3
Prepared types.
実施例1(本発明品) 焼結基板1に5.0モル/lの硝酸ニッケル水溶液を含浸さ
せ、濃縮後、熱アルカリで中和してニッケル焼結体の孔
中に水酸化ニッケルを充填するという通常の化学含浸法
の工程を3回行なって第1層目の水酸化ニッケルの層を
形成し、次に1.4モル/lの硝酸コバルト水溶液を用いて
化学含浸法の工程を1回行ない、第2層目の水酸化コバ
ルト単独の層を形成した後、比重1.250(20℃)KOH水溶
液中で、通電して水酸化コバルトを酸化した。この極板
を洗浄及び乾燥した後、第1層目の形成と同様にして、
化学含浸法の工程を5回行なって、第3層目の水酸化ニ
ッケル層を形成して正極板とした。これを試料Fとす
る。Example 1 (invention product) Sintered substrate 1 was impregnated with 5.0 mol / l nickel nitrate aqueous solution, concentrated, and neutralized with hot alkali to fill the pores of the nickel sintered body with nickel hydroxide. The normal chemical impregnation method is performed three times to form the first layer of nickel hydroxide, and then the chemical impregnation method is performed once using 1.4 mol / l cobalt nitrate aqueous solution. After forming the second layer of cobalt hydroxide alone, the cobalt hydroxide was oxidized by applying electricity in a KOH aqueous solution having a specific gravity of 1.250 (20 ° C.). After washing and drying this electrode plate, similarly to the formation of the first layer,
The step of the chemical impregnation method was performed 5 times to form a third layer of nickel hydroxide, and the positive electrode plate was obtained. This is designated as Sample F.
実施例2(本発明品) 焼結基板2を用いた以外は全て実施例1と同様にして正
極板とした。これを試料Gとする。Example 2 (Invention product) A positive electrode plate was prepared in the same manner as in Example 1 except that the sintered substrate 2 was used. This is designated as Sample G.
実施例3(本発明品) 実施例1で作製した試料Fを基にし、さらに2.2モル/l
の硝酸コバルト水溶液を用いて化学含浸法の工程を1回
行ない、第4層目の水酸化コバルト単独の層を形成して
正極板とした。これを試料Hとする。Example 3 (invention product) Based on the sample F prepared in Example 1, further 2.2 mol / l
The step of the chemical impregnation method was performed once using the cobalt nitrate aqueous solution described above to form a fourth layer of cobalt hydroxide alone as a positive electrode plate. This is designated as Sample H.
実施例4(本発明品) 実施例2で作製した試料Gを基にし、実施例3と同様の
方法で第4層目の水酸化コバルト単独の層を形成して正
極板とした。これを試料Iとする。Example 4 (Invention product) Based on the sample G prepared in Example 2, a fourth layer of cobalt hydroxide alone was formed as a positive electrode plate in the same manner as in Example 3. This is designated as Sample I.
実施例5(従来品) 焼結基板1に5.0モル/lの硝酸ニッケル水溶液を用いて
化学含浸法の工程を8回行ない、ニッケル焼結基板に水
酸化ニッケルを充填し、次に2.6モル/lの硝酸コバルト
水溶液を用い、化学含浸法の工程を1回行なって表面に
水酸化コバルト単独の層を形成して正極板とした。これ
を試料Jとする。Example 5 (conventional product) The process of chemical impregnation was performed 8 times on the sintered substrate 1 using a 5.0 mol / l nickel nitrate aqueous solution to fill the nickel sintered substrate with nickel hydroxide, and then 2.6 mol / l. Using the cobalt nitrate aqueous solution (1), the step of chemical impregnation was performed once to form a layer of cobalt hydroxide alone on the surface to obtain a positive electrode plate. This is designated as Sample J.
実施例6(従来品) 焼結基板1に(4.7モル硝酸ニッケル+0.3モル硝酸コバ
ルト)/lの水溶液を用いて化学含浸法の工程を8回行な
い、ニッケル焼結基板に水酸化ニッケルと水酸化コバル
トの混合物を充填して正極板とした。これを試料Kとす
る。Example 6 (Conventional product) A chemical impregnation process was performed 8 times using an aqueous solution of (4.7 mol nickel nitrate + 0.3 mol cobalt nitrate) / l on the sintered substrate 1 to form nickel hydroxide on the nickel sintered substrate. A positive electrode plate was prepared by filling a mixture of cobalt hydroxide. This is designated as Sample K.
実施例7(本発明品) 水酸化ニッケル粉末86部、カーボニルニッケル粉末10
部、金属コバルト粉末4部からなる200メッシュパスの
混合粉末に水とメチルセルロースを加えて活物質ペース
トとしたものを、多孔度95%のフォーム状ニッケル多孔
体に規定量の約50%の量だけ物理的に充填し、第1層目
の水酸化ニッケルを主成分とする層を形成した。次に、
1.4モル/lの硝酸コバルト水溶液を用いて化学含浸の工
程を1回行ない、第2層目の水酸化コバルト単独の層を
形成した後、第1層目の形成と同様にして残りの活物質
ペーストを充填し、第3層目の水酸化ニッケルを主成分
とする層を形成した。さらに後工程として、上記極板に
フッ素ディスパージョンを含浸させた後、乾燥とプレス
を行ない正極板とした。これを試料Lとする。Example 7 (product of the present invention) 86 parts of nickel hydroxide powder, 10 carbonyl nickel powders
Part, and a powder of 200 mesh pass consisting of 4 parts of metallic cobalt powder to form an active material paste by adding water and methylcellulose to a foam-like nickel porous body with a porosity of 95% in an amount of about 50% of the specified amount. Physical filling was performed to form a first layer containing nickel hydroxide as a main component. next,
After the chemical impregnation step was performed once using a 1.4 mol / l cobalt nitrate aqueous solution to form a second layer of cobalt hydroxide alone, the remaining active material was formed in the same manner as in the formation of the first layer. The paste was filled to form a third layer containing nickel hydroxide as a main component. Further, as a post-process, the above electrode plate was impregnated with fluorine dispersion, dried and pressed to obtain a positive electrode plate. This is designated as sample L.
実施例8(従来品) フォーム状ニッケル多孔体に実施例7で用いたのと同じ
活物質ペーストを同量充填しただけで水酸化コバルトの
層を形成しないで正極板とした。これを試料Mとする。Example 8 (conventional product) A positive electrode plate was prepared by filling the same amount of the same active material paste as that used in Example 7 in the foamed nickel porous body without forming a cobalt hydroxide layer. This is designated as sample M.
実施例9(従来品) 実施例8で作製した試料Mを元にし、さらに2.6モル/l
の硝酸コバルト水溶液を用いて化学含浸の工程を1回行
なって活物質表面に水酸化コバルト単独の層を形成し、
正極板とした。これを試料Nとする。Example 9 (conventional product) Based on the sample M prepared in Example 8, 2.6 mol / l was further added.
The step of chemical impregnation is performed once using the aqueous cobalt nitrate solution to form a layer of cobalt hydroxide alone on the surface of the active material,
The positive electrode plate was used. This is designated as Sample N.
以上のようにして作製した試料F〜Nの理論容量を表1
に、活物質組成を表2に示す。なお、理論容量は水酸化
ニッケル及び水酸化コバルトが1電子反応に従うものと
して算出した。The theoretical capacities of the samples F to N produced as described above are shown in Table 1.
Table 2 shows the active material composition. The theoretical capacity was calculated assuming that nickel hydroxide and cobalt hydroxide follow a one-electron reaction.
次に各試料を40×40(mm)の寸法に切断し、過剰の比重
1.250(20℃)KOH水溶液中で同寸法の焼結式カドミウム
負極板2枚を対極として用いて充放電を行ない、活物質
利用率と放電電位特性の放電レート依存性を調べた。な
お、1サイクル目の化成充電は0.1CAの電流で理論容量
の160%,2サイクル目以後は0.2CAの電流で120%まで行
ない、放電は全て酸化水銀電極基準OVまでとした。第7
図は焼結基板を用い化学含浸法によって活物質を充填し
た試料F〜Kの活物質利用率の放電レート依存性を調べ
た結果で、利用率の高い物から1>H>G>F>J>K
の順になっており、2つの水酸化ニッケルの層の間に水
酸化コバルトを酸化した層を形成し、サンドイッチ構造
とした本発明品I,H,G,Fは従来品J,Kに比べ、利用率が明
らかに向上している。また3CA,10CAといった高率放電に
おいては、本発明品と従来品の差はさらに拡大してい
る。この傾向は放電電位特性について調べた第8図でも
同様である。また活物質を4層構造にした試料I,Hは3
層構造の試料F,Gに比べ、活物質利用率の向上が見ら
れ、ニッケル焼結体の表面にニッケル酸化物の不働態皮
膜を形成した試料I,Gはそうでない試料F,Hに比べ、主に
放電電位特性の向上が認められる。なお、第8図におい
て試料Kの電位が0.2CAの低率放電でも低いのは、活物
質中に分散している水酸化コバルトの含有量が他の試料
に比べ多いことが原因と考えられる。 Next, cut each sample to a size of 40 × 40 (mm) and
Charge and discharge were performed using two sintered cadmium negative electrode plates of the same size in a 1.250 (20 ° C) KOH aqueous solution as counter electrodes, and the discharge rate dependence of the active material utilization rate and discharge potential characteristics was investigated. The formation charge in the first cycle was performed at a current of 0.1 CA to 160% of the theoretical capacity and after the second cycle was performed at a current of 0.2 CA to 120%, and the discharge was performed up to the mercury oxide electrode reference OV. 7th
The figure shows the results of examining the discharge rate dependence of the active material utilization rate of Samples F to K filled with the active material by a chemical impregnation method using a sintered substrate. From the highest utilization rate, 1>H>G>F>J> K
In this order, the present invention products I, H, G, and F, which have a sandwich structure in which a layer obtained by oxidizing cobalt hydroxide is formed between two nickel hydroxide layers, are compared with the conventional products J and K. The utilization rate is clearly improving. Further, in the high rate discharge of 3 CA and 10 CA, the difference between the product of the present invention and the conventional product is further widened. This tendency is the same in FIG. 8 in which the discharge potential characteristics are examined. Samples I and H, which have a 4-layer structure of the active material, have 3
Compared to the layered samples F and G, the utilization rate of the active material was improved, and the samples I and G with the nickel oxide passivation film formed on the surface of the nickel sintered body were compared with the samples F and H that did not. , Mainly the improvement of discharge potential characteristics is observed. In FIG. 8, the reason why the potential of Sample K is low even at a low rate discharge of 0.2 CA is considered to be because the content of cobalt hydroxide dispersed in the active material is higher than that of the other samples.
またフォーム状ニッケル多孔体に活物質を物理的に充填
した試料L〜Nの性能を示したのが、第9図及び第10図
で、前記の焼結式極板の性能を示した第7図及び第8図
と同様の傾向を示しており、本発明品である試料Lは従
来品の試料M及びNよりも高率放電時の活物質利用率及
び放電電位特性が良好であることがわかる。Further, the performance of Samples L to N obtained by physically filling the foam-like nickel porous body with the active material is shown in FIGS. 9 and 10, and the performance of the sintered electrode plate is shown in FIG. The same tendency as in FIGS. 8 and 9 is shown, and the sample L which is the product of the present invention has better active material utilization rate and discharge potential characteristics at the time of higher rate discharge than the samples M and N of the conventional products. Recognize.
このように化学含浸法以外の方法で活物質を充填する場
合には、第2層目の水酸化コバルトを酸化せずとも活物
質充填密度の高い状態において良好な放電特性が得られ
た。Thus, when the active material was filled by a method other than the chemical impregnation method, good discharge characteristics were obtained in a state where the active material filling density was high without oxidizing the second layer of cobalt hydroxide.
以上のように本発明品は従来の物に比べ、その放電特性
が明らかに良好である。As described above, the discharge property of the present invention product is clearly better than that of the conventional product.
発明の効果 前記実施例において示したように、本発明に基づき、水
酸化ニッケルを主成分とする2つの層の間にサンドイッ
チ構造的に水酸化コバルトあるいはコバルト酸化物を主
成分とする層を形成した3層の活物質構造にすることに
よって、従来の物より放電特性のすぐれたアルカリ蓄電
池用ニッケル正極板を得ることができる。また前記3層
構造の上に第4層目として水酸化コバルトを主成分とす
る層を形成することによって、活物質利用率はさらに数
%向上することが可能である。またこれらの本発明が本
来持つ効果を安定的に得るには多孔性金属基板の表面に
金属酸化物の不働態皮膜を形成することが効果的で、こ
れによってさらに良好な放電特性が得られる。EFFECTS OF THE INVENTION As shown in the above examples, according to the present invention, a layer containing cobalt hydroxide or cobalt oxide as a main component is sandwiched between two layers containing nickel hydroxide as a main component. By using the three-layer active material structure described above, it is possible to obtain a nickel positive electrode plate for alkaline storage batteries, which has better discharge characteristics than the conventional one. Further, by forming a layer containing cobalt hydroxide as a main component as the fourth layer on the three-layer structure, the utilization factor of the active material can be further improved by several percent. Further, in order to stably obtain these inherent effects of the present invention, it is effective to form a passivation film of a metal oxide on the surface of the porous metal substrate, and thereby a better discharge characteristic can be obtained.
第1図は含浸増量に対する第2層目のコバルト含有量と
活物質利用率の関係を示す図、第2図は含浸増量に対す
る第4層目のコバルト含有量と活物質利用率の関係を示
す図、第3図は本発明のニッケル正極板と従来品との活
物質充填密度に対する活物質利用率を比較して示す図、
第4図は第2層目及び第4層目の活物質組成と活物質利
用率の関係を示す図、第5図は活物質利用率の放電レー
ト依存性に及ぼすニッケル焼結基板表面の影響を示す
図、第6図は放電電位特性の放電レート依存性に及ぼす
ニッケル焼結基板表面の影響を示す図、第7図及び第9
図は本発明のニッケル正極板と従来品との活物質利用率
の放電レート依存性を比較して示す図、第8図及び第10
図は本発明のニッケル正極板と従来品との放電電位特性
の放電レート依存性を比較して示す図である。FIG. 1 shows the relationship between the cobalt content of the second layer and the active material utilization rate with respect to the impregnation increase, and FIG. 2 shows the relationship between the cobalt content of the fourth layer and the active material utilization rate with respect to the impregnation increase. FIGS. 3A and 3B are diagrams showing a comparison of the active material utilization rate with respect to the active material packing density of the nickel positive electrode plate of the present invention and a conventional product,
FIG. 4 is a diagram showing the relationship between the active material composition of the second and fourth layers and the active material utilization rate, and FIG. 5 is the effect of the nickel sintered substrate surface on the discharge rate dependence of the active material utilization rate. And FIG. 6 are views showing the influence of the nickel sintered substrate surface on the discharge rate dependence of the discharge potential characteristics, FIG. 7, and FIG.
The figures compare the discharge rate dependence of the active material utilization rate between the nickel positive electrode plate of the present invention and the conventional product, FIG. 8, FIG.
The figure compares the nickel positive electrode plate of the present invention and the conventional product in comparison with the discharge rate dependence of the discharge potential characteristics.
Claims (10)
分とする正極活物質層を形成させたニッケル正極板にお
いて、その正極活物質層が以下の構造であるもの、即
ち、多孔性金属基板上の第1層目は水酸化ニッケルを主
成分とする層であり、第2層目は水酸化コバルトあるい
はコバルト酸化物を主成分とする層であり、さらにその
上の第3層目は水酸化ニッケルを主成分とする層である
もの、つまり水酸化ニッケルを主成分とする2つの層の
間にサンドイッチ構造的に水酸化コバルトあるいはコバ
ルト酸化物を主成分とする層を形成したことを特徴とす
るアルカリ蓄電池用ニッケル正極板。1. A nickel positive electrode plate in which a positive electrode active material layer containing nickel hydroxide as a main component is formed on a porous metal substrate, and the positive electrode active material layer has the following structure, that is, a porous metal. The first layer on the substrate is a layer containing nickel hydroxide as a main component, the second layer is a layer containing cobalt hydroxide or cobalt oxide as a main component, and the third layer thereabove is What is a layer containing nickel hydroxide as a main component, that is, a layer containing cobalt hydroxide or cobalt oxide as a main component is sandwiched between two layers containing nickel hydroxide as a main component. Characteristic nickel positive electrode plate for alkaline storage batteries.
バルト酸化物を主成分とする層に含まれるコバルト化合
物の量が水酸化ニッケルの量に対し、0.6〜10.0モル%
である特許請求範囲第(1)項記載のアルカリ蓄電池用
ニッケル正極板。2. The amount of cobalt compound contained in the second layer containing cobalt hydroxide or cobalt oxide as a main component is 0.6 to 10.0 mol% with respect to the amount of nickel hydroxide.
The nickel positive electrode plate for alkaline storage batteries according to claim (1).
バルト酸化物を主成分とする層のコバルト化合物の含有
量が70モル%以上である特許請求の範囲第(1)項記載
のアルカリ蓄電池用ニッケル正極板。3. The alkaline storage battery according to claim 1, wherein the content of the cobalt compound in the second layer containing cobalt hydroxide or cobalt oxide as a main component is 70 mol% or more. Nickel positive electrode plate.
態皮膜を形成したことを特徴とする特許請求の範囲第
(1)項記載のアルカリ蓄電池用ニッケル正極板。4. A nickel positive electrode plate for an alkaline storage battery according to claim 1, wherein a passivation film of a metal oxide is formed on the surface of the porous metal substrate.
る酸化溶液を含浸した後、濃縮、アルカリ処理を行なう
という通常の化学含浸の工程を数回行なって多孔性金属
基板上に第1層目の水酸化ニッケルを主成分とする層を
形成し、次にコバルト塩が主成分である酸性溶液を用い
て化学含浸の工程を少なくとも1回以上行なって第2層
目の水酸化コバルトを主成分とする層を形成した後、電
気化学的あるいは化学的に酸化して前記水酸化コバルト
が主成分である層をコバルト酸化物が主成分である層に
変化させ、さらに第1層目の形成と同様にして化学含浸
の工程を数回行なって第3層目として水酸化ニッケルを
主成分とする層を形成することを特徴とするアルカリ蓄
電池用ニッケル正極板の製造法。5. The ordinary chemical impregnation step of impregnating a porous metal substrate with an oxidizing solution containing nickel salt as a main component, followed by concentration and alkali treatment is repeated several times to form a first layer on the porous metal substrate. A second layer of cobalt hydroxide is formed by forming a second layer of nickel hydroxide as a main component, and then performing a chemical impregnation step at least once using an acidic solution containing a cobalt salt as a main component. After the layer containing the main component is formed, it is electrochemically or chemically oxidized to change the layer containing cobalt hydroxide as a main component into a layer containing cobalt oxide as a main component. A method for producing a nickel positive electrode plate for an alkaline storage battery, which comprises performing a chemical impregnation step several times in the same manner as forming to form a layer containing nickel hydroxide as a main component as a third layer.
分とする正極活物質層を形成させたニッケル正極板にお
いて、その正極活物質層が以下の構造であるもの、即
ち、多孔性金属基板上の第1層目は水酸化ニッケルを主
成分とする層であり、第2層目は水酸化コバルトあるい
はコバルト酸化物を主成分とする層であり、第3層目は
水酸化ニッケルを主成分とする層であり、さらにその上
の第4層目は水酸化コバルトを主成分とする層であるも
の、つまり水酸化ニッケルを主成分とする層とコバルト
化合物を主成分とする層が交互に積層していることを特
徴とするアルカリ蓄電池用ニッケル正極板。6. A nickel positive electrode plate in which a positive electrode active material layer containing nickel hydroxide as a main component is formed on a porous metal substrate, wherein the positive electrode active material layer has the following structure, that is, a porous metal. The first layer on the substrate is a layer containing nickel hydroxide as a main component, the second layer is a layer containing cobalt hydroxide or cobalt oxide as a main component, and the third layer is a layer containing nickel hydroxide. The layer containing the main component, and the fourth layer on top of it is the layer containing cobalt hydroxide as the main component, that is, the layer containing nickel hydroxide as the main component and the layer containing the cobalt compound as the main component. A nickel positive electrode plate for an alkaline storage battery, characterized by being alternately laminated.
バルト酸化物を主成分とする層に含まれるコバルト化合
物の量が水酸化ニッケルの量に対し、0.6〜10.0モル%
である特許請求の範囲第(6)項記載のアルカリ蓄電池
用ニッケル正極板。7. The amount of cobalt compound contained in the second layer containing cobalt hydroxide or cobalt oxide as a main component is 0.6 to 10.0 mol% with respect to the amount of nickel hydroxide.
The nickel positive electrode plate for an alkaline storage battery according to claim (6).
する層に含まれる水酸化コバルトの量が、水酸化ニッケ
ルの量に対し、0.4〜7.0モル%である特許請求の範囲第
(6)項記載のアルカリ蓄電池用ニッケル正極板。8. The amount of cobalt hydroxide contained in the fourth layer containing cobalt hydroxide as a main component is 0.4 to 7.0 mol% with respect to the amount of nickel hydroxide. A nickel positive electrode plate for an alkaline storage battery according to the item (6).
トあるいは酸化コバルトを主成分とする層のコバルト化
合物の含有量が70モル%以上である特許請求の範囲第
(6)項記載のアルカリ蓄電池用ニッケル正極板。9. The content of the cobalt compound in the second and fourth layers containing cobalt hydroxide or cobalt oxide as a main component is 70 mol% or more, claim (6). A nickel positive electrode plate for an alkaline storage battery as described above.
働態皮膜を形成したことを特徴とする特許請求の範囲第
(6)項記載のアルカリ蓄電池用ニッケル正極板。10. The nickel positive electrode plate for an alkaline storage battery according to claim 6, wherein a passivation film of a metal oxide is formed on the surface of the porous metal substrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60213182A JPH0677452B2 (en) | 1985-09-25 | 1985-09-25 | Nickel positive electrode plate for alkaline storage battery and manufacturing method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60213182A JPH0677452B2 (en) | 1985-09-25 | 1985-09-25 | Nickel positive electrode plate for alkaline storage battery and manufacturing method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6271168A JPS6271168A (en) | 1987-04-01 |
| JPH0677452B2 true JPH0677452B2 (en) | 1994-09-28 |
Family
ID=16634900
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60213182A Expired - Lifetime JPH0677452B2 (en) | 1985-09-25 | 1985-09-25 | Nickel positive electrode plate for alkaline storage battery and manufacturing method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0677452B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62103972A (en) * | 1985-10-30 | 1987-05-14 | Shin Kobe Electric Mach Co Ltd | Manufacture of cathode plate for alkaline storage battery |
| JPH01272050A (en) * | 1988-04-21 | 1989-10-31 | Yuasa Battery Co Ltd | Nickel electrode for alkaline battery |
| JP2609911B2 (en) * | 1988-10-19 | 1997-05-14 | 三洋電機株式会社 | Alkaline storage battery |
| JP3533032B2 (en) * | 1996-04-03 | 2004-05-31 | 松下電器産業株式会社 | Alkaline storage battery and its manufacturing method |
| EP1006598A3 (en) * | 1998-11-30 | 2006-06-28 | SANYO ELECTRIC Co., Ltd. | Nickel electrodes for alkaline secondary battery and alkaline secondary batteries |
| US6193871B1 (en) * | 1998-12-09 | 2001-02-27 | Eagle-Picher Industries, Inc. | Process of forming a nickel electrode |
| JP5577541B2 (en) * | 2008-03-07 | 2014-08-27 | 公立大学法人首都大学東京 | Electrode active material filling method and manufacturing method of all solid state battery |
-
1985
- 1985-09-25 JP JP60213182A patent/JPH0677452B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6271168A (en) | 1987-04-01 |
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