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JPH0810596B2 - Metal oxide / hydrogen battery - Google Patents
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JPH0810596B2 - Metal oxide / hydrogen battery - Google Patents

Metal oxide / hydrogen battery

Info

Publication number
JPH0810596B2
JPH0810596B2 JP61107614A JP10761486A JPH0810596B2 JP H0810596 B2 JPH0810596 B2 JP H0810596B2 JP 61107614 A JP61107614 A JP 61107614A JP 10761486 A JP10761486 A JP 10761486A JP H0810596 B2 JPH0810596 B2 JP H0810596B2
Authority
JP
Japan
Prior art keywords
hydrogen
hydrogen storage
battery
negative electrode
metal oxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61107614A
Other languages
Japanese (ja)
Other versions
JPS62264557A (en
Inventor
えり子 矢ケ崎
慎司 鶴田
優治 佐藤
基 神田
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP61107614A priority Critical patent/JPH0810596B2/en
Priority to US06/872,844 priority patent/US4696873A/en
Priority to CA000512075A priority patent/CA1279095C/en
Priority to DE8686304743T priority patent/DE3677831D1/en
Priority to EP86304743A priority patent/EP0206776B1/en
Publication of JPS62264557A publication Critical patent/JPS62264557A/en
Publication of JPH0810596B2 publication Critical patent/JPH0810596B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889Manganese, technetium or rhenium
    • B01J23/8892Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/83Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • 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
    • H01M4/242Hydrogen storage 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
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/383Hydrogen absorbing alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • 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)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) この発明は、金属酸化物を正極活物質とし水素を負極
活物質とするいわゆる金属酸化物・水素素二次電池に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application] The present invention relates to a so-called metal oxide / hydrogen secondary battery using a metal oxide as a positive electrode active material and hydrogen as a negative electrode active material.

(従来の技術) 現在、金属酸化物・水素電池において、水素負極を水
素吸蔵合金で構成した形式のものが注目を集めている。
その理由は、この電池系が元来高エネルギー密度を有
し、容積効率的に有利であり、しかも安全作動が可能で
あって、特性的にも信頼度の点でも優れているからであ
る。
(Prior Art) Currently, in a metal oxide / hydrogen battery, a type in which a hydrogen negative electrode is composed of a hydrogen storage alloy is drawing attention.
The reason is that this battery system originally has a high energy density, is advantageous in volumetric efficiency, can operate safely, and is excellent in characteristics and reliability.

この形式の電池の水素負極に用いる水素吸蔵合金とし
ては、従来から、LaNi5が多用されている。また、La,C
e,Pr,Nd,Smなどのランタン系元素の混合物であるミッシ
ュメタル(以下Mmと指称する)とNiとの合金、すなわち
MmNi5も広く用いられている。このほかLaCo5,SmCo5など
の希土類元素とCoとの合金もしばしば用いられている。
As a hydrogen storage alloy used for the hydrogen negative electrode of this type of battery, LaNi5 has been frequently used. Also, La, C
An alloy of Ni with a misch metal (hereinafter referred to as Mm) that is a mixture of lanthanum-based elements such as e, Pr, Nd, and Sm, that is,
MmNi 5 is also widely used. In addition, alloys of rare earth elements such as LaCo 5 and SmCo 5 with Co are often used.

このような水素吸蔵合金を用いた場合、その電池内圧
は水素吸蔵合金を使用しない電池の内圧(50kg/cm2
下)に比べてたしかに低くなることは事実である。しか
しながら、その値は常温においても依然として2〜5kg/
cm2程度であって、例えばニッケルカドミウム電池の内
圧(0〜1kg/cm2)に比べれば高い値である。
When such a hydrogen storage alloy is used, the internal pressure of the battery is certainly lower than the internal pressure (50 kg / cm 2 or less) of a battery not using the hydrogen storage alloy. However, the value is still 2-5kg / at room temperature.
The value is about cm 2 , which is higher than the internal pressure (0 to 1 kg / cm 2 ) of a nickel-cadmium battery, for example.

電池内圧が大気圧よりも高い場合には、電池容器の構
造をある程度堅牢にすることが必要であることと並ん
で、特性的には次のような不都合な事態を惹起する。第
1の問題は、電池内の水素分子はその分子径が小さく、
そのため電池容器から徐々にせよ漏洩することが不可避
であり、安全性を著しく損なうこと:第2の問題は、第
1の現象の結果、水素負極から吸蔵されている水素が放
出されて電池容量は低下し自己放電を招くことである。
When the internal pressure of the battery is higher than the atmospheric pressure, along with the fact that the structure of the battery container needs to be robust to some extent, the following inconvenient situation is characteristically caused. The first problem is that the molecular size of hydrogen molecules in the battery is small,
Therefore, it is unavoidable that the battery gradually leaks from the battery container, and the safety is significantly impaired. The second problem is that as a result of the first phenomenon, hydrogen stored in the hydrogen negative electrode is released and the battery capacity is It causes a decrease and causes self-discharge.

このようなことから、水素負極には平衡プラトー圧の
低い水素吸蔵合金を使用することが提案され、各種の合
金の研究が進められている。
Under such circumstances, it has been proposed to use a hydrogen storage alloy having a low equilibrium plateau pressure for the hydrogen negative electrode, and various alloys have been studied.

例えば、LaNi5,MmNi5に関していえば、常温における
それぞれの平衡プラトー圧は約3気圧,15気圧と高いの
で、これらを負極材料として使用した電池では前述の安
全性低下および自己放電招来という不都合が生ずる。
For example, with regard to LaNi 5 and MmNi 5 , the equilibrium plateau pressures at room temperature are high at about 3 atm and 15 atm, respectively, so batteries using these as negative electrode materials suffer from the above-mentioned inconvenience of reduced safety and self-discharge. Occurs.

一方、たとえこの平衡プラトー圧は低くても吸蔵し得
る水素量が小さい水素吸蔵合金を負極材料として構成し
た電池では、つぎのような問題点が惹起される。まず第
1に、水素吸蔵量が小さいので充電可能な電池容量が小
さくなること:第2に充電容量が小さいため、過充電状
態になりやすく、その結果として気体状の水素が発生し
やすいことである。過充電時の水素発生は電池圧内上昇
をもたらすので、電池の安全性を損なう。
On the other hand, even if the equilibrium plateau pressure is low, the battery having the hydrogen storage alloy having a small amount of hydrogen that can be stored as the negative electrode material has the following problems. Firstly, because the hydrogen storage capacity is small, the battery capacity that can be charged is small. Secondly, because the charging capacity is small, the battery tends to be overcharged, and as a result, gaseous hydrogen is easily generated. is there. Hydrogen generation during overcharging raises the internal pressure of the battery, thus impairing the safety of the battery.

以上の点を考えあわせると、水素負極の材料として
は、平衡プラトー圧が低く、かつ水素吸蔵量が大きい水
素吸蔵合金を使用することが望ましいといえる。
Considering the above points, it can be said that it is desirable to use a hydrogen storage alloy having a low equilibrium plateau pressure and a large hydrogen storage amount as the material of the hydrogen negative electrode.

例えば既知の水素吸蔵合金であるLaCo5,LaNi1.5Co3.5
の室温付近の平衡プラトー圧はそれぞれ0.1気圧,0.2気
圧と低いが、しかしながら3気圧以下で吸蔵し得る水素
量はLaNi5の約60%でしかない(H.H.Van Mal,K,H.J.Bu
schow and F.A.Kuijpers,J.Less−Comon Metals,32,
289(1973))。従って、これらを負極材料とした電池
では、容量が小さく過充電状態になりやすいという問題
が生じる。
For example, the known hydrogen storage alloys LaCo 5 , LaNi 1.5 Co 3.5
The equilibrium plateau pressure near room temperature is as low as 0.1 atm and 0.2 atm, respectively, however, the amount of hydrogen that can be stored at 3 atm or less is only about 60% of LaNi 5 (HHVan Mal, K, HJBu
schow and FAKuijpers, J. Less-Comon Metals, 32 ,
289 (1973)). Therefore, a battery using these as a negative electrode material has a problem that it has a small capacity and is likely to be overcharged.

また、すでに水素吸蔵合金電極の材料として使用され
た報告もあるLa−Ni−Co系合金(J.J.G.Willems,Philps
J.Res,39,1(1984))やMm−Ni−Co系合金の場合に
は、先のLa−Ni−Mm系合金やMm−Ni−Mn系合金に比べて
平衡プラトー圧をさらに低下させることは可能である
が、この種の合金は水素吸蔵量が充分に得られないとい
う問題を有していた。
In addition, there are reports that it has already been used as a material for hydrogen storage alloy electrodes (JJGWillems, Philps
J. Res, 39 , 1 (1984)) and Mm-Ni-Co alloys further lower the equilibrium plateau pressure compared to the previous La-Ni-Mm alloys and Mm-Ni-Mn alloys. Although it is possible to do so, this type of alloy has a problem that a sufficient hydrogen storage capacity cannot be obtained.

このように、金属酸化物・水素電池の負極材料として
の水素吸蔵合金には、水素吸蔵量が大きくかつ平衡プラ
トー圧が低いという特性が必要とされる。しかし、これ
らの特性を共にもつ水素吸蔵合金を使用した場合でも、
実際の電池系ではしばしば次のような不都合を生じる。
まず第1には、金属酸化物・水素二次電池の電極には、
電解液中で充分放電を繰り返しても容量が低下しないと
いう長寿命特性が求められるが、水素吸蔵合金がアルカ
リ水溶液中の充放電に対して化学的に不安定であると、
少ない充放電の繰り返しで電池の寿命が尽きてしまうと
いう問題がある。第2に、水素吸蔵合金電極の理論容量
は合金の水素吸蔵量から計算できるが、水素吸蔵量の大
きい合金を使用した場合でも理論容量に満たない小さな
電気容量しか測定されないことが多いという問題があ
る。
As described above, the hydrogen storage alloy as the negative electrode material of the metal oxide / hydrogen battery is required to have characteristics that the hydrogen storage amount is large and the equilibrium plateau pressure is low. However, even when using a hydrogen storage alloy that has both of these characteristics,
In actual battery systems, the following disadvantages often occur.
First of all, the electrode of the metal oxide / hydrogen secondary battery is
Long life characteristics that the capacity does not decrease even after repeating sufficient discharge in the electrolytic solution are required, but when the hydrogen storage alloy is chemically unstable with respect to charge and discharge in an alkaline aqueous solution,
There is a problem that the life of the battery will be exhausted by repeated charge and discharge. Second, the theoretical capacity of the hydrogen storage alloy electrode can be calculated from the hydrogen storage capacity of the alloy, but even if an alloy with a large hydrogen storage capacity is used, only a small electric capacity that is less than the theoretical capacity is often measured. is there.

第1の問題点に関しては、例えばMmNi4.5Mn0.5やMnNi
4.2Mn0.8合金といった従来より多用されている合金を負
極材料とした電極では、初期には充電容量に対し100%
の放電が可能であるが、約100回の充放電サイクルで80
%に、約150回で50%に容量が低下してしまう。これは
電解液中での充放電サイクルに対して負極材料である水
素吸蔵合金が化学的に安定でないことが原因であると考
えられており、長寿命化のためにはこのような化学的安
定性をも要求される。このような電極の科学的安定性
は、例えばAlを成分として少量含有する水素吸蔵合金を
材料として使用した場合に得られ、電極は長寿命となる
(特開昭61−2269号)。また、Al,Cr,Siのような元素の
含有によって表面に閉鎖された酸化物層が生じるため水
素吸蔵合金が耐腐蝕性をもつともいわれている(特開昭
60−89066号)。
Regarding the first problem, for example, MmNi 4.5 Mn 0.5 or MnNi
In the case of an electrode using a negative electrode material such as a 4.2 Mn 0.8 alloy, which has been widely used in the past, the initial charge was 100% of the charging capacity.
Can be discharged, but 80 in about 100 charge / discharge cycles
%, The capacity will be reduced to 50% after about 150 times. This is considered to be due to the fact that the hydrogen storage alloy, which is the negative electrode material, is not chemically stable with respect to the charge / discharge cycle in the electrolytic solution, and such a chemical stability is required for extending the life. Sex is also required. Such scientific stability of the electrode is obtained, for example, when a hydrogen storage alloy containing a small amount of Al as a component is used as the material, and the electrode has a long life (JP-A-61-2269). Further, it is said that the hydrogen storage alloy has corrosion resistance because a closed oxide layer is formed on the surface due to the inclusion of elements such as Al, Cr and Si.
60-89066).

第2の問題点は、水素吸蔵合金粉末を高分子結着材を
用いて電極に成形する際に、合金粉末粒子間の接触が不
完全で電気的に接続されていない合金粒子が生じてしま
うことに起因している。すなわち、充放電時に電流の流
れない水素吸蔵合金の粒子は水素の吸蔵・放出を行なら
ず、電極の容量に全く寄与しないために電極の容量は理
論容量よりも小さくなる。従来より、電気抵抗を小さく
するために水素吸蔵合金粉末にアセチレンブラックを混
入した例(特公昭57−30273号)はあるが、このような
問題点に着眼して解決した金属酸化物・水素電池はな
い。
A second problem is that when the hydrogen-absorbing alloy powder is molded into an electrode using a polymer binder, alloy particles that are not electrically connected due to incomplete contact between the alloy powder particles are generated. It is due to that. That is, the particles of the hydrogen storage alloy, to which current does not flow during charging / discharging, do not store and release hydrogen and do not contribute to the capacity of the electrode at all, so that the capacity of the electrode becomes smaller than the theoretical capacity. Conventionally, there is an example (Japanese Patent Publication No. 57-30273) in which acetylene black is mixed into a hydrogen storage alloy powder to reduce electric resistance, but a metal oxide / hydrogen battery solved by focusing on such a problem. There is no.

以上述べたように、金属酸化物・水素電池の負極に
は、水素吸蔵量が大きく平衡プラトー圧が低くかつ電解
液中での充放電に対して科学的に安定な水素吸蔵合金を
用いること、および合金粒子相互が電気的に良く接触し
ていることが必要とされるが、これらをすべて満足する
ような水素吸蔵合金電極はこれまでに得られていない。
よって金属酸化物・水素電池に求められている大容量で
あり、かつ内圧上昇が防止され水素漏洩の危険が少なく
安定性にすぐれており、自己放電も少なくて長寿命であ
るという特性をすべて有した電池はつくりえなかった。
As described above, for the negative electrode of the metal oxide / hydrogen battery, use a hydrogen storage alloy that has a large hydrogen storage capacity, a low equilibrium plateau pressure, and is scientifically stable against charge / discharge in an electrolytic solution, It is required that the alloy particles and the alloy particles be in good electrical contact with each other, but no hydrogen storage alloy electrode satisfying all of them has been obtained so far.
Therefore, it has all the characteristics of large capacity required for metal oxide / hydrogen batteries, increased internal pressure, reduced risk of hydrogen leakage, excellent stability, low self-discharge, and long life. I couldn't make the battery.

(発明が解決しようとする問題点) 本発明は、水素漏洩や破裂の危険を防止しかつ短期間
に寿命が尽きるという問題を解消し、さらに電極の容量
が期待される容量よりも小さくなるという問題を解決す
るものである。すなわち本発明の目的は、安全性に優
れ、自己放電も少なく、大容量を有し、かつ長寿命であ
る金属酸化物・水素電池を提供することである。
(Problems to be Solved by the Invention) The present invention solves the problem of preventing the risk of hydrogen leakage and rupture and ending the life in a short time, and further, the capacity of the electrode is smaller than the expected capacity. It solves the problem. That is, an object of the present invention is to provide a metal oxide / hydrogen battery which is excellent in safety, has less self-discharge, has a large capacity, and has a long life.

[発明の構成] (問題点を解決するための手段) 本発明者らは水素吸蔵合金を材料とする電池負極につ
いて研究を重ねた結果、適当な組成を有する水素吸蔵合
金粉末と適当な大きさの導電性粉末とをともに含む電極
を用いることで、前記問題点が解決されることを見出し
た。
[Structure of the Invention] (Means for Solving the Problems) As a result of repeated research on the battery negative electrode using a hydrogen storage alloy as a material, the present inventors have found that a hydrogen storage alloy powder having an appropriate composition and an appropriate size. It was found that the above-mentioned problems can be solved by using an electrode containing both of the conductive powder of 1.

すなわち、本発明の金属酸化物・水素電池は、正極
と、アルカリ電解液と、セリウム(Ce)を含む少なくと
も2種類以上の希土類元素を含んだ希土類系水素吸蔵合
金を主材料としてなる負極とを備えた金属酸化物・水素
電池において、 前記Ce含有量が前記希土類元素の総量に対して0.1重
量%以上10重量%以下でありかつ負極の副材料として平
均粒計10μm以下の導電性粉末を含むことを特徴とす
る。
That is, the metal oxide / hydrogen battery of the present invention comprises a positive electrode, an alkaline electrolyte, and a negative electrode mainly composed of a rare earth-based hydrogen storage alloy containing at least two kinds of rare earth elements including cerium (Ce). A metal oxide / hydrogen battery provided, wherein the Ce content is 0.1% by weight or more and 10% by weight or less with respect to the total amount of the rare earth elements, and a conductive powder having an average particle size of 10 μm or less is included as a negative electrode auxiliary material It is characterized by

本発明に用いるのに好ましい水素吸蔵合金としては特
に次式 MNixCoyMnzAlw ……(I) (式中MはCeを含む少なくとも2種以上の希土類元素
(イットリウムを含む))で示されるものがあげられ
る。そして希土類元素成分M以外の成分であるNi,Co,M
n,Alはそのすべてが適量含まれるとき、すなわち組成式
中のx,y,z,wが、 3.5<x≦4.4 ……… 0.05<y≦1.2 ……… 0.05<z≦1.2 ……… 0.05<w≦0.6 ……… 4.7≦x+y+z+w≦5.4 ……… のすべての関係を満たすときに、充分な水素吸蔵量、低
い平衡プラトー圧、電解液中での化学的安定性に関して
良好な特性が得られる。x,y,z,wは、後述する各成分の
作用を勘案して〜式の範囲内で定められる。なお本
発明に係る合金の組成は、その製造時に入る不可避的な
不純物を除くものではない。この不可避的な不純物とし
ては例えばFe,Cu,Sn等があげられる。
Particularly preferred hydrogen storage alloys for use in the present invention are those represented by the following formula MNi x Co y Mn z Al w (I) (wherein M is at least two rare earth elements (including yttrium) containing Ce). The ones shown are: And Ni, Co, M which is a component other than the rare earth element component M
When all of n and Al are contained in appropriate amounts, that is, x, y, z, w in the composition formula are 3.5 <x ≦ 4.4 ………… 0.05 <y ≦ 1.2 ……… 0.05 <z ≦ 1.2 ……… 0.05 <w ≦ 0.6 ……… 4.7 ≦ x + y + z + w ≦ 5.4 ……… If all the relations are satisfied, good hydrogen storage capacity, low equilibrium plateau pressure, and good chemical stability in the electrolyte can get. x, y, z, w are determined within the range of the formula by considering the action of each component described later. The composition of the alloy according to the present invention does not exclude inevitable impurities that enter during the production thereof. Examples of the inevitable impurities include Fe, Cu, Sn and the like.

また導電性粉末は、例えばCu,Ni,Fe,Al等の金属粉末
があってもよいし、活性炭や黒鉛、アセチレンブラッ
ク,ケッチェンブラック等の炭素粉末でもよいし、ある
いはこれらの混合物や活性炭上に金属微粒子を担持させ
てもよい。特にこうした金属微粒子としてはPt等の貴金
属微粒子を担持させた場合には。上述の水素吸蔵合金粒
子相互の電気的接触が確保されることによる大容量化や
電気抵抗の低下による大電流での充放電特性の向上とい
った効果に加えて、さらにセル内圧の上昇を防止する効
果も顕著となる。正極に金属酸化物、負極に水素吸蔵合
金を使用した電池で、過充電を行なった場合には通常、
充電末期に正極から酸素ガスの発生が見られる。この酸
素ガスは負極表面で水素と反応して水となるので、放電
するかあるいは開路状態で長時間放置すれば内圧は低下
するものである。貴金属微粒子は、この酸素と水素が結
合して水になる化学反応を速めるので、充電中にも酸素
はガス状態にならず内圧上昇は起こらない。また、極端
な過充電時に酸素ガス発生が起こっても貴金属微粒子を
含有している場合には、セル内圧は低位に迎えられ、放
電時あるいは放置時の内圧低下も速く、安全性に優れて
いる。貴金属としては、その触媒能の大きさからPtが最
も優れており、次いでPh,Ruなど、またAg,Auなどが適当
である。
The conductive powder may be metal powder such as Cu, Ni, Fe and Al, carbon powder such as activated carbon, graphite, acetylene black, Ketjen black, or a mixture thereof or activated carbon. The metal fine particles may be supported on the. Especially when such noble metal particles such as Pt are supported as such metal particles. In addition to the effect of increasing the capacity by ensuring electrical contact between the hydrogen-absorbing alloy particles described above and improving the charging / discharging characteristics at large current due to a decrease in electrical resistance, an effect of further preventing an increase in cell internal pressure Will also be noticeable. In a battery that uses a metal oxide for the positive electrode and a hydrogen storage alloy for the negative electrode, normally when overcharged,
Oxygen gas is generated from the positive electrode at the end of charging. Since this oxygen gas reacts with hydrogen on the surface of the negative electrode to become water, the internal pressure decreases if discharged or left for a long time in an open circuit state. Since the noble metal particles accelerate the chemical reaction of the oxygen and hydrogen to be combined with each other to form water, the oxygen does not become a gas state and the internal pressure does not rise even during charging. In addition, when the noble metal particles are contained even if oxygen gas is generated during extreme overcharging, the cell internal pressure reaches a low level and the internal pressure drops rapidly during discharge or when left alone, which is excellent in safety. . As the noble metal, Pt is the most excellent because of its catalytic ability, and then Ph, Ru, etc., and Ag, Au, etc. are suitable next.

本発明の貴金属酸化物・水素電池は次に延べるような
方法で製造することができる。
The noble metal oxide / hydrogen battery of the present invention can be manufactured by the following method.

金属酸化物よりなる正極としては、例えば金属ニッケ
ルの焼結体に水酸化ニッケル(Ni(OH))のような活
物質を含浸、化成して成るニッケル酸化物(NiOOH)の
電極を用いることができる。
As the positive electrode made of a metal oxide, for example, a nickel oxide (NiOOH) electrode obtained by impregnating and forming an active material such as nickel hydroxide (Ni (OH) 2 ) in a sintered body of metal nickel is used. You can

水素負極の材料である水素吸蔵合金は、目的組成から
決められる各成分元素粉末の所定量を混合し、その混合
粉末を例えば真空アーク溶解炉で溶解することにより均
一溶体として得ることができる。さらに、この固溶体を
粉砕するか、あるいは常温で大気圧以上の圧力の水素雰
囲気中に置くというような活性化処理を施することによ
り容易にその粉末体を調整することができる。このよう
にして調整した水素吸蔵合金粉末は、電池負極を作成す
る際に水素を放出した状態であってもよいし、部分的に
水素を吸蔵した状態であってもよい。この水素吸蔵合金
粉末と例えば活性炭のような導電性粉末、および例えば
テトラフルオロエチレンのような結着剤を混合したのち
混練しシート状に成形し、このシートと集電体あるいは
リードとを例えば圧着するなどして電池の水素負極を製
造することができる。
The hydrogen storage alloy, which is the material of the hydrogen negative electrode, can be obtained as a uniform solution by mixing a predetermined amount of each component element powder determined from the target composition and melting the mixed powder in, for example, a vacuum arc melting furnace. Further, the powder body can be easily prepared by crushing the solid solution or subjecting it to an activation treatment such as placing it in a hydrogen atmosphere at a pressure of atmospheric pressure or higher at room temperature. The hydrogen storage alloy powder prepared in this manner may be in a state of releasing hydrogen or may be in a state of partially storing hydrogen when the battery negative electrode is produced. The hydrogen storage alloy powder, a conductive powder such as activated carbon, and a binder such as tetrafluoroethylene are mixed and then kneaded to form a sheet, and the sheet and the current collector or the lead are bonded by, for example, pressure bonding. The hydrogen negative electrode of the battery can be manufactured by, for example,

このようにして得られた正極及び負極とをナイロンや
ポリプロピレン製のセパレーターで絶縁し、KOHやNaOH
等のアルカリ水溶液からなる電解液に浸積して本発明に
係る金属酸化物・水素電池が構成される。
Insulate the positive electrode and negative electrode thus obtained with a separator made of nylon or polypropylene, and use KOH or NaOH.
The metal oxide / hydrogen battery according to the present invention is constructed by immersing the electrolyte in an electrolytic solution containing an alkaline aqueous solution such as.

(作用) 本発明に係る水素吸蔵合金の希土類成分であるMとし
ては、Ce及び他の1種以上の希土類元素をあらかじめ所
定の割合で用意したものを用いることもできるが、安価
に入手できる事から通常のミッシュメタルからCeを部分
的に除去した希土類元素の混合物を用いることが望まし
い。このCe量としては、Mに対して0.1〜10重量%であ
れば電池負極材料として充分大きい水素吸蔵量と充分低
い平衡プラトー圧を有し、さらに0.1〜8重量%であれ
ば一層好ましい。Ce量が12重量%を越えた場合あるいは
0.1重量%未満の場合では寿命特性が悪化してしまう。
そして特に0.1重量%以上8重量%以下の場合には長寿
命化が達成される。このCeは希土類元素中唯一4価の酸
化物となり得るので容易に除去し得る。また好ましい組
成として示した前記(I)式における水素吸蔵合金の希
土類以外の金属成分量では、Ni量については、x≦3.5
では水素吸蔵量が減少し、4.4<xでは平衡プラトー圧
が上昇して問題を生じる。Coは平衡プラトー圧を低下さ
せる作用をもつ成分であり、Co量が1.2<yでは水素吸
蔵量が減少し、一方ごく微量すなわちy≦0.05の場合で
はCoを含有させることによる効果が有効に生かされない
という問題を生じる。Mnは、水素吸蔵量を維持しつつ平
衡プラトー圧を低下させる作用をもち、その量は0.05<
z≦1.2が適当である。Mn量が1.2<zとなって過剰とな
ると水素吸蔵量の低下をきたし、一方Mn量がごく微量す
なわちz≦0.05の場合ではMnを含有させたことによる効
果が充分に得られない。CoとMnはともに含有されたと
き、いずれか一方のみの含有よりも優れた効果を発揮す
る。Coを含みMnを含まない場合には平衡プラトー圧は低
下するが水素吸蔵量の現象が顕著に起こり、逆にMnを含
みCoを含まない場合には平衡プラトー圧の低下が不充分
となる。Alは電解液中で合金を化学的に安定に保つ作用
をもつ成分であり、電池の長寿命化に寄与する。その量
は、0.05<w≦0.6が好ましく、0.6<wでは水素吸蔵量
が減少し電極の容量低下をきたし、w≦0.05では化学的
安定化の作用が不充分で電池の長寿命化まで至らない。
また、前記式の希土類元素以外の成分の総量に関して
いえば、式の範囲をはずれる組成の合金では、典型的
な水素吸蔵合金であるLaNi5型の構造から大きく歪んだ
構造になるために水素吸蔵量が減少して好ましくない。
なお、上述した合金の組成は、その製造時に入る不可避
的な不純物を除くものではない。原料鉱の産地によって
は、Feがしばしば不純物として含有されることがある
し、炉や容器からの不純物混入も起こり得るものであ
る。
(Function) As M, which is a rare earth component of the hydrogen storage alloy according to the present invention, Ce and one or more other rare earth elements prepared in a predetermined ratio may be used in advance, but they should be inexpensively available. Therefore, it is desirable to use a mixture of rare earth elements obtained by partially removing Ce from ordinary misch metal. If the Ce amount is 0.1 to 10% by weight with respect to M, it has a sufficiently large hydrogen storage amount as a battery negative electrode material and a sufficiently low equilibrium plateau pressure, and is more preferably 0.1 to 8% by weight. If the amount of Ce exceeds 12% by weight, or
If it is less than 0.1% by weight, the life characteristics will deteriorate.
In particular, when the content is 0.1% by weight or more and 8% by weight or less, a long life is achieved. This Ce can be easily removed because it can be the only tetravalent oxide in the rare earth elements. Further, in the amount of metal components other than rare earth elements of the hydrogen storage alloy in the above formula (I) shown as a preferable composition, the amount of Ni is x ≦ 3.5.
Hydrogen storage capacity decreases, and equilibrium plateau pressure rises at 4.4 <x, causing a problem. Co is a component that has the effect of lowering the equilibrium plateau pressure. When the Co content is 1.2 <y, the hydrogen storage capacity decreases, while when the amount is very small, that is, y ≦ 0.05, the effect of including Co is effective. The problem of not being produced arises. Mn has a function of lowering the equilibrium plateau pressure while maintaining the hydrogen storage amount, and the amount is 0.05 <
z ≦ 1.2 is suitable. When the amount of Mn becomes 1.2 <z and becomes excessive, the hydrogen storage amount decreases, while when the amount of Mn is very small, that is, when z ≦ 0.05, the effect due to the inclusion of Mn cannot be sufficiently obtained. When both Co and Mn are contained, the effect is superior to that of only one of Co and Mn. When Co is included and Mn is not included, the equilibrium plateau pressure decreases, but the phenomenon of hydrogen storage amount remarkably occurs. Conversely, when Mn is included and Co is not included, the equilibrium plateau pressure is insufficiently decreased. Al is a component that acts to keep the alloy chemically stable in the electrolytic solution, and contributes to extending the battery life. The amount is preferably 0.05 <w ≦ 0.6, and when 0.6 <w, the hydrogen storage amount decreases and the capacity of the electrode decreases, and when w ≦ 0.05, the chemical stabilization action is insufficient and the battery life is extended. Absent.
Further, regarding the total amount of components other than the rare earth element in the above formula, in an alloy having a composition outside the range of the formula, a hydrogen storage capacity is greatly distorted from the structure of a typical hydrogen storage alloy LaNi 5 type. The amount is reduced, which is not preferable.
The composition of the alloy described above does not exclude inevitable impurities that enter during the production thereof. Depending on the origin of the raw material ore, Fe is often contained as an impurity, and it is possible for impurities to be mixed from the furnace or vessel.

本発明に係る導電性粉末は平均粒径10μm以下である
ことが必要である。本発明で用いる平均粒径は、粉末を
SEMで拡大撮影して測定した値を用いて算出した。水素
吸蔵合金に水素による活性化を施して粉末としたときに
は、その粒径はおよそ2〜70μm程度となり平均粒径は
20〜30μmとなる。機械的に粉砕した場合でも電極成形
後、電池として充放電を施すと水素による微粉化と同様
の平均粒径をもつ粒子となる。よってこのような大きさ
の水素吸蔵合金粒子相互の電気的接触を確保するために
は、負極内に共存する導電性粒子の平均粒径は10μm以
下であることが必要となる。これより水素吸蔵合金粒子
が相互に電気的に良く接触され、これより電極の充放電
時に水素を吸蔵・放出しない独立した合金粒子がなくな
って、大容量を有する電極となり、これを負極とする金
属酸化物・水素電池も大容量となる。この導電性粒子が
10μmを越えていると水素吸蔵合金粒子と同等ないしそ
れ以上の大きさとなり、導電性粉末の含有量が少ない場
合には孤立した水素吸蔵合金粒子が存在して電極の電気
容量が不充分となるし、多い場合には電気的接触は確保
されるが電極中に体積的に含み得る水素吸蔵合金粒子量
が減少して電極の容量低下をきたす。従って、平均粒径
20〜30μmの合金粒子間の電気的接触を確保するという
作用を充分に発揮し、かつ電極中に占める総体積が過剰
になることを避けるという理由から導電性粉末の大きさ
が制限され、平均粒径10μm以下が適当となる。
The conductive powder according to the present invention needs to have an average particle size of 10 μm or less. The average particle size used in the present invention is the powder
It was calculated by using the value measured by magnifying with SEM. When the hydrogen storage alloy is activated by hydrogen to form a powder, the particle size is about 2 to 70 μm, and the average particle size is
20 to 30 μm. Even when mechanically pulverized, when the battery is charged and discharged after forming the electrode, particles having an average particle size similar to that of hydrogen atomization are obtained. Therefore, in order to secure electrical contact between the hydrogen storage alloy particles having such a size, the average particle diameter of the conductive particles coexisting in the negative electrode needs to be 10 μm or less. As a result, the hydrogen-absorbing alloy particles are in good electrical contact with each other, and as a result, there is no separate alloy particle that does not occlude or release hydrogen during charge / discharge of the electrode, resulting in an electrode with a large capacity, which is used as the negative electrode metal. Oxide / hydrogen batteries will also have a large capacity. These conductive particles
If it exceeds 10 μm, the size becomes equal to or larger than the hydrogen storage alloy particles, and if the content of the conductive powder is small, isolated hydrogen storage alloy particles exist and the electric capacity of the electrode becomes insufficient. However, when the number is large, electrical contact is secured, but the amount of hydrogen storage alloy particles that can be contained volumetrically in the electrode decreases, resulting in a decrease in the capacity of the electrode. Therefore, the average particle size
The size of the conductive powder is limited because the effect of ensuring electrical contact between alloy particles of 20 to 30 μm is sufficiently exerted and the total volume occupied in the electrode is prevented from becoming excessive, and the average size of the conductive powder is limited. A particle size of 10 μm or less is suitable.

導電性粉末としては金属粉末や活性炭等の炭素粉末、
あるいは粉末状触媒などが適当であるが、比重が小さい
との理由から炭素粉末ないし炭素粉末を担体とした触媒
粉末が特に好ましい。比重の大きな金属粉末の含有は電
極の重量増加をもたらすが、活性炭粉末などではその含
有による重量増加はわずかでほとんど無視できるからで
ある。導電性粉末の含有量は導電性粉末の種類や粒径に
よって異なるが、炭素粉末の場合電極重量の0.05〜10重
量%以下で前述の作用が得られる。特に平均粒径0.005
〜1μmの微細な炭素粉末の場合には5重量%以下の含
有量でも充分な効果が得られ好ましい。なお、このよう
な導電性粉末の含有は、電気抵抗低下の効果もあわせも
つのであり、電極の大電流による充放電特性を同時に向
上する。
As the conductive powder, carbon powder such as metal powder or activated carbon,
Alternatively, a powdery catalyst or the like is suitable, but a carbon powder or a catalyst powder having a carbon powder as a carrier is particularly preferable because of its low specific gravity. This is because the inclusion of metal powder having a large specific gravity causes an increase in the weight of the electrode, but in the case of activated carbon powder or the like, the increase in weight due to the inclusion is slight and can be almost ignored. The content of the conductive powder varies depending on the type and particle size of the conductive powder, but in the case of carbon powder, the above-mentioned effect can be obtained at 0.05 to 10% by weight or less of the electrode weight. Especially average particle size 0.005
In the case of a fine carbon powder of ˜1 μm, a content of 5% by weight or less is preferable because a sufficient effect can be obtained. It should be noted that the inclusion of such a conductive powder also has the effect of lowering the electrical resistance, and simultaneously improves the charge / discharge characteristics of the electrode due to the large current.

(実施例) 以下に本発明につき実施例に基づいて更に詳細に説明
する。
(Example) Hereinafter, the present invention will be described in more detail based on examples.

実施例1 (1)負極の形成 M,Ni,Co,Mn,Alの各金属元素の粉末をそれぞれ所定量
混合し、得られた混合粉末を真空アーク溶解炉で溶解し
て、組成がMNi4.2Co0.2Mn0.3Al0.3となる合金の均一固
溶体を得た。Mとしては市販のミッシュメタルからCeの
1部を除去した希土類元素の混合物を用いた。Mの組成
の分析値は La:45.10重量%,Nd:37.01重量%,Pr:12.07重量%,Ce:4.
60重量%,Sm:1.06重量%,Eu:0.06重量%,Dy:0.05重量
%,Tb:0.03重量%,Lu:0.02重量%であった。この固溶体
を直径約5mmに破砕し、ついでこれを真空ポンプおよび
水素ボンベに接続された容器中に入れ、10-3Torr以下の
真空に室温で1時間保ったのち、水素を導入し、圧力約
10kg/cm2の水素雰囲気下に室温で1〜数時間保持するこ
とによって微粉化させた。再び1時間以上10-3Torr以下
に保って室温〜60℃の範囲で脱気した後、合金の粉末を
容器から取り出した。得られた合金粉末の平均粒径は約
25μmであった。
Example 1 (1) Formation of Negative Electrode Powders of metal elements M, Ni, Co, Mn, and Al were mixed in predetermined amounts, and the obtained mixed powder was melted in a vacuum arc melting furnace to have a composition of MNi 4.2. A uniform solid solution of an alloy that becomes Co 0.2 Mn 0.3 Al 0.3 was obtained. As M, a mixture of rare earth elements obtained by removing a part of Ce from commercially available misch metal was used. The analysis values of the composition of M are La: 45.10 wt%, Nd: 37.01 wt%, Pr: 12.07 wt%, Ce: 4.
The content was 60% by weight, Sm: 1.06% by weight, Eu: 0.06% by weight, Dy: 0.05% by weight, Tb: 0.03% by weight, Lu: 0.02% by weight. This solid solution was crushed to a diameter of about 5 mm, then placed in a container connected to a vacuum pump and a hydrogen cylinder, kept at a vacuum of 10 -3 Torr or less at room temperature for 1 hour, then hydrogen was introduced, and the pressure was adjusted to about
It was pulverized by keeping it at room temperature for 1 to several hours under a hydrogen atmosphere of 10 kg / cm 2 . The alloy powder was taken out of the container again after being degassed at room temperature to 60 ° C. for 1 hour or more and 10 −3 Torr or less. The average particle size of the obtained alloy powder is about
It was 25 μm.

この合金粉末と平均粒径0.03μmの市販のアセチレン
・ブラック粉末および結着剤のテトラフルオロエチレン
の粉末を重量比95.5:0.5:4の割合で混合した後混練して
厚さ0.5mmのシートに形成した。このシートをSEMで拡大
撮影して観察したところ、結着剤は繊維状になって水素
吸蔵合金粒子を保持しており、その間隙を炭素の微粒子
が接続していた。
This alloy powder, commercially available acetylene black powder with an average particle size of 0.03 μm and tetrafluoroethylene powder as a binder were mixed in a weight ratio of 95.5: 0.5: 4 and then kneaded to form a 0.5 mm thick sheet. Formed. When the sheet was magnified and observed by SEM, the binder became fibrous and retained the hydrogen-absorbing alloy particles, and carbon particles were connected to the gaps.

得られたシート2枚を、1枚のニッケルネットの両面
から圧着して一体化し、厚み0.7mmの電極を形成しこれ
を負極とした。
The obtained two sheets were pressure-bonded from both sides of one nickel net to be integrated to form an electrode having a thickness of 0.7 mm, which was used as a negative electrode.

(2)正極の形成 多孔質のニッケル焼結体Ni(OH)を含浸し、これを
化成処理してNiOOH電極を形成しこれを正極とした。
(2) Formation of Positive Electrode A porous nickel sintered body Ni (OH) 2 was impregnated and subjected to chemical conversion treatment to form a NiOOH electrode, which was used as a positive electrode.

(3)電池の製造 以上の負極、正極、更には厚み0.3mmのポリプロピレ
ン不織布をセパレータとし、8モル/のKOH水溶液を
電解液として第1図に示した電池を製造した。
(3) Manufacture of Battery The battery shown in FIG. 1 was manufactured by using the above negative electrode, positive electrode, and polypropylene nonwoven fabric having a thickness of 0.3 mm as a separator, and using 8 mol / KOH aqueous solution as an electrolytic solution.

第1図において、1は負極、2はセパレータ、3は正
極である。4および5はそれぞれ負極および正極の端子
であり、電池容器6とは電気的に独立して外部に取り出
されている。7は電解液である。本発明による負極1は
セパレータ2でU字型につつみ、その両側から正極3を
配置してアクリル製のホルダー8で密着させた。正極の
容量は負極の容量より充分大きくなるように設定し、電
池性能が負極の特性に支配される条件で以下の測定を行
なった、また、負極電位を測定するためにCd/Cd(OH)
参照極11を系内に入れリード12を外部へ取り出した。
In FIG. 1, 1 is a negative electrode, 2 is a separator, and 3 is a positive electrode. Reference numerals 4 and 5 respectively denote a negative electrode terminal and a positive electrode terminal, which are taken out to the outside electrically independently of the battery container 6. 7 is an electrolytic solution. The negative electrode 1 according to the present invention was wrapped in a U shape with the separator 2, and the positive electrode 3 was arranged from both sides of the negative electrode 1 and they were brought into close contact with each other by the acrylic holder 8. The capacity of the positive electrode was set to be sufficiently larger than the capacity of the negative electrode, and the following measurements were performed under the condition that the battery performance was governed by the characteristics of the negative electrode. Also, in order to measure the negative electrode potential, Cd / Cd (OH)
2 The reference electrode 11 was put in the system, and the lead 12 was taken out.

(4)電池特性 この電池に、水素吸蔵合金1g当たり0.17Aの電流密度
で充放電を繰り返したときの20サイクル目の放電特性を
第2図の特性図に曲線Aで示す。第2図において横軸は
合金1g当たりの放電容量、縦軸は参照極を基準とした負
極電位である。第2図の曲線Aより明らかなように本実
施例の電池はおよそ0.27Ahg-1という大容量をもってい
る。
(4) Battery characteristics The discharge characteristics at the 20th cycle when this battery was repeatedly charged and discharged at a current density of 0.17 A per gram of hydrogen storage alloy are shown by the curve A in the characteristic diagram of FIG. In FIG. 2, the horizontal axis represents the discharge capacity per 1 g of the alloy, and the vertical axis represents the negative electrode potential based on the reference electrode. As is clear from the curve A in FIG. 2, the battery of this example has a large capacity of about 0.27 Ahg -1 .

上記の放電特性測定後、充電容量0.17Ahg-1で充放電
サイクルを繰り返す寿命試験を行なったが、1000サイク
ルまで90%以上の放電容量を示した。
After measuring the above-mentioned discharge characteristics, a life test was conducted in which the charge and discharge cycles were repeated at a charge capacity of 0.17 Ahg -1 and a discharge capacity of 90% or more was shown up to 1000 cycles.

実施例2 負極中の導電性粉末がPtを10重量%担持した炭素粉末
であることを除いては実施例1と同様の電池を製造し、
同様の測定を行なった。本実施例では平均粒径0.03μm
の市販のアセチレン・ブラック粉末に塩化白金酸溶液か
らPtを含浸させ蒸発乾固させた後、高温で水素によって
還元してPtを担持した粉末を作成して用いた。この電池
の放電特性を第3図に曲線Bで示す。本実施例でもやは
り実施例1と同様に大容量を示した。また寿命特性も実
施例1と同様1000サイクルまで充電容量0.17Ahg-1に対
し90%以上の放電容量を示した。
Example 2 A battery similar to that of Example 1 was manufactured except that the conductive powder in the negative electrode was a carbon powder carrying 10% by weight of Pt.
The same measurement was performed. In this embodiment, the average particle size is 0.03 μm
The commercially available acetylene black powder of Pt was impregnated with Pt from a chloroplatinic acid solution, evaporated to dryness, and then reduced with hydrogen at a high temperature to prepare a Pt-supported powder. The discharge characteristic of this battery is shown by curve B in FIG. Also in this example, a large capacity was shown as in Example 1. Also, as with Example 1, the life characteristics showed a discharge capacity of 90% or more with respect to a charge capacity of 0.17 Ahg -1 up to 1000 cycles.

比較例1 負極中に導電性粉末を含まないことを除いては実施例
1と同様の電池を製造した。ただしMNi4.2Co0.2Mn0.3Al
0.3合金粉末とテトラフルオロエチレンの重量比は96:4
とした。
Comparative Example 1 A battery similar to that of Example 1 was manufactured except that the negative electrode contained no conductive powder. However, MNi 4.2 Co 0.2 Mn 0.3 Al
The weight ratio of 0.3 alloy powder and tetrafluoroethylene is 96: 4
And

実施例1,2と同様の電流密度、充電容量で放電特性を
測定したが、第3図に曲線Cで示すように本比較例では
0.21Ahg-1の容量しか得られなかった。また、放電特性
測定後、0.17Ahg-1の充電容量で充放電サイクルを繰り
返したところ660サイクルで90%(0.153Ahg-1)以下の
容量となった。
The discharge characteristics were measured with the same current density and charge capacity as in Examples 1 and 2, but in this comparative example as shown by the curve C in FIG.
Only a capacity of 0.21 Ahg -1 was obtained. After the discharge characteristics were measured, the charge and discharge cycles were repeated at a charge capacity of 0.17 Ahg -1 and the capacity was 90% (0.153 Ahg -1 ) or less after 660 cycles.

比較例2 負極材料である水素吸蔵合金の組成がNmNi4.2Mn0.8で
導電性材料を含まない電池を実施例1と同様の方法で製
造した。Mmの組成の分析値は、La:26.31重量%,Nb:14.3
4重量%,Pr:15.37重量%,Ce:43.30重量%,Sm:0.65重量
%であった。合金粉末とテトラルオロチレンの重量比は
96:4とした。
Comparative Example 2 A battery in which the composition of the hydrogen storage alloy as the negative electrode material was NmNi4.2Mn0.8 and no conductive material was contained was manufactured in the same manner as in Example 1. The analytical value of the composition of Mm is La: 26.31% by weight, Nb: 14.3
The content was 4% by weight, Pr: 15.37% by weight, Ce: 43.30% by weight, Sm: 0.65% by weight. The weight ratio of alloy powder and tetraluorotylene is
It was 96: 4.

実施例1,2と同様の電流密度、充電容量で放電特性を
測定したが、第2図に曲線Dで示すように本比較例では
約0.20Ahg-1の容量しか得られなかった。また、0.17Ahg
-1の充電容量で充放電サイクルを繰り返したところ約10
0サイクルで90%(0.153Ahg-1)以下の放電容量しか得
られなくなった。
The discharge characteristics were measured with the same current density and charge capacity as in Examples 1 and 2, but as shown by the curve D in FIG. 2, in this comparative example, only a capacity of about 0.20 Ahg -1 was obtained. Also, 0.17Ahg
About 10 were repeated charging and discharging cycle in the charging capacity of -1
Only 0% of discharge capacity (0.153 Ahg -1 ) was obtained at 0 cycles.

同組成の合金を用いた実施例1,2と比較例1の電池の
寿命特性にも差が生じているのは、負極中に含まれる合
金量は等しくとも、導電性粉末を含まない比較例1にお
いては、孤立した水素吸蔵合金粉末には電流が流れない
ために有効に使用されている水素吸蔵合金粉末に対する
電流密度が実施例1,2に比べて大きくなったことによ
る。
The difference in the life characteristics of the batteries of Examples 1 and 2 and Comparative Example 1 using the alloys of the same composition is that Comparative Example containing no conductive powder even if the amount of alloy contained in the negative electrode was the same. In No. 1, the current density does not flow in the isolated hydrogen storage alloy powder, so that the current density for the hydrogen storage alloy powder that is effectively used is larger than that in Examples 1 and 2.

[発明の効果] 本発明による金属酸化物・水素電池は大きな理論容量
をもち、内圧上昇の危険が防止され自己放電や水素漏洩
も少なく、かつ長寿命の電池であり、さらに電極内の水
素吸蔵合金粒子相互の電気的接触がより確実に保持され
電極の容量が大幅に向上する。
[Effects of the Invention] The metal oxide / hydrogen battery according to the present invention is a battery having a large theoretical capacity, preventing the risk of internal pressure rise, reducing self-discharge and hydrogen leakage, and having a long life. The electrical contact between the alloy particles is more reliably maintained, and the capacity of the electrode is significantly improved.

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

第1図は本発明に係る電池の概略断面図、第2図は本発
明による電池ならびに比較例の電池の放電特性を示した
特性図である。 1……負極、2……セパレータ、3……正極、4……負
極の端子、5……正極の端子、6……電池容器、7……
電解液、8……ホルダー、9……絶縁ガスケット、10…
…O−リング、11……参照極、12……参照極の端子
FIG. 1 is a schematic sectional view of a battery according to the present invention, and FIG. 2 is a characteristic diagram showing discharge characteristics of a battery according to the present invention and a battery of a comparative example. 1 ... Negative electrode, 2 ... Separator, 3 ... Positive electrode, 4 ... Negative electrode terminal, 5 ... Positive electrode terminal, 6 ... Battery container, 7 ...
Electrolyte, 8 ... Holder, 9 ... Insulation gasket, 10 ...
… O-ring, 11 …… reference electrode, 12 …… reference electrode terminal

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】正極と、アルカリ電解液と、セリウムを含
む少なくとも2種以上の希土類元素を含んだ希土類系水
素吸蔵合金を主材料としてなる負荷とを備えた金属酸化
物・水素電池において、該負極の前記セリウムの含有量
が前記希土類元素の総量に対して0.1重量%以上10重量
%以下であり、かつ負極の副材料として平均粒径10μm
以下の導電性粉末を含むことを特徴とする金属酸化物・
水素電池。
1. A metal oxide / hydrogen battery comprising a positive electrode, an alkaline electrolyte, and a load containing a rare earth-based hydrogen storage alloy containing at least two rare earth elements containing cerium as a main material. The content of cerium in the negative electrode is 0.1% by weight or more and 10% by weight or less with respect to the total amount of the rare earth elements, and the average particle diameter of 10 μm is used as a secondary material of the negative electrode.
Metal oxide characterized by containing the following conductive powder
Hydrogen battery.
【請求項2】負極の主材料である希土類系水素吸蔵合金
が MNixCoyMnzAlw (式中Mはセリウムを含む少なくとも2種以上の希土類
元素;x,y,z,wはそれぞれMの1グラム原子に対する原子
比を表し、 3.5<x≦4.4,0.05<y≦1.2, 0.05<z≦1.2,0.05<w≦0.6, 4.7≦x+y+z+w≦5.4の関係を満足する数を表
す。)で示される水素吸蔵合金であることを特徴とする
特許請求の範囲第1項記載の金属酸化物・水素電池。
2. A rare earth-based hydrogen storage alloy, which is the main material of the negative electrode, is MNi x Co y Mn z Al w (where M is at least two or more rare earth elements containing cerium; x, y, z, w are respectively It represents the atomic ratio of M to 1 gram atom, and represents a number satisfying the relationship of 3.5 <x ≦ 4.4, 0.05 <y ≦ 1.2, 0.05 <z ≦ 1.2, 0.05 <w ≦ 0.6, 4.7 ≦ x + y + z + w ≦ 5.4. The metal oxide / hydrogen battery according to claim 1, which is a hydrogen storage alloy represented by:
【請求項3】セリウムの含有量が希土類元素の総量に対
して0.1重量%以上8重量%以下であることを特徴とす
る特許請求の範囲第1項および第2項のいずれかに記載
の金属酸化物・水素電池。
3. The metal according to claim 1, wherein the content of cerium is 0.1% by weight or more and 8% by weight or less based on the total amount of rare earth elements. Oxide / hydrogen battery.
【請求項4】導電性粉末が炭素粉末であることを特徴と
する特許請求の範囲第1項記載の金属酸化物・水素電
池。
4. The metal oxide / hydrogen battery according to claim 1, wherein the conductive powder is carbon powder.
【請求項5】導電性粉末が平均粒径0.005μm以上1μ
m以下の炭素粉末であることを特徴とする特許請求の範
囲第4項記載の金属酸化物・水素電池。
5. The conductive powder has an average particle size of 0.005 μm or more and 1 μm.
The metal oxide / hydrogen battery according to claim 4, characterized in that the carbon powder is m or less.
JP61107614A 1985-06-21 1986-05-13 Metal oxide / hydrogen battery Expired - Lifetime JPH0810596B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP61107614A JPH0810596B2 (en) 1986-05-13 1986-05-13 Metal oxide / hydrogen battery
US06/872,844 US4696873A (en) 1985-06-21 1986-06-11 Rechargeable electrochemical cell with a negative electrode comprising a hydrogen absorbing alloy including rare earth component
CA000512075A CA1279095C (en) 1985-06-21 1986-06-20 Rechargeable electrochemical cell with a negative electrode comprising a hydrogen absorbing alloy including rare earth component
DE8686304743T DE3677831D1 (en) 1985-06-21 1986-06-20 RECHARGEABLE ELECTROCHEMICAL CELL WITH A NEGATIVE ELECTRODE MADE FROM A HYDROGEN ABSORBING ALLOY CONTAINING A RARE EARTH ELEMENT.
EP86304743A EP0206776B1 (en) 1985-06-21 1986-06-20 Rechargeable electrochemical cell with a negative electrode comprising a hydrogen absorbing alloy including rare earth component

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61107614A JPH0810596B2 (en) 1986-05-13 1986-05-13 Metal oxide / hydrogen battery

Publications (2)

Publication Number Publication Date
JPS62264557A JPS62264557A (en) 1987-11-17
JPH0810596B2 true JPH0810596B2 (en) 1996-01-31

Family

ID=14463636

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61107614A Expired - Lifetime JPH0810596B2 (en) 1985-06-21 1986-05-13 Metal oxide / hydrogen battery

Country Status (1)

Country Link
JP (1) JPH0810596B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0677450B2 (en) * 1986-06-13 1994-09-28 松下電器産業株式会社 Sealed nickel-hydrogen battery
JP3177653B2 (en) * 1989-03-08 2001-06-18 日本電池株式会社 Method for producing hydrogen storage electrode
GB0229079D0 (en) * 2002-12-12 2003-01-15 Univ Southampton Electrochemical cell for use in portable electronic devices
SE541537C2 (en) * 2017-11-28 2019-10-29 Nilar Int Ab Milling of recovered negative electrode material

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58198856A (en) * 1982-05-14 1983-11-18 Matsushita Electric Ind Co Ltd Manufacturing method of cadmium negative electrode plate for alkaline storage batteries
JPS61288371A (en) * 1985-06-17 1986-12-18 Sanyo Electric Co Ltd Hydrogen occlusion electrode

Also Published As

Publication number Publication date
JPS62264557A (en) 1987-11-17

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