JPH02155165A - Cadmium negative plate and alkaline secondary battery using this negative plate - Google Patents

Cadmium negative plate and alkaline secondary battery using this negative plate

Info

Publication number
JPH02155165A
JPH02155165A JP63309611A JP30961188A JPH02155165A JP H02155165 A JPH02155165 A JP H02155165A JP 63309611 A JP63309611 A JP 63309611A JP 30961188 A JP30961188 A JP 30961188A JP H02155165 A JPH02155165 A JP H02155165A
Authority
JP
Japan
Prior art keywords
cadmium
negative electrode
electrode plate
nickel
battery
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.)
Pending
Application number
JP63309611A
Other languages
Japanese (ja)
Inventor
Masayuki Yoshimura
公志 吉村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Japan Storage Battery Co Ltd
Original Assignee
Japan Storage Battery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Japan Storage Battery Co Ltd filed Critical Japan Storage Battery Co Ltd
Priority to JP63309611A priority Critical patent/JPH02155165A/en
Publication of JPH02155165A publication Critical patent/JPH02155165A/en
Pending legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/246Cadmium electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To enhance charging efficiency by containing a specified ratio of dinickel trioxide based on the amount of total cadmium. CONSTITUTION:0.25-20wt.% dinickel trioxide (Ni2O3) based on the weight of total cadmium is contained in a negative plate of an alkaline secondary battery. By containing dinickel trioxide in the negative active material, charging efficiency is enhanced. For example, when a cadmium negative plate mainly comprising cadmium hydroxide or cadmium oxide and metallic cadmium is charged at 1cA on the basis of the theoretical capacity of cadmium oxide or cadmium hydroxide, charging efficiency until hydrogen evolution starts is about 93%. If 2wt.% dinickel trioxide based on the weight of total cadmium is contained, charging efficiency exceeds 93%.

Description

【発明の詳細な説明】 産業上の利用分野 本発明はカドミウム負極板と、その負極板を用いたアル
カリ二次電池に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a cadmium negative electrode plate and an alkaline secondary battery using the negative electrode plate.

従来の技術とその課題 現在、二次電池としては、主として鉛電池およびニッケ
ルーカドミウム電池が用いられているが、特にニッケル
ーカドミウム電池は、高率放電での特性が良好であるこ
とや、鉛電池に比べて寿命が長いなどの理由によって需
要が急増している。また一方では、近年の電子機器の小
型化、軽量化などに伴って、高容量化や充電時間の短縮
が二次電池に対して要求されている。
Conventional technology and its issues At present, lead batteries and nickel-cadmium batteries are mainly used as secondary batteries, but nickel-cadmium batteries in particular have good characteristics at high rate discharge, and lead Demand is rapidly increasing for reasons such as their long lifespan compared to batteries. On the other hand, as electronic devices have become smaller and lighter in recent years, secondary batteries are required to have higher capacity and shorter charging time.

カドミウム負極板を用いた従来のアルカリ二次電池には
次のような問題がある。それはカドミウム負極板に関す
るもので、充放Th反応に関与しない水酸化カドミウム
を多く有していることである。
Conventional alkaline secondary batteries using cadmium negative electrode plates have the following problems. This is related to the cadmium negative electrode plate, which contains a large amount of cadmium hydroxide that does not participate in the charging and discharging Th reaction.

つまり、水酸化カドミウムの水素ガス発生までの充電効
率は、通常90%程度であり、残り約10%の水酸化カ
ドミウムは何等役に立つこともなく不要な体積を占めて
いる。さらにニッケル−カドミウム電池を例にとると、
電池の密閉状態を保つために、負極板内に正極板の容量
の20%以上のいわゆるリザーブの水酸化カドミウムが
必要であった。
In other words, the charging efficiency of cadmium hydroxide until hydrogen gas is generated is usually about 90%, and the remaining 10% of cadmium hydroxide is of no use and occupies unnecessary volume. Furthermore, taking a nickel-cadmium battery as an example,
In order to keep the battery sealed, a so-called reserve of cadmium hydroxide of 20% or more of the capacity of the positive electrode plate was required in the negative electrode plate.

このリザーブの水酸化カドミウムは正極活物質の保持体
である金属ニッケルの活物質化や電池内の空間体積を補
償するものであり、放電容量には寄与しない、これらの
水酸化カドミウムを有していることが、カドミウム負極
板および電池の高容量化を妨げている一因である。
This reserve cadmium hydroxide is used to make the metal nickel, which is the support for the positive electrode active material, into an active material and to compensate for the space volume inside the battery, and does not contribute to the discharge capacity. This is one of the reasons that prevents higher capacity of cadmium negative electrode plates and batteries.

また、従来のニッケルーカドミウム電池は、電池の密閉
状態を保つために定電流で充電した場合には電流を約1
CA以下に抑えなければならないという問題を有してい
る。これは、充電電流を1CA以上に大きくした場合に
は、過充を領域において正極板から発生した全ての酸素
ガスを負極板で吸収することができずに、結局は安全弁
が作動して電解液の減少を起こし、容量低下とか金持性
の劣化を起こすためである。そこで、特願昭62−83
582号や特願昭63−13345号で提案されている
ように、充電時における負極板の水素発生にいたる過程
の電位変化を充電電圧の変化として検出して充電制御を
容易にし、かつ急速充電を可能にする試みがあるが、負
極板の充電効率の点で不十分である。
In addition, when conventional nickel-cadmium batteries are charged at a constant current to keep the battery sealed, the current is approximately 1
There is a problem in that it must be kept below CA. This is because when the charging current is increased to 1 CA or more, the negative electrode plate cannot absorb all the oxygen gas generated from the positive electrode plate in the overcharging region, and the safety valve is activated and the electrolyte is dissolved. This is because it causes a decrease in capacity and a deterioration in wealth. Therefore, the special application
As proposed in No. 582 and Japanese Patent Application No. 63-13345, potential changes in the process leading to hydrogen generation in the negative electrode plate during charging are detected as changes in the charging voltage to facilitate charging control and provide rapid charging. Although there are attempts to make this possible, they are insufficient in terms of charging efficiency of the negative electrode plate.

課題を解決するための手段 本発明はカドミウム負極板と、その負極板を備えたアル
カリ二次電池に関するものであって、該負極板は三二酸
化ニッケル(Ni、O,)を全カドミウム量に対し0.
25重量%以上20重量%以下含有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 cadmium negative electrode plate and an alkaline secondary battery equipped with the negative electrode plate, the negative electrode plate containing nickel sesquioxide (Ni, O,) relative to the total amount of cadmium. 0.
It is characterized by containing 25% by weight or more and 20% by weight or less.

作用 カドミウム負極板の充電効率について検討した結果、負
極活物質中に三二酸化ニッケルを含有させることによっ
て充電効率が高くなることがわかった。
As a result of investigating the charging efficiency of a cadmium negative electrode plate, it was found that the charging efficiency was increased by incorporating nickel sesquioxide into the negative electrode active material.

例えば、水酸化カドミウムあるいは酸化カドミウムと金
属カドミウムとを活物質の主体とするカドミウム負極板
を、酸化カドミウムあるいは水酸化カドミウムの理論容
量を基準として 1CAの電流で充電した際の水素ガス
が発生するまでの充電効率は約93″gであるが、三二
酸化ニッケルを全カドミウム量に対し例えば2重量%含
有した場合には充電効率が99%以上に向上する。
For example, when a cadmium negative electrode plate whose main active materials are cadmium hydroxide or cadmium oxide and metal cadmium is charged with a current of 1 CA, based on the theoretical capacity of cadmium oxide or cadmium hydroxide, until hydrogen gas is generated. The charging efficiency is about 93''g, but when nickel sesquioxide is contained, for example, 2% by weight based on the total amount of cadmium, the charging efficiency improves to 99% or more.

また、このような充電効率の優れた負極板を用いて、そ
の負極板の充電時の水素発生にいたる電位変化を端子電
圧の変化として検出すれば充電制御が容易であり、その
時点で定電圧に設定すれば過充電領域では電流が小さく
なるために、急速充電が可能でしかも電解液の減量のな
いアルカリ二次電池となる。
In addition, by using such a negative electrode plate with excellent charging efficiency, it is easy to control charging by detecting the potential change that leads to hydrogen generation during charging of the negative electrode plate as a change in terminal voltage, and at that point, the constant voltage If set to , the current becomes small in the overcharge region, resulting in an alkaline secondary battery that allows rapid charging and does not cause loss of electrolyte.

実施例 以下本発明を好適な実施例を用いて詳細に説明する。Example The present invention will be explained in detail below using preferred embodiments.

本発明の目的は、充電効率の優れたカドミウム負極板を
得ることであり、またそれを電池に適用することである
。従って、まず最初にカドミウム負極板について述べる
9 [実施例1] 酸化カドミウム粉末240+1(lと金属カドミウム粉
末210ngと配合量を0〜b 酸化ニッケルとを混合してから、230kv/cn”の
圧力で加圧成形して、全カドミウムの理論容量が200
iAhの錠剤とした。さらにこの錠剤を20メツシユの
ニッケル網で包んで負極板とした。これを負極板群(イ
)とする。
An object of the present invention is to obtain a cadmium negative electrode plate with excellent charging efficiency, and to apply it to batteries. Therefore, first, we will discuss the cadmium negative electrode plate9 [Example 1] After mixing cadmium oxide powder 240+1 (l), 210 ng of metal cadmium powder, and nickel oxide in a blending amount of 0 to b, the mixture was heated at a pressure of 230 kv/cn''. Pressure molded, total theoretical capacity of cadmium is 200
It was made into iAh tablets. Furthermore, this tablet was wrapped in a nickel mesh of 20 meshes to form a negative electrode plate. This is called the negative electrode plate group (a).

[実施例2コ 水酸化カドミウム粉末273ngと金属カドミウム粉末
210uと配合量を0〜8419の範囲で変えた三二酸
化ニッケルとを混合した後、実施例1と同様にして、理
論容量が200nAhの錠剤形負極板とした。
[Example 2] After mixing 273 ng of cadmium hydroxide powder, 210 u of metal cadmium powder, and nickel sesquioxide with varying amounts in the range of 0 to 8419, tablets with a theoretical capacity of 200 nAh were prepared in the same manner as in Example 1. It was made into a negative electrode plate.

これを負極板群(ロ)とする。This is called the negative electrode plate group (b).

なお、全カドミウム量とはカドミウム負極板に含まれる
Cd原子の総量である。
Note that the total amount of cadmium is the total amount of Cd atoms contained in the cadmium negative electrode plate.

これらの負極板を比重1.250(20°C)の水酸化
カリウム水溶液中で、対極にニッケル平板2枚を用いて
、配合時における酸化カドミウム粉末あるいは水酸化カ
ドミウム粉末の理論容量を基準としてICAt1OOn
A)の電流で充放電を繰り返し、下記の式(1)から充
電効率を求めた。
These negative electrode plates were placed in a potassium hydroxide aqueous solution with a specific gravity of 1.250 (20°C), using two nickel flat plates as counter electrodes, and ICAt1OOn based on the theoretical capacity of the cadmium oxide powder or cadmium hydroxide powder at the time of compounding.
Charging and discharging were repeated using the current A), and the charging efficiency was determined from the following equation (1).

その結果を第1図に示す、同図から活物質原料として酸
化カドミウムあるいは水酸化カドミウムを用いたことに
よる差は認められず、全カドミウム量に対する三二酸化
ニッケルの含有率が0.25重量%以上の範囲で充電効
率の向上が認められる。
The results are shown in Figure 1. From the figure, no difference was observed due to the use of cadmium oxide or cadmium hydroxide as the raw material for the active material, and the content of nickel sesquioxide relative to the total amount of cadmium was 0.25% by weight or more. An improvement in charging efficiency is observed within the range of .

特に含有率が1重量%以上20重量%以下の範囲では充
電効率が98X以上と極めて高く、充電できない不活性
な水酸化カドミウムが減少していることを示している。
In particular, when the content is in the range from 1% by weight to 20% by weight, the charging efficiency is extremely high at 98X or more, indicating that inactive cadmium hydroxide, which cannot be charged, is reduced.

なお、三二酸化ニッケルの含有量を20重量%よりも高
くすることは可能であるが、カドミウム活物質の理論容
量密度の低下が大きくなるため、その含有率は20重量
%以下であることが望ましい考えられる。
Note that although it is possible to make the content of nickel sesquioxide higher than 20% by weight, it is desirable that the content is 20% by weight or less because the decrease in the theoretical capacity density of the cadmium active material will be large. Conceivable.

以上のことから全カドミウムに対する三二酸化ニッケル
の含有率は、0.25重量%以上20重量%以下とする
のが適しているといえる。
From the above, it can be said that the content of nickel sesquioxide relative to the total cadmium is preferably 0.25% by weight or more and 20% by weight or less.

以下に実施例で用いた各原料の性状を示す。The properties of each raw material used in the examples are shown below.

〈酸化カドミウム粉末〉 アトマイズ法によって製作した平均粒子径1μlのもの く水酸化カドミウム粉末〉 上記の酸化カドミウム粉末を精製水中に浸漬して水和さ
せたもの く金属カドミウム粉末〉 電気化学的な置換法によって製作した平均粒子径2μm
のもの く三二酸化ニッケル〉 市販の試薬 次に以上の実施例で説明した極めて高い充電効率を有す
る本発明のカドミウム負極板を用いた電池の評価を行っ
た。
<Cadmium oxide powder> Cadmium hydroxide powder with an average particle size of 1 μl produced by the atomization method> Metallic cadmium powder obtained by immersing the above cadmium oxide powder in purified water and hydrating it> Electrochemical substitution method Average particle size 2μm manufactured by
Monokuku Nickel Sesquioxide> Commercially available reagent Next, a battery using the cadmium negative electrode plate of the present invention having extremely high charging efficiency as described in the above examples was evaluated.

本発明のカドミウム負極板はリザーブの水酸化カドミウ
ムを必要とする従来のニッケルーカドミウム電池に使用
できる他に、これよりも高容量化と充電時間の短縮が可
能であるリザーブの水酸化カドミウムを有しない電池に
使用した場合にその効果がより明確である。それは、本
発明のカドミウム負極板の充電効率が優れていることに
起因する。従って以下の実施例ではリザーブの水酸化カ
ドミウムを有しない電池を例にして説明する。
The cadmium negative electrode plate of the present invention can be used in conventional nickel-cadmium batteries that require cadmium hydroxide as a reserve, and also has cadmium hydroxide as a reserve, which enables higher capacity and shorter charging time. The effect is more obvious when used with batteries that do not. This is due to the excellent charging efficiency of the cadmium negative electrode plate of the present invention. Therefore, in the following examples, a battery without cadmium hydroxide as a reserve will be described as an example.

本発明のアルカリ電池に使用できる正極活物質は水酸化
ニッケル、二酸化マンガンおよび酸化銀である。これら
のうち一般的に多く用いられている活物質は水酸化ニッ
ケルであるので、ニッケルカドミウム電池を中心にして
説明する。
Positive electrode active materials that can be used in the alkaline battery of the present invention are nickel hydroxide, manganese dioxide and silver oxide. Among these, the most commonly used active material is nickel hydroxide, so the explanation will focus on nickel-cadmium batteries.

本発明に用いるカドミウム負極板は、基本的に以下に示
す集電体を用いて製造することができる。
The cadmium negative electrode plate used in the present invention can basically be manufactured using the current collector shown below.

すなわち、ニッケルや銅やカドミウムの網、エクスパン
デッドメタル、穿孔板あるいは集電体と活物質保持体を
兼ねる三次元構造の金属発泡体や金属繊維のマットであ
る。
That is, it is a nickel, copper, or cadmium net, an expanded metal, a perforated plate, or a three-dimensionally structured metal foam or metal fiber mat that serves both as a current collector and an active material holder.

また、鉄にニッケルメッキしたものや、鉄あるいはニッ
ケルに銅メツキしたもの、さらに鉄、ニッケルあるいは
銅にカドミウムメツキしたものも使用できる。
Further, iron plated with nickel, iron or nickel plated with copper, and iron, nickel or copper plated with cadmium can also be used.

[実施例3] 酸化カドミウム粉末60重量部と金属カドミウム粉末4
0重量部と三二酸化ニッケル2重量部と長さ 11mの
ポリプロピレン製の短繊維0.1重量部とを1.5重量
%のポリビニルアルコールを含むエチレングリコール3
01で混合してペースト状にする。このペーストをニッ
ケルメツ?r(5μm)した穿孔鋼板に塗着し、次いで
乾燥、加圧して酸化カドミウムの理論容量が960nA
hで寸法が2,9x14x52(nn)の負極板を製作
した。
[Example 3] 60 parts by weight of cadmium oxide powder and 4 parts by weight of metal cadmium powder
0 parts by weight of nickel sesquioxide, 2 parts by weight of nickel sesquioxide, and 0.1 parts by weight of short polypropylene fibers having a length of 11 m, and ethylene glycol 3 containing 1.5% by weight of polyvinyl alcohol.
Mix with 01 to make a paste. Nickelmets this paste? The theoretical capacity of cadmium oxide is 960 nA by coating it on a perforated steel plate with a diameter of 5 μm and then drying and pressurizing it.
A negative electrode plate with dimensions of 2.9 x 14 x 52 (nn) was manufactured in h.

一方、正極板は次の方法で製作した。On the other hand, the positive electrode plate was manufactured by the following method.

多孔度が約80%の焼結式ニッケル基板に、ニッケルと
コバルトとの合計に対するコバルトの含有率が8モル%
の硝酸コバルトと硝酸ニッケルとの混合水溶液[PH=
2、比重1.50(20℃)]を含浸した後、比重1.
2QO(20℃)の水酸化ナトリウム水溶液に浸漬し、
湯洗、乾燥する。この操作を繰り返して、水酸化ニッケ
ルと水酸化コバルトの理論容量の合計が400nAhで
寸法が1.4 x14x52mmの正極板を製作した。
A sintered nickel substrate with a porosity of approximately 80%, and a cobalt content of 8 mol% based on the total of nickel and cobalt.
A mixed aqueous solution of cobalt nitrate and nickel nitrate [PH=
2, specific gravity 1.50 (20°C)].
Immerse in aqueous sodium hydroxide solution at 2QO (20°C),
Wash with hot water and dry. This operation was repeated to produce a positive electrode plate having a total theoretical capacity of nickel hydroxide and cobalt hydroxide of 400 nAh and dimensions of 1.4 x 14 x 52 mm.

次に負極板1枚を厚さ0.2nnのポリアミドの不織布
に包んだ後に正極板2枚の間にはさみ、電解液として比
重1.250  (20℃)の水酸化カリウム水溶i2
.4nlを用いて、公称容量が700nAhの合成樹脂
製の電槽を用いたニッケルーカドミウム電池(A)を製
作した。外形寸法は67x 16.5x 8[in)で
あり、0.1kg/cn’で作動する安全弁を付けてい
る。
Next, one negative electrode plate was wrapped in a polyamide nonwoven fabric with a thickness of 0.2 nn, and then sandwiched between two positive electrode plates, and the electrolyte was prepared using potassium hydroxide aqueous solution I2 with a specific gravity of 1.250 (20°C).
.. A nickel-cadmium battery (A) using a synthetic resin battery case with a nominal capacity of 700 nAh was manufactured using 4nl. The external dimensions are 67 x 16.5 x 8 [in], and it is equipped with a safety valve that operates at 0.1 kg/cn'.

また、この電池の負極板中の酸化カドミウムは電解液を
入れると以下の式(2)に示す反応によって水を消費す
るため、その消費分に相当する水を余分に注入した。
In addition, since the cadmium oxide in the negative electrode plate of this battery consumes water by the reaction shown in the following equation (2) when an electrolytic solution is added, an extra amount of water corresponding to the consumed amount was injected.

CdO+H,0−Cd (OH)、  ・・・(2)[
実施例4] 水酸化カドミウム粉末68.5重量部と金属カドミウム
粉末40jl量部と三二酸化ニッケル2重量部と長さ1
1IIlのポリプロピレン製の短繊維0.1重量部とを
1.5重量%のポリビニルアルコールを含むエチレング
リコール301で混合してペースト状にする。このペー
ストを銅メツキ(5μr#)シた穿孔鋼板に塗着し、次
いで乾燥、加圧して水酸化カドミラムノ理論容量が96
0mAh テ寸法カ2.9 x14x52(nl)の負
極板を製作した。
CdO+H, 0-Cd (OH), ... (2) [
Example 4] 68.5 parts by weight of cadmium hydroxide powder, 40 parts by weight of metal cadmium powder, 2 parts by weight of nickel sesquioxide, and 1 part by weight of nickel sesquioxide
0.1 part by weight of short polypropylene fibers of 1IIIl are mixed with ethylene glycol 301 containing 1.5% by weight of polyvinyl alcohol to form a paste. This paste was applied to a copper-plated (5μr#) perforated steel plate, then dried and pressurized to reach a theoretical capacity of 96%.
A negative electrode plate of 0 mAh, size 2.9 x 14 x 52 (nl) was manufactured.

次に上記の負極板と実施例3と同じ正極板とを用いて実
施例3と同様な構成の公称容量が700IIAhの角形
ニッケルーカドミウム電池(B)を製作した。
Next, using the above negative electrode plate and the same positive electrode plate as in Example 3, a prismatic nickel-cadmium battery (B) having the same configuration as in Example 3 and having a nominal capacity of 700 IIAh was manufactured.

[実施例5] 実施例3における負極板の集電体すなわちニッケルメッ
キした穿孔鋼板の代わりにカドミウムメツ−’r(5μ
s)した穿孔鋼板を用いた以外は全て実施例3と同様に
して公称容量700IIAhの角形ニッケルーカドミウ
ム電池(C)を製作した。
[Example 5] Instead of the current collector of the negative electrode plate in Example 3, that is, the nickel-plated perforated steel plate, cadmium
A prismatic nickel-cadmium battery (C) with a nominal capacity of 700 IIAh was manufactured in the same manner as in Example 3 except that the perforated steel plate prepared in s) was used.

[比教例1] 実施例3における負極板の配合から三二酸化ニッケルを
削除した以外は全て実施例3と同様にして公称容量70
0iAhの角形ニッケルーカドミウム電池(0)を製作
しな。
[Comparison Example 1] The same procedure as in Example 3 was made except that nickel sesquioxide was removed from the formulation of the negative electrode plate in Example 3, with a nominal capacity of 70.
Make a 0iAh square nickel-cadmium battery (0).

以上のようにして製作した電池(、A)、 (8)、 
(C)および(D)を20℃において最大電流3CAの
電流で1゜90Vの定電圧充電を30分間行った後、0
.2CAの電流で0.5vまで放電するという充放電サ
イクルを250回行つな。1サイクル目の放電容量を1
00とした場合の各サイクルにおける容量保持率を第2
図に示す。同図から本発明の電池(A)、 f8)、お
よび(C)は比較電池(D)よりも容量保持率が明らか
に高いことがわかる。この原因は本発明の電池の負極活
物質の充電効率が極めて高く、3CAのような大きな@
流であっても充電終期の負極電位の立ち上がりまでの充
電電気量が多いためであり、また充電効率のサイクルに
おける低下がほとんどないためである。
Batteries manufactured as above (, A), (8),
After charging (C) and (D) at a constant voltage of 1°90V for 30 minutes at a maximum current of 3CA at 20°C,
.. Do 250 charge/discharge cycles of discharging to 0.5V with a current of 2CA. The discharge capacity of the first cycle is 1
The capacity retention rate in each cycle when set to 00 is the second
As shown in the figure. From the figure, it can be seen that the batteries (A), f8), and (C) of the present invention have clearly higher capacity retention rates than the comparative battery (D). The reason for this is that the charging efficiency of the negative electrode active material of the battery of the present invention is extremely high.
This is because the amount of electricity charged until the negative electrode potential rises at the end of charging is large even when current is applied, and there is almost no decrease in charging efficiency during the cycle.

なお、電池(A)、 (B)、 (C)およびTO)の
負極板中の水酸化カドミウムの含有量は重量比で正極中
の水酸化ニッケルの約0.95倍[2,73(9/^h
) /2.88((]/Ah)]となっている、また負
極板の製作に用いた酸化カドミウム粉末等の原料の性状
は先の錠剤形負極板の実施例で用いたものと同様である
The content of cadmium hydroxide in the negative electrode plates of batteries (A), (B), (C) and TO) is about 0.95 times [2,73 (9 /^h
) /2.88((]/Ah)], and the properties of the raw materials such as cadmium oxide powder used to manufacture the negative electrode plate are the same as those used in the previous example of the tablet-shaped negative electrode plate. be.

以上のように、本発明の電池は、定電圧制御という簡便
な充電方法で超急速充電が可能であり、容量保持率が優
れている。
As described above, the battery of the present invention can be charged extremely rapidly using a simple charging method of constant voltage control, and has an excellent capacity retention rate.

なお、充電方法は、最大電流を規制して定電圧充電する
方法を適用したがこの方法は、従来のニッケルーカドミ
ウム電池で用いられている定を流で充電した後、充電電
圧がガス吸収によって低下するのを検出して充電を打切
る方法やガス吸収による発熱を検出して充電を打切る方
法のような複雑な充電システムではない、また本発明の
特徴のひとつは従来ニッケルーカドミウム電池ではその
適用が困難であった定電圧充電方式が容易に行えること
である。すなわち従来のニッケルーカドミウム電池では
充電過程の電圧と充電終期の電圧との差が高々150〜
20QnVと少なかったため、定電圧充電方式が適用で
きなかったが、本発明による電池の場合にはその差が0
.2CA以上の電流で400Ilv以上にも達するため
に充電電圧の変化を検出することが容易である。この場
合、定電流で充電して、充電電圧の上昇を検出してから
電流を下げてもよいし、定電圧で充電してもよい、なお
、従来の焼結式極板を用いた公称容量が700mAhの
円筒形ニッケルーカドミウム電池(AAサイズ)を最大
電流3CAの電流で1.9vの定電圧充電を30分間行
ったところ、安全弁が作動して液漏れが発生した。この
ことは従来の電池の充電電圧が1.9■に達しないため
に電池が過充電されたことによるものである。
The charging method used a constant voltage charging method that regulated the maximum current, but this method is similar to that used in conventional nickel-cadmium batteries, where after charging with a constant current, the charging voltage changes due to gas absorption. One of the features of the present invention is that it does not require a complicated charging system, such as a method that stops charging by detecting a drop in battery voltage or a method that stops charging by detecting heat generation due to gas absorption. The constant voltage charging method, which has been difficult to apply, can be easily performed. In other words, in conventional nickel-cadmium batteries, the difference between the voltage during the charging process and the voltage at the end of charging is at most 150 ~
However, in the case of the battery according to the present invention, the difference was reduced to 0.
.. Since the current reaches 400 Ilv or more with a current of 2 CA or more, it is easy to detect changes in charging voltage. In this case, you can charge with a constant current and then lower the current after detecting an increase in the charging voltage, or you can charge with a constant voltage. When a cylindrical nickel-cadmium battery (AA size) with a capacity of 700 mAh was charged at a constant voltage of 1.9 V for 30 minutes at a maximum current of 3 CA, the safety valve was activated and leakage occurred. This is because the battery was overcharged because the charging voltage of the conventional battery did not reach 1.9μ.

このように本発明の電池では、充電終期の負極板の電位
変化を大きくすることが有利であり、集電体の表面は、
基本的に水素発生の過電圧が大きい銅あるいはカドミウ
ムであるもの、例えば銅やカドミウムの網、エクスパン
デッドメタル、穿孔板あるいは集電体と活物質保持体を
兼ねる三次元構造の金属発泡体や金属繊維のマット等、
さらに材質としては鉄あるいはニッケルに銅あるいはカ
ドミウムメツキしたものが適している。しかし、水素発
生の過電圧が小さいニッケルの集電体であっても、活物
質にニッケル粉末等の水素過電圧の小さい物質を少なく
することによって、例えば5重量%以下にすれば集電体
として用いることができる。
As described above, in the battery of the present invention, it is advantageous to increase the potential change of the negative electrode plate at the end of charging, and the surface of the current collector is
Basically copper or cadmium with a large overvoltage for hydrogen generation, such as copper or cadmium nets, expanded metals, perforated plates, or three-dimensional metal foams and metals that serve as current collectors and active material holders. fiber mat etc.
Further, suitable materials include iron or nickel plated with copper or cadmium. However, even if a nickel current collector has a small hydrogen overvoltage, it can still be used as a current collector by reducing the amount of a substance with a small hydrogen overvoltage, such as nickel powder, in the active material, for example to 5% by weight or less. Can be done.

以上の本発明実施例では、正極活物質として水酸化ニッ
ケルを用いて説明したが、活物質として二酸化マンガン
を用いてもニッケルーカドミウム電池と同様な効果が現
れる。以下に、本発明を二酸化マンガン−カドミウム電
池に適用した場合について好適な実施例を用いて説明す
る。
Although the above embodiments of the present invention have been described using nickel hydroxide as the positive electrode active material, the same effects as those of the nickel-cadmium battery can be obtained even when manganese dioxide is used as the active material. Below, the case where the present invention is applied to a manganese dioxide-cadmium battery will be explained using preferred embodiments.

[実施例6] 金属カドミウム粉末100重量部と、三二酸化ニッケル
2重量部と長さ innのポリプロピレン製の短繊維0
.1重量部とを1.5重量%のポリビニルアルコールを
含むエチレングリコール3011で混合してペースト状
にする。このペーストを銅のエクスパンデッドメタルに
塗着し、次いで乾燥、加圧して金属カドミウムの容量が
800iAhで寸法が2゜9 x 14x 52(nr
m)の負極板を製作した。
[Example 6] 100 parts by weight of metal cadmium powder, 2 parts by weight of nickel sesquioxide, and 0 short fibers made of polypropylene with a length of inn.
.. 1 part by weight and ethylene glycol 3011 containing 1.5% by weight of polyvinyl alcohol to form a paste. This paste was applied to copper expanded metal, then dried and pressurized to form a metal cadmium with a capacity of 800 iAh and dimensions of 2°9 x 14 x 52 (nr
A negative electrode plate of m) was manufactured.

一方、正極板は次の方法で製作した。On the other hand, the positive electrode plate was manufactured by the following method.

二酸化マンガン(γ−MnO2)80重量部とグラファ
イト10f!量部とを60重量%のポリテトラフルオロ
エチレンの水性デイスパージョン301で混練した後、
ローラーでシート状にし、20メツシユのニッケル網に
両面からさらに加圧して理論容量が2001lAh、寸
法が1.4 x 14x 52(ll)の正極板を製作
した。
80 parts by weight of manganese dioxide (γ-MnO2) and 10f of graphite! After kneading the following parts with 60% by weight of polytetrafluoroethylene aqueous dispersion 301,
It was formed into a sheet using a roller and further pressed from both sides against a 20-mesh nickel mesh to produce a positive electrode plate with a theoretical capacity of 2001 mAh and dimensions of 1.4 x 14 x 52 (ll).

次に先の負極板1枚を厚さ0.2nnのポリビニルアル
コール製の不織布で包んだ後、正極板2枚の間にはさみ
、電解液として比重1.350  (20℃)の水酸化
カリウム水溶液を2.71用い、公称容量が240iA
hで合成樹脂電槽を用いた角形二酸化マンガン−カドミ
ウム電池(E)を製作した。この電池は外径寸法が67
x 16.5X 8(+111)であり、0.1kg/
c12で作動する安全弁を有している。
Next, one negative electrode plate was wrapped in a non-woven fabric made of polyvinyl alcohol with a thickness of 0.2 nn, and then sandwiched between two positive electrode plates, and an aqueous potassium hydroxide solution with a specific gravity of 1.350 (20°C) was used as the electrolyte. 2.71, the nominal capacity is 240iA
A prismatic manganese dioxide-cadmium battery (E) using a synthetic resin battery case was manufactured in 1.h. This battery has an outer diameter of 67
x 16.5X 8 (+111) and 0.1kg/
It has a safety valve that operates at c12.

[比較例2] 実施例6の負極板の配合から三二酸化ニッケルを削除し
た以外は全て実施例6と同様にして比較例の角形二酸化
マンガン−カドミウム電池(F)を製作した。
[Comparative Example 2] A prismatic manganese dioxide-cadmium battery (F) of a comparative example was manufactured in the same manner as in Example 6 except that nickel sesquioxide was omitted from the formulation of the negative electrode plate of Example 6.

以上のようにして製作した電池(E)および([)を0
.2CAの電流で100nAh放電し、次いで同じ電流
で1.6vまで充電するという条件で充放電したときの
容量推移の結果を第3図に示した。
The batteries (E) and ([) produced as above are 0
.. FIG. 3 shows the results of the change in capacity when charging and discharging were performed under the conditions of discharging 100 nAh with a current of 2 CA, and then charging to 1.6 V with the same current.

第3図から充電効率が優れ、かつ充電効率のサイクルに
おける低下がほとんどない負極板を有する本発明の電池
(E)は、比教電池(F)に比べて明らかに容量低下が
小さく、1oooサイクルを経過してもほとんど容量が
低下しなかった。
As can be seen from FIG. 3, the battery (E) of the present invention, which has a negative electrode plate with excellent charging efficiency and almost no decrease in charging efficiency during cycles, has a clearly smaller capacity decrease than the Hikyo battery (F), and has a 1ooo cycle. There was almost no decrease in capacity even after 30 days.

なお、これらの電池のリザーブ用水酸化カドミウムはほ
とんど含まれていない状態となっている。
Note that these batteries contain almost no reserve cadmium hydroxide.

つまり、負極板に含まれる水酸化カドミウムの含有量は
重量比で常に正極活物質の二酸化マンガンの約0.84
倍[2,73(q/Ah)/2.34 ((1/Ah)
]となっている。
In other words, the content of cadmium hydroxide contained in the negative electrode plate is always about 0.84 of the manganese dioxide of the positive electrode active material in terms of weight ratio.
times [2,73(q/Ah)/2.34 ((1/Ah)
].

以上にニッケルーカドミウム電池および二酸化マンガン
−カドミウム電池を例にとって説明したが、正極活物質
として酸化銀を用いても充電制御が容易な酸化銀−カド
ミウム電池を得ることができる。
Although the above description has been made using a nickel-cadmium battery and a manganese dioxide-cadmium battery as examples, a silver oxide-cadmium battery with easy charge control can be obtained even if silver oxide is used as the positive electrode active material.

[実施例7] 金属カドミウム粉末100重量部と三二酸化ニッケル2
重量部と長さ111のポリプロピレン製の短繊維0.1
重量部とを1.5重量%のポリビニルアルコールを含む
エチレングリコール30m lで混合してペースト状に
する。このペーストをカドミウムメツキ(5μm)シた
銅のエクスパンデッドメタルに塗着し、次いで乾燥、加
圧して金属カドミウムの理論容量が1000nAhで寸
法が3x 14x 52(Ill)の負極板を製作した
[Example 7] 100 parts by weight of metal cadmium powder and 2 parts of nickel sesquioxide
Short fibers made of polypropylene with weight part and length 111 0.1
parts by weight and mixed with 30 ml of ethylene glycol containing 1.5% by weight of polyvinyl alcohol to form a paste. This paste was applied to expanded copper metal plated with cadmium (5 μm), then dried and pressurized to produce a negative electrode plate with a theoretical capacity of 1000 nAh and dimensions of 3 x 14 x 52 (Ill).

一方、正極板は以下の方法で製作した。On the other hand, the positive electrode plate was manufactured by the following method.

活物質である酸化銀粉末と集を体である銀のエクスパン
デッドメタルとを常法によって加圧焼結したものを水酸
化カリウム水溶液中で電解酸化した後水洗、乾燥して理
論容量が500iAhで寸法が1゜3 x 14x 5
2(nIl)の正極板を製作した。
Silver oxide powder as an active material and expanded silver metal as an aggregate are sintered under pressure using a conventional method, electrolytically oxidized in an aqueous potassium hydroxide solution, washed with water, and dried to have a theoretical capacity of 500 iAh. The dimensions are 1゜3 x 14x 5
A positive electrode plate of 2(nIl) was manufactured.

次に先の負極板1枚を厚さ0.02n11のセロファン
で4重に巻いた後に正極板2枚の間にはさみ、電解液と
して比重1.250(20℃)の水酸化カリウム水溶液
31を用いて公称容量が500mAhの角形酸化銀−カ
ドミウム電池(G)を製作した。外径寸法は67x 1
6.5x 8(ill)であり、電槽は合成樹脂製のも
のを用いた。また0、 5kg/cm”め圧力で作動す
る安全弁を取り付けている。
Next, one negative electrode plate was wrapped four times in cellophane with a thickness of 0.02n11, then sandwiched between two positive electrode plates, and a potassium hydroxide aqueous solution 31 with a specific gravity of 1.250 (20°C) was added as an electrolyte. Using this method, a prismatic silver oxide-cadmium battery (G) with a nominal capacity of 500 mAh was manufactured. Outer diameter size is 67x1
The size was 6.5 x 8 (ill), and the container was made of synthetic resin. Additionally, a safety valve is installed that operates at a pressure of 0.5kg/cm''.

[比較例3] 実施例7の負極板の配合から三二酸化ニッケルを削除し
た以外は全て実施例7と同様にして角形酸化銀−カドミ
ウム電池(H)を製作した。
[Comparative Example 3] A prismatic silver oxide-cadmium battery (H) was manufactured in the same manner as in Example 7 except that nickel sesquioxide was omitted from the formulation of the negative electrode plate in Example 7.

なお、これらの電池のリザーブ用水酸化カドミウムは、
はとんどない状態であり、負極板に含まれる水酸化カド
ミウムの含有量は重量比で常に正極活物質の銀の約1.
4倍[2,73((J/^h)/ 2.01((1/^
h)]となっている。
In addition, the cadmium hydroxide for the reserve of these batteries is
The content of cadmium hydroxide contained in the negative electrode plate is always about 1.0% by weight of the silver of the positive electrode active material.
4 times [2,73((J/^h)/2.01((1/^h)
h)].

以上のようにして製作した電池(G)および(H)を2
0℃で0.2CAの電流で300nAh放電した後に、
同じ電流で充電するという操作を繰り返した時の充電電
圧特性を第4図に示しな。
Batteries (G) and (H) manufactured as described above are
After discharging 300nA with a current of 0.2CA at 0°C,
Figure 4 shows the charging voltage characteristics when charging with the same current is repeated.

第4図から本発明の酸化銀−カドミウム電池(G)の充
電終期の電圧上昇は、比較電池[H)よりら遅くに起き
ており、その充電効率はほぼ100%である。この2つ
の電池の電圧上昇の時期が異なるのは負極板の充電効率
に基づくものであり、本発明の電池は優れた容量保持率
を有することが明らかである。
From FIG. 4, the voltage rise at the end of charging of the silver oxide-cadmium battery (G) of the present invention occurs later than that of the comparative battery [H), and its charging efficiency is approximately 100%. The difference in the timing of the voltage rise of these two batteries is based on the charging efficiency of the negative electrode plate, and it is clear that the battery of the present invention has an excellent capacity retention rate.

以上の実施例で本発明のカドミウム負極板および電池の
特性について説明した。
The characteristics of the cadmium negative electrode plate and battery of the present invention have been explained in the above examples.

本発明のカドミウム負極板の集電体としては、各実施例
で説明したように、その表面がニッケル。
As explained in each example, the surface of the current collector of the cadmium negative electrode plate of the present invention is nickel.

銅あるいはカドミウムであればよい、つまり、その素材
としてはニッケル、銅、カドミウムの他に鉄の表面にニ
ッケル、@あるいはカドミウムの層を有するものや、ニ
ッケルの表面に銅あるいはカドミウムの層を有するもの
、さらに銅の表面にカドミウムの層を有するものである
Any material such as copper or cadmium is sufficient; in other words, in addition to nickel, copper, and cadmium, the material is one that has a layer of nickel, @, or cadmium on the surface of iron, or one that has a layer of copper or cadmium on the surface of nickel. , which also has a cadmium layer on the copper surface.

またその形状としてはエクスパンデッドメタル。Its shape is expanded metal.

網、穿孔板1発泡体あるいは繊維マットが使用できる。Netting, perforated foam or fiber mats can be used.

発明の効果 以上に述べたように本発明のカドミウム負極板は充電効
率が極めて高いために、不活性な水酸化カドミウムをほ
とんど有していない、従って従来のカドミウム負極板に
比べて実質的な容量密度は高くなる。
Effects of the Invention As stated above, the cadmium negative electrode plate of the present invention has extremely high charging efficiency, so it contains almost no inert cadmium hydroxide, and therefore has a substantial capacity compared to conventional cadmium negative electrode plates. Density increases.

また、これを用いたアルカリ二次電池では正・負極活物
質の量比を調節することによって充電制御が容易で、か
つICA以上の大電流による超急速充電が可能である。
In addition, in an alkaline secondary battery using this, charging control is easy by adjusting the ratio of the positive and negative electrode active materials, and ultra-rapid charging is possible with a large current higher than ICA.

また、この電池にはリザーブ用の水酸化カドミウムがほ
とんど必要でないために高容量化が可能である。
Moreover, this battery requires almost no cadmium hydroxide for reserve, so it is possible to increase the capacity.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明のカドミウム負極板において、三二酸
化ニッケルの含有率と充電効率との関係について示した
図、第2図は、本発明のニッケルーカドミウム電池と比
較のための電池との充放電サイクルにおける容量保持率
を示した図、第3図は本発明の二酸化マンガン−カドミ
ウム電池と比較のための電池との充放電サイクルにおけ
る容量保持率を示した図、第4図は本発明の酸化銀−カ
ドミウム電池と比較のための電池との充電特性を示した
図。 力 r r 殆う已 I【道イイフル数 / 田 第L(目 戸 /D。 rv λ!:O え立1rイ2 1I−社 / (n た 電 崎 閏 / k。
Figure 1 shows the relationship between the content of nickel sesquioxide and charging efficiency in the cadmium negative electrode plate of the present invention, and Figure 2 shows the relationship between the nickel-cadmium battery of the present invention and a battery for comparison. Figure 3 shows the capacity retention rate during charge/discharge cycles of the manganese dioxide-cadmium battery of the present invention and a comparative battery; Figure 4 shows the capacity retention rate during charge/discharge cycles of the manganese dioxide-cadmium battery of the present invention. FIG. 3 is a diagram showing the charging characteristics of a silver oxide-cadmium battery and a battery for comparison.力r r almost 已I [道Iiifuru number / Tadai L (Medo / D. rv λ!: O erate 1r ii 2 1I-sha / (n Ta Denzaki Jun / k.

Claims (1)

【特許請求の範囲】 1、全カドミウム量に対し0.25重量%以上20重量
%以下の三二酸化ニッケルを含有することを特徴とする
カドミウム負極板。 2、水酸化ニッケル、二酸化マンガンあるいは酸化銀の
いずれかを活物質の主体とする正極板と請求項1記載の
カドミウム負極板とを備えたことを特徴とするアルカリ
二次電池。
[Scope of Claims] 1. A cadmium negative electrode plate containing 0.25% by weight or more and 20% by weight or less of nickel sesquioxide based on the total amount of cadmium. 2. An alkaline secondary battery comprising a positive electrode plate whose active material is either nickel hydroxide, manganese dioxide or silver oxide, and a cadmium negative electrode plate according to claim 1.
JP63309611A 1988-12-07 1988-12-07 Cadmium negative plate and alkaline secondary battery using this negative plate Pending JPH02155165A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63309611A JPH02155165A (en) 1988-12-07 1988-12-07 Cadmium negative plate and alkaline secondary battery using this negative plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63309611A JPH02155165A (en) 1988-12-07 1988-12-07 Cadmium negative plate and alkaline secondary battery using this negative plate

Publications (1)

Publication Number Publication Date
JPH02155165A true JPH02155165A (en) 1990-06-14

Family

ID=17995112

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63309611A Pending JPH02155165A (en) 1988-12-07 1988-12-07 Cadmium negative plate and alkaline secondary battery using this negative plate

Country Status (1)

Country Link
JP (1) JPH02155165A (en)

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