JPH0656762B2 - Nickel positive electrode plate for alkaline storage battery - Google Patents
Nickel positive electrode plate for alkaline storage batteryInfo
- Publication number
- JPH0656762B2 JPH0656762B2 JP61055813A JP5581386A JPH0656762B2 JP H0656762 B2 JPH0656762 B2 JP H0656762B2 JP 61055813 A JP61055813 A JP 61055813A JP 5581386 A JP5581386 A JP 5581386A JP H0656762 B2 JPH0656762 B2 JP H0656762B2
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- positive electrode
- electrode plate
- active material
- discharge
- 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
- H01M4/24—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、超高率放電における特性が非常に良好であ
り、またサイクルの進行に伴なう性能低下がほとんど起
きない高性能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 The present invention relates to a nickel positive electrode for a high-performance alkaline storage battery, which has very good characteristics in ultra-high-rate discharge and hardly causes performance deterioration with the progress of cycles. It is about boards.
従来の技術 従来、アルカリ蓄電池に用いられるニッケル正極板の多
くは、カーボニルニッケル粉末を還元雰囲気下で焼結し
た多孔性のニッケル焼結基板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。2. Description of the Related Art Conventionally, many nickel positive electrode plates used in alkaline storage batteries are concentrated by impregnating a porous nickel sintered substrate obtained by sintering carbonyl nickel powder in a reducing atmosphere with an acidic solution containing nickel salt as a main component. After that, it is manufactured by a method of immersing in a hot alkaline solution and filling the positive electrode active material containing nickel hydroxide as a main component into the holes of the nickel substrate.
また最近、ニッケル正極板の性能改良について2つのこ
とが提案されている。その1つは、正極活物質中に水酸
化ニッケルと固溶体を形成しないコバルト化合物を含有
させることである。この方法によると放電時の活物質利
用率を従来のものより10〜15%程度高くすることが可能
である。例えば、従来の正極板では1CA放電の活物質
利用率が約70〜80%であったのに対し、前記の改良法で
は約85〜90%になるため正極板の高容量化に有利であ
る。もう1つは、ニッケル焼結体の表面にニッケル酸化
物の層を形成させることである。例えば、ニッケル酸化
物の層を形成していないニッケル焼結基板を用い、化学
含浸法によって活物質を充填した場合、酸性の含浸液に
よってニッケル焼結体が腐食されて、極板の機械的強度
が低下する。しかし、前記改良技術に基づきニッケル焼
結体の表面にニッケル酸化物の層を形成した場合は、前
記した如きニッケル焼結体の腐食を防ぐことが可能であ
る。Recently, two proposals have been made for improving the performance of nickel positive electrode plates. One is to incorporate a cobalt compound that does not form a solid solution with nickel hydroxide into the positive electrode active material. According to this method, the utilization rate of the active material at the time of discharging can be increased by about 10 to 15% as compared with the conventional one. For example, the conventional positive electrode plate has an active material utilization rate of about 70 to 80% for 1 CA discharge, whereas the improved method described above is about 85 to 90%, which is advantageous for increasing the capacity of the positive electrode plate. . The other is to form a nickel oxide layer on the surface of the nickel sintered body. For example, when a nickel sintered substrate without a nickel oxide layer is used and the active material is filled by the chemical impregnation method, the nickel impregnated body is corroded by the acidic impregnating solution, resulting in the mechanical strength of the electrode plate. Is reduced. However, when the nickel oxide layer is formed on the surface of the nickel sintered body based on the improved technique, it is possible to prevent the corrosion of the nickel sintered body as described above.
発明が解決しようとする問題点 以上の改良がなされた結果、最近のニッケル正極板は従
来のものに比べて性能が向上しているものの、このとこ
ろ需要が急増している電動工具の動力源として用いる場
合のような超高率放電用としてはまだ性能的に不充分で
ある。例えば、電動工具の用途では、アルカリ蓄電池の
放電々流が30CA程度を必要とする。このような条件で
は前記した如き改良がなされた最近のニッケル正極板で
あっても放電時の分極が相当大きくなり、蓄電池の端子
電圧が起大きく低下する。また活物質利用率も同様であ
る。Problems to be Solved by the Invention As a result of the above improvements, the recent nickel positive electrode plate has improved performance as compared with the conventional one, but as a power source for power tools whose demand is rapidly increasing recently. Performance is still insufficient for ultra high rate discharge such as when used. For example, in electric power tool applications, the discharge current of an alkaline storage battery requires about 30 CA. Under such a condition, even in the recent nickel positive electrode plate which has been improved as described above, the polarization at the time of discharge becomes considerably large, and the terminal voltage of the storage battery significantly decreases. The same applies to the active material utilization rate.
問題点を解決するための手段 本発明は前記のような超高率放電における活物質利用率
と放電々位の低下が非常に小さく、かつ高容量であるニ
ッケル正極板に関するものであり、その構造としては活
物質中に水酸化ニッケルと固溶体を形成しないコバルト
化合物を含有しており、さらに活物質を保持しているニ
ッケル多孔体の表面に平均厚み5〜70Åのニッケル酸化
物の層が存在することを特徴とするものである。Means for Solving the Problems The present invention relates to a nickel positive electrode plate having a very small decrease in utilization rate of active material and discharge potential in the ultra-high-rate discharge as described above and having a high capacity. As the active material contains a cobalt compound that does not form a solid solution with nickel hydroxide, and a nickel oxide layer having an average thickness of 5 to 70Å is present on the surface of the nickel porous body which holds the active material. It is characterized by that.
作 用 ニッケル正極板はカドミウム負極板よりも活物質利用率
の放電レート依存性は小さく良好であるが、先に述べた
ような電動工具などの超高率放電の用途においてはさら
に良好な放電レート依存性が求められる。これは活物質
利用率だけでなく放電々位についても同様である。The working nickel positive electrode plate has a smaller dependence on the discharge rate of the active material utilization rate than the cadmium negative electrode plate, and is good, but it has a better discharge rate in the applications of ultra-high-rate discharge such as the power tools described above. Dependency is required. This applies not only to the utilization rate of the active material but also to the discharge potential.
先に述べた2つの改良技術のうち、活物質利用率を向上
させる方法、即ち、水酸化ニッケルと固溶体を形成しな
いコバルト化合物を活物質中に含有させるという方法は
その効果の大きさ故に注目されたが、もう1つのニッケ
ル焼結基板の表面にニッケル酸化物の層を形成すること
重要視されなかった。その理由は次のようなことのため
である。化学含浸法によって活物質を充填する場合、ニ
ッケルを主とする酸性金属塩溶液の含浸、中和、そして
乾燥といった一連の工程を数回繰返すことを必要とする
が、製造コストの点でその回数を少なくすることが望ま
れていた。そのため、従来は故意にニッケル焼結体を腐
食させて活物質化し、活物質の充填量を多くしていた。
ニッケル焼結体の表面にニッケル酸化物の層を形成して
防食することは、これに逆行することであり、コストア
ップの要因になる。Among the above-mentioned two improved techniques, the method of improving the utilization rate of the active material, that is, the method of incorporating a cobalt compound which does not form a solid solution with nickel hydroxide into the active material is noted for its great effect. However, the formation of a nickel oxide layer on the surface of another nickel sintered substrate was not emphasized. The reason is as follows. When the active material is filled by the chemical impregnation method, it is necessary to repeat a series of steps such as impregnation, neutralization, and drying of an acidic metal salt solution mainly containing nickel, which is the number of times in terms of manufacturing cost. It was desired to reduce the Therefore, conventionally, the nickel sintered body has been intentionally corroded into an active material, and the amount of the active material filled has been increased.
Forming a layer of nickel oxide on the surface of the nickel sintered body to prevent corrosion is against this, and causes a cost increase.
本発明者はこの防食についても詳細に検討したところ、
含浸工程でニッケル焼結体の腐食を防ぐことと共に、ニ
ッケル正極板の製造工程が終了した時点、つまりニッケ
ル正極板の構造としてニッケル焼結体表面に存在するニ
ッケル酸化物の厚みがその放電性能に対し、非常に重量
な効果を及ぼすことを見い出した。つまり、ニッケル焼
結体の表面に平均厚み5〜70Åのニッケル酸化物の層を
有するニッケル正極板は活物質利用率及び放電々位の放
電レート存在性が小さく非常に良好であり、30CAのよ
うな超高率放電での性能低下が小さいことを見い出し
た。The present inventor has also examined this anticorrosion in detail,
In addition to preventing corrosion of the nickel sintered body in the impregnation process, the thickness of the nickel oxide present on the surface of the nickel sintered body as the structure of the nickel positive electrode plate, which is the time when the manufacturing process of the nickel positive electrode plate is completed, affects its discharge performance. On the other hand, it has been found to have a very heavy effect. In other words, a nickel positive electrode plate having a nickel oxide layer with an average thickness of 5 to 70Å on the surface of a nickel sintered body has very small active material utilization rate and discharge rate existence at discharge level, and is very good. It was found that the performance degradation at such a very high rate discharge was small.
また上記のニッケルの正極板の活物質中に水酸化ニッケ
ルと固溶体を形成しないコバルト化合物を含有させた場
合、相乗的に正極板の放電性能がさらに良好になり、超
高率放電の用途に適していることがわかった。Further, when a nickel compound and a cobalt compound which does not form a solid solution are contained in the active material of the positive electrode plate of nickel described above, synergistically the discharge performance of the positive electrode plate is further improved, which is suitable for use in ultra-high rate discharge. I found out.
ニッケル酸化物層の厚みが5Å未満あるいは70Åを越え
る場合は超高率放電の用途に適していない。例えば5Å
未満の場合、正極板の初期性能は良好であるが充放電サ
イクルの進行に伴ない性能は徐々に低下する。この要因
の1つとしては、ニッケル焼結体の活物質化による次の
ような影響が考えられる。第1に含浸工程で外部から充
填する活物質の組成は通常水酸化ニッケルを主成分とす
るニッケル、コバルト及びカドミウムの混合物である
が、これはニッケル単独の場合に比べ正極板の充電効率
や放電時の活物質利用率などが良好なためである。とこ
ろがニッケル焼結体の腐食によって生成するのは水酸化
ニッケルだけである。つまり集電体であるニッケル焼結
体と充填した活物質の間に充電効率や放電時の活物質利
用率の低い水酸化ニッケル単独の活物質の層が生成する
ため、極板の性能を低下させていることが考えられる。
また活物質の組成が異なるため、電流分布が不均一にな
ることも考えられる。また第2に集電体であるニッケル
焼結体が減少することによる集電性能の低下である。こ
のような問題点は焼結式正極板に限ったことではなく、
非焼結式も同様である。If the thickness of the nickel oxide layer is less than 5Å or exceeds 70Å, it is not suitable for ultra high rate discharge. For example, 5Å
When it is less than the above, the initial performance of the positive electrode plate is good, but the performance gradually decreases as the charge / discharge cycle progresses. As one of the factors, it is considered that the nickel sintered body is made into an active material as follows. First, the composition of the active material to be filled from the outside in the impregnation step is usually a mixture of nickel, cobalt and cadmium whose main component is nickel hydroxide. This is because the active material utilization rate at that time is good. However, only nickel hydroxide is produced by the corrosion of the nickel sintered body. In other words, an active material layer of nickel hydroxide alone, which has low charge efficiency and utilization rate of the active material at the time of discharge, is formed between the nickel sintered body which is the current collector and the filled active material, so that the performance of the electrode plate is deteriorated. It is possible that
Further, it is considered that the current distribution becomes non-uniform because the composition of the active material is different. Secondly, there is a decrease in current collecting performance due to a decrease in the amount of nickel sintered body which is a current collector. Such problems are not limited to the sintering type positive electrode plate,
The same applies to the non-sintered type.
一方、ニッケル酸化物層の厚みが70Åを超えた正極板は
初期からその放電性能が低下している。この原因の1つ
としては、ニッケル酸化物層が厚くなると本来絶縁体で
あるニッケル酸化物の性質が顕著に現われ、活物質と集
電体であるニッケル焼結基板との接触抵抗が大きく起な
ることが考えられる。On the other hand, the discharge performance of the positive electrode plate having a nickel oxide layer thickness of more than 70 Å has deteriorated from the beginning. One of the causes for this is that as the nickel oxide layer becomes thicker, the nature of the nickel oxide, which is originally an insulator, appears remarkably, and the contact resistance between the active material and the nickel sintered substrate, which is the current collector, becomes large. It is possible.
実施例 以下、本発明の実施例及びその効果を従来例と比較して
説明する。Example Hereinafter, an example of the present invention and its effect will be described in comparison with a conventional example.
実験1 先ず、ニッケル焼結基板として以下に説明する2種類の
ものを用い、そして以下に示す本発明によるニッケル正
極板及び従来のニッケル正極板をそれぞれ作製した。Experiment 1 First, two types of nickel sintered substrates described below were used, and a nickel positive electrode plate according to the present invention and a conventional nickel positive electrode plate described below were prepared.
カーボニルニッケル粉末をメチルセルロース及び水と混
練してニッケルスラリーとなし、このニッケルスラリー
をニッケルメッキした穿孔鋼板に塗布、乾燥した後、水
蒸気を含む還元雰囲気下 900℃で焼結し、ニッケル焼結
基板を作製した。これを基板Aとする。さらに基板Aを
空気雰囲気下 250℃で加熱処理し、ニッケル焼結体の表
面にニッケル酸化物の層を有するニッケル焼結基板を作
製した。これを基板Bとする。なお、基板Bのニッケル
酸化物層の平均厚みは約80Åであったが、熱処理の条件
を変更することによって酸化物層の厚みを自由に変える
ことができる。Carbonyl nickel powder is kneaded with methylcellulose and water to form a nickel slurry.This nickel slurry is applied to a nickel-plated perforated steel sheet, dried, and then sintered at 900 ° C in a reducing atmosphere containing water vapor to form a nickel sintered substrate. It was made. This is substrate A. Further, the substrate A was heat-treated at 250 ° C. in an air atmosphere to prepare a nickel sintered substrate having a nickel oxide layer on the surface of the nickel sintered body. This is substrate B. The average thickness of the nickel oxide layer of the substrate B was about 80Å, but the thickness of the oxide layer can be freely changed by changing the heat treatment conditions.
正極板A(従来品)ニッケル,コバルト,カドミウムの
比が95:2:3である各硝酸塩の混合水溶液にニッケル
酸化物層を形成していない基板Aを浸漬し、次いで濃
縮、中和を行なうという通常の化学含浸の工程を数回繰
返して作製した。Positive electrode plate A (conventional product) Substrate A on which a nickel oxide layer is not formed is immersed in a mixed aqueous solution of each of the nitrates in which the ratio of nickel, cobalt and cadmium is 95: 2: 3, and then concentrated and neutralized. The ordinary chemical impregnation process was repeated several times to produce the film.
正極板B(従来品)正極板Aを用い、さらに硝酸コバル
ト単独の溶液で通常の化合物含浸の工程を1回行なって
活物質中に単独の水酸化コバルトを生成させて作製し
た。Positive electrode plate B (conventional product) A positive electrode plate A was used, and a normal compound impregnation process was further performed once with a solution of cobalt nitrate alone to produce cobalt hydroxide alone in the active material.
正極板C(従来品)正極板Aにおける基板Aの代わりに
平均厚みが80Åのニッケル酸化物の層を有する基板Bを
用いた以外は全て正極板Aと同様の方法で作製した。Positive electrode plate C (conventional product) All were prepared in the same manner as the positive electrode plate A except that the substrate A having a nickel oxide layer having an average thickness of 80Å was used instead of the substrate A in the positive electrode plate A.
正極板D(本発明品)正極板Bにおける基板Aの代わり
に平厚みが80Åのニッケル酸化物の層を有する基板Bを
用いた以外は全て正極板Bと同様の方法で作製した。Positive Electrode Plate D (Product of the Present Invention) A positive electrode plate B was produced in the same manner as in the positive electrode plate B, except that a substrate B having a nickel oxide layer having a flat thickness of 80 Å was used in place of the substrate A.
なお、活物質の含浸工程終了御に測定した正極板C及び
Dのニッケル酸化物層の平均厚みは両方とも約60Åであ
った。また正極板A及びBでは活物質の含浸工程中にニ
ッケル焼結体の20%が腐食していた。また活物質中に単
独の水酸化コバルトを含有している正極板B及びDにつ
いては、そのコバルト化合物の添加量によって正極板の
放電性能が影響を受けることがわかっており、すでにコ
バルト化合物の適正な配合量を確認しているので、その
適正な配合量とした。例えばニッケル焼結体表面にニッ
ケル酸化物層を形成していない正極板では、単独のコバ
ルト化合物の量が水酸化ニッケルの量に対し、 2.0〜
8.0モル%の場合に放電性能が良好である。正極板Bの
場合は5モル%の量になるようにしてある。一方、ニッ
ケル焼結体表面にニッケル酸化物層を有する正極板で
は、単独のコバルト化合物量が水酸化ニッケル量に対
し、 0.4〜 7.0モル%の場合に放電性能が良好である。
正極板Dや後で述べる実験2においては 4.2モル%の量
になるようにしてある。The average thickness of the nickel oxide layers of the positive electrode plates C and D measured at the end of the step of impregnating the active material were both about 60Å. Further, in the positive electrode plates A and B, 20% of the nickel sintered body was corroded during the step of impregnating the active material. Further, regarding the positive electrode plates B and D in which the active material contains a single cobalt hydroxide, it is known that the discharge performance of the positive electrode plate is affected by the addition amount of the cobalt compound, and it is already confirmed that the cobalt compound is suitable. Since the proper blending amount was confirmed, the proper blending amount was set. For example, in a positive electrode plate in which a nickel oxide layer is not formed on the surface of a nickel sintered body, the amount of a single cobalt compound is 2.0 to 2.0% with respect to the amount of nickel hydroxide.
When it is 8.0 mol%, the discharge performance is good. In the case of the positive electrode plate B, the amount is 5 mol%. On the other hand, in the positive electrode plate having the nickel oxide layer on the surface of the nickel sintered body, the discharge performance is good when the amount of the single cobalt compound is 0.4 to 7.0 mol% with respect to the amount of nickel hydroxide.
In the positive electrode plate D and Experiment 2 described later, the amount was 4.2 mol%.
以上のようにして作製した4種類の正極板を所定に寸法
に切断した後、比重 1.250(20℃)のKOH電解液中で
試料正極板と同寸法のカドミウム負極板2枚を対極とし
て用い、放電特性を測定した。充電は 0.2CA×8時間
とし、基準電極としては酸化水銀電極を使用した。活物
質利用率の放電レート依存正を第1図に、放電中間電位
の放電レート依存性は第2図に示す。なお、第2図の放
電中間電位は理論容量に対する放電深度が50%の時の値
である。After cutting the four types of positive electrode plates produced as described above into predetermined dimensions, two cadmium negative electrode plates having the same dimensions as the sample positive electrode plate were used as counter electrodes in a KOH electrolyte having a specific gravity of 1.250 (20 ° C). The discharge characteristics were measured. Charging was performed for 0.2 CA × 8 hours, and a mercury oxide electrode was used as a reference electrode. The discharge rate dependency of the active material utilization rate is shown in FIG. 1, and the discharge intermediate potential dependency of the discharge rate is shown in FIG. The discharge intermediate potential in FIG. 2 is the value when the discharge depth is 50% of the theoretical capacity.
第1図からわかるように、従来品の正極板Aは他のどの
正極板より活物質利用率が低く、放電レート依存性も劣
っている。これに対し、硝酸コバルトを単独で含浸して
活物質中に水酸化ニッケルと固溶体を形成しない水酸化
コバルトを含む正極板Bを活物質利用率が約15〜20%ほ
ど向上している。またニッケル焼結体の表面にニッケル
酸化物の層を形成して、活物質含浸工程でニッケル焼結
体が腐食しないようにした正極板Cは活物質利用率だけ
でなく、その放電レート依存性も向上している。さらに
ニッケル焼結基板の表面にニッケル酸化物の層を形成
し、且つ硝酸コバルトを単独で含浸した本発明品の正極
板Dは活物質利用率及びその放電レート依存性が最も良
好で、30CA放電時の性能低下が非常に少ない。このよ
うな性能は従来品では得られなかったものであり、前述
した2つの改良技術による相乗的な効果が現われたもの
と考えらる。As can be seen from FIG. 1, the positive electrode plate A of the conventional product has a lower active material utilization rate than any other positive electrode plate and is inferior in discharge rate dependency. On the other hand, the positive electrode plate B containing cobalt hydroxide which does not form a solid solution with nickel hydroxide by being impregnated with cobalt nitrate alone has an improved active material utilization rate of about 15 to 20%. Further, the positive electrode plate C in which a nickel oxide layer is formed on the surface of the nickel sintered body to prevent the nickel sintered body from corroding in the active material impregnation step has not only the active material utilization rate but also its discharge rate dependency. Is also improving. Further, the positive electrode plate D of the present invention in which the nickel oxide layer was formed on the surface of the nickel sintered substrate and which was impregnated with cobalt nitrate alone had the best utilization of the active material and its discharge rate dependency, and the discharge rate was 30 CA. Very little deterioration in performance. Such performance was not obtained with the conventional product, and it is considered that the synergistic effect of the above-described two improved techniques appeared.
第2図の放電中間電位においても第1図と同様の傾向で
あるが、特に30CAといった超高率放電の用途ではニッ
ケル焼結体の表面にニッケル酸化物の層を形成すること
が重要であると言える。The intermediate discharge potential shown in FIG. 2 has the same tendency as that shown in FIG. 1, but it is important to form a nickel oxide layer on the surface of the nickel sintered body especially in the case of ultra high rate discharge such as 30 CA. Can be said.
以上2つの初期特性を測定した付から明らかなように、
ニッケル焼結体の表面にニッケル酸化物の層を形成し
て、活物質の含浸工程におけるニッケル焼結体の腐食を
防ぎ、さらに水酸化ニッケルと固溶体の形成しないコバ
ルト化合物を活物質中に含有させることによって、超高
率放電特性の非常に良好なニッケル正極板が得られるこ
とが明らかである。As is clear from the measurements of the above two initial characteristics,
A nickel oxide layer is formed on the surface of the nickel sintered body to prevent corrosion of the nickel sintered body in the step of impregnating the active material, and further nickel hydroxide and a cobalt compound which does not form a solid solution are contained in the active material. Thus, it is clear that a nickel positive electrode plate having an extremely high discharge characteristic can be obtained.
実験2 次にニッケル焼結体表面に形成するニッケル酸化物層の
厚みと放電特性について述べる。Experiment 2 Next, the thickness and discharge characteristics of the nickel oxide layer formed on the surface of the nickel sintered body will be described.
ここで用いたニッケル焼結基板は実験1で用いた基板B
と同様の方法で作製したものであるが、酸化条件を変え
ることによてニッケル焼結体の表面に生成するニッケル
酸化物層の平均厚みを10〜 140Åの間で変化されたもの
を用いた。The nickel sintered substrate used here is the substrate B used in Experiment 1.
Was prepared in the same manner as in, but the average thickness of the nickel oxide layer formed on the surface of the nickel sintered body was changed between 10 and 140Å by changing the oxidation conditions. .
活物質の含浸は実験1の正極板B及びDと同様の方法に
従った。つまり、含浸液は硝酸ニッケルを主成分とする
ニッケル、コバルト及びカドミウムの各硝酸塩の混合溶
液であり、この含浸液をニッケル焼結基板に含浸し、次
いで濃縮、中和を行うという通常の化学含浸の工程を数
回繰返した後、最後に硝酸コバルト単独の溶液を用いて
化学含浸の工程を1回行なって単独の水酸化コバルトを
生成させた。Impregnation with the active material was performed in the same manner as in the positive electrode plates B and D of Experiment 1. In other words, the impregnating solution is a mixed solution of nickel nitrate containing cobalt nitrate as a main component, cobalt nitrate, and cadmium nitrate. After repeating the above process several times, finally, the process of chemical impregnation was performed once using a solution of cobalt nitrate alone to produce cobalt hydroxide alone.
活物質の含浸工程終了後、各正極板毎にニッケル焼結体
表面のニッケル酸化物層の厚みを測定したところ、活物
質の含浸工程前に比べ約20Åづつ減少していた。つま
り、活物質の含浸工程中にニッケル酸化物層が約20Å溶
解したと考えられる。なお、元のニッケル酸化物層の厚
みが20Å未満であった正極板では、全てニッケル焼結体
の腐食が起きていたため、以下の試験では除外した。After the completion of the active material impregnation step, the thickness of the nickel oxide layer on the surface of the nickel sintered body was measured for each positive electrode plate, and it was found that the thickness decreased by about 20 Å compared to that before the active material impregnation step. In other words, it is considered that the nickel oxide layer was dissolved by about 20Å during the step of impregnating the active material. In the positive electrode plate in which the original nickel oxide layer had a thickness of less than 20 Å, the nickel sintered body was corroded in all cases, so it was excluded from the following test.
試料正極板は下記の条件で連続サイクルを行なった。The sample positive electrode plate was continuously cycled under the following conditions.
充電 1CA× 1.2時間 休止 1時間 放電 30CA+ 0.1Vまでvs. Hg /Hg O 休止 1時間 第3図に3サイクル目と 100サイクル目の放電時活物質
利用率を、第4図にその時の放電中間電位を示す。な
お、横軸のニッケル酸化物層平均厚みは活物質の含浸工
程終了後の値である。Charging 1CA × 1.2 hours Pause 1 hour Discharge up to 30CA + 0.1V vs. Hg / Hg O Pause 1 hour Figure 3 shows the active material utilization rate during discharge at the 3rd and 100th cycles, and in Fig. 4 the discharge intermediate time. Indicates electric potential. The average thickness of the nickel oxide layer on the horizontal axis is a value after the completion of the step of impregnating the active material.
第3図の結果からわかるように、ニッケル焼結体表面の
ニッケル酸化物層の厚みが80Å超えると活物質利用率が
低下している。この理由の1つしては、ニッケル酸化物
の絶縁体的な性質が影響を及ぼしたもの考えらる。一
方、 100サイクル目ではニッケル酸化物層の厚みが5Å
未満の場合にも活物質利用率が低下している。この理由
の1つとしては、ニッケル酸化物層の厚みが非常に薄い
場合は充放電サイクルの進行に伴なうニッケル焼結体の
活物質化が起こることが考えられる。つまり、含浸工程
で充填した活物質の組成とは異なる水酸化ニッケル単独
の活物質がニッケル焼結体と充填した活物質の間に生成
し、電流分布の不均一などの極板性能の低下させる原因
の1つになっていると考えられる。As can be seen from the results in FIG. 3, when the thickness of the nickel oxide layer on the surface of the nickel sintered body exceeds 80 Å, the active material utilization rate decreases. It is considered that one of the reasons for this is that the insulating property of nickel oxide has an influence. On the other hand, at the 100th cycle, the nickel oxide layer had a thickness of 5Å
The utilization rate of the active material is also reduced when the ratio is less than the above. As one of the reasons for this, it is conceivable that when the nickel oxide layer is very thin, the nickel sintered body becomes an active material as the charge / discharge cycle progresses. That is, an active material of nickel hydroxide alone having a composition different from the composition of the active material filled in the impregnation step is generated between the nickel sintered body and the filled active material, which deteriorates the electrode plate performance such as uneven current distribution. It is considered to be one of the causes.
第4図の放電中間電位においても第3図と同様の傾向で
あるが、ニッケル酸化物層の厚みが70Åを超えると性能
が低下しており、第3図の活物質利用率よりもニッケル
酸化物層厚さの影響が大きいようである。The discharge intermediate potential in Fig. 4 shows the same tendency as in Fig. 3, but the performance deteriorates when the thickness of the nickel oxide layer exceeds 70Å, and the nickel oxidation rate is higher than the active material utilization rate in Fig. 3. It seems that the thickness of the material layer has a great influence.
以上のことから、ニッケル焼結体表面のニッケル酸化物
層の平均厚みが5〜70Åの場合に、超高率放電特性の非
常に良好なニッケル正極板が得られることが明らかであ
る。From the above, it is clear that when the average thickness of the nickel oxide layer on the surface of the nickel sintered body is 5 to 70Å, a nickel positive electrode plate having very good ultra-high rate discharge characteristics can be obtained.
なお、前記した実験1及び2ではニッケルを焼結基板を
用い化学含浸法によって活物質を充填する方法で本発明
を説明したが、活物質の充填方法が電解含浸方法である
場合や非焼結式のニッケル多孔体よりなる基板を用いた
場合でも同様の結果が得られることを実験により確認し
ている。また単独のコバルト化合物については、水酸化
コバルトで説明したが、各種のコバルト塩やコバルト酸
化物でも同様の結果が得られることを実験により確認し
ている。In the experiments 1 and 2 described above, the present invention has been described by the method of filling the active material by the chemical impregnation method using the sintered substrate of nickel, but when the filling method of the active material is the electrolytic impregnation method or the non-sintering method. It has been confirmed by experiments that similar results are obtained even when a substrate made of the nickel porous body of the formula is used. Further, although the cobalt compound alone has been explained with cobalt hydroxide, it has been confirmed by experiments that similar results can be obtained with various cobalt salts and cobalt oxides.
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、活物
質を保持しているニッケル多孔体の表面に平均厚み5〜
70Åのニッケル酸化物の層を有し、さらに水酸化ニッ
ケルと固溶体を形成しないコバルト化合物を活物質中に
含有していることによって、超効率放電において活物質
利用率及び放電々位が非常に良好なニッケル正極板を得
ることができる。EFFECTS OF THE INVENTION Based on the present invention as shown in the above examples, the average thickness of 5 to 5 is provided on the surface of the nickel porous body holding the active material.
By having a 70Å layer of nickel oxide and further containing a cobalt compound that does not form a solid solution with nickel hydroxide in the active material, the active material utilization rate and discharge position are very good in super-efficient discharge. It is possible to obtain an excellent nickel positive electrode plate.
第1図は本発明によるアルカリ蓄電池用ニッケル正極板
及び従来のこの種ニッケル正極板の活物質利用率の放電
レート依存性の一例を示す特性図、第2図は同じく本発
明によるアルカリ蓄電池用ニッケル正極板及び従来のこ
の種ニッケル正極板の放電中間電位の放電レート依存性
の一例を示す特性図、第3図はニッケル焼結体表面のニ
ッケル酸化物層の厚みと放電時活物質利用率との関係を
示す特性図、第4図は同じくニッケル焼結体表面のニッ
ケル酸化物層の厚みと放電中間電位との関係を示す特性
図である。FIG. 1 is a characteristic diagram showing an example of the discharge rate dependence of the active material utilization rate of the nickel positive electrode plate for alkaline storage batteries according to the present invention and the conventional nickel positive electrode plate of this kind, and FIG. 2 is the nickel for alkaline storage batteries according to the present invention. A characteristic diagram showing an example of the discharge rate dependence of the discharge intermediate potential of a positive electrode plate and a conventional nickel positive electrode plate of this kind, and FIG. 3 shows the thickness of the nickel oxide layer on the surface of the nickel sintered body and the utilization rate of the active material during discharge. FIG. 4 is a characteristic diagram showing the relationship between the thickness of the nickel oxide layer on the surface of the nickel sintered body and the discharge intermediate potential.
Claims (1)
平均厚みが5Å以上70Å以下のNiOからなるニッケ
ル酸化物の層を有し、さらに水酸化ニッケルと固溶体を
形成しないコバルト化合物を活物質中に含有すること特
徴とするアルカリ蓄電池用ニッケル正極板。1. A cobalt compound having a nickel oxide layer having an average thickness of 5 Å or more and 70 Å or less on the surface of a nickel porous body holding an active material, the cobalt compound not forming a solid solution with nickel hydroxide. A nickel positive electrode plate for an alkaline storage battery, which is characterized by being contained therein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61055813A JPH0656762B2 (en) | 1986-03-12 | 1986-03-12 | Nickel positive electrode plate for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61055813A JPH0656762B2 (en) | 1986-03-12 | 1986-03-12 | Nickel positive electrode plate for alkaline storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62211860A JPS62211860A (en) | 1987-09-17 |
| JPH0656762B2 true JPH0656762B2 (en) | 1994-07-27 |
Family
ID=13009371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61055813A Expired - Lifetime JPH0656762B2 (en) | 1986-03-12 | 1986-03-12 | Nickel positive electrode plate for alkaline storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0656762B2 (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5564372A (en) * | 1978-11-07 | 1980-05-15 | Japan Storage Battery Co Ltd | Manufacturing method of sintered negative plate for alkaline storage battery |
| EP0028072B1 (en) * | 1979-10-03 | 1984-08-01 | LUCAS INDUSTRIES public limited company | A nickel electrode, a method of producing the nickel electrode and an electrochemical cell employing the nickel electrode |
| JPS59154779A (en) * | 1983-02-21 | 1984-09-03 | Matsushita Electric Ind Co Ltd | Charging method of enclosed type nickel-cadmium storage battery |
| JPS6251157A (en) * | 1985-08-29 | 1987-03-05 | Shin Kobe Electric Mach Co Ltd | Manufacture of cathode plate for nickel-cadmium alkaline storage battery |
-
1986
- 1986-03-12 JP JP61055813A patent/JPH0656762B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62211860A (en) | 1987-09-17 |
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