JPH07101607B2 - Manufacturing method of hydrogen storage electrode - Google Patents
Manufacturing method of hydrogen storage electrodeInfo
- Publication number
- JPH07101607B2 JPH07101607B2 JP62098939A JP9893987A JPH07101607B2 JP H07101607 B2 JPH07101607 B2 JP H07101607B2 JP 62098939 A JP62098939 A JP 62098939A JP 9893987 A JP9893987 A JP 9893987A JP H07101607 B2 JPH07101607 B2 JP H07101607B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- paste
- hydrogen
- electrode
- storage alloy
- 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 - Fee Related
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
- H01M4/242—Hydrogen storage electrodes
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/383—Hydrogen absorbing alloys
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、水素を可逆的に吸蔵・放出する水素吸蔵合金
を用いる水素吸蔵電極の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for manufacturing a hydrogen storage electrode using a hydrogen storage alloy that stores and releases hydrogen reversibly.
従来の技術 各種の電源のうち二次電池としては、鉛蓄電池とアルカ
リ蓄電池とが広く使われている。2. Description of the Related Art Lead storage batteries and alkaline storage batteries are widely used as secondary batteries among various power sources.
そのうちアルカリ蓄電池には、ニッケル−カドミウム蓄
電池が大半を占め、焼結式ニッケル極の実用化が利用の
範囲を大きく広げた。Of these, nickel-cadmium storage batteries accounted for the majority of alkaline storage batteries, and the practical use of sintered nickel electrodes greatly expanded the range of applications.
この電池は放電特性の店で優れ、高率放電を行なっても
電圧や容量の低下が少ない。また、寿命も長く、過充電
など苛酷な条件にも耐え、低温での性能もよい。This battery has excellent discharge characteristics, and the voltage and capacity are not significantly reduced even when discharged at a high rate. It also has a long life, withstands harsh conditions such as overcharging, and has excellent low-temperature performance.
ところが高エネルギー密度に対する対応には、なお相当
の努力が必要である。正極については、例えば発泡状ニ
ッケル極などが実用化されたが、負極のカドミウム極に
ついては、現在のところあまり顕著な進歩はない。However, considerable effort is still needed to deal with high energy densities. With respect to the positive electrode, for example, a foamed nickel electrode has been put into practical use, but with respect to the cadmium electrode of the negative electrode, no significant progress has been made so far.
例えばこの中で負極のカドミウムに代わって亜鉛が取り
上げられている。一次電池用としては成功しているが、
よく知られているように充放電時での変形、樹枝状析出
などによる寿命の問題があるので特殊用の域を出ていな
い。For example, zinc is taken up in place of cadmium in the negative electrode. Although it has been successful for primary batteries,
As is well known, there is a problem of life due to deformation during charging / discharging, dendritic precipitation, etc., so it is not beyond the special range.
そこで最近注目されてきたのは水素を可逆的に吸蔵・放
出する水素吸蔵合金を用いた水素極である。宇宙用に採
用されている水素ガス拡散電極方式と異なり、この場合
は、カドミウムや亜鉛などと同じ取扱いで電池を構成で
き、実際の放電可能な容量密度をカドミウムより大きく
できることや亜鉛のようなデンドライトの形成や電極の
形状変化などがないことから、高エネルギー密度で長寿
命、無公害のアルカリ蓄電池として有望である。Therefore, what has recently attracted attention is a hydrogen electrode using a hydrogen storage alloy that stores and releases hydrogen reversibly. Unlike the hydrogen gas diffusion electrode method used for space, in this case, a battery can be constructed in the same way as cadmium and zinc, and the actual dischargeable capacity density can be made larger than that of cadmium, and dendrites such as zinc. Since it does not cause the formation of electrodes and changes in the shape of electrodes, it is promising as a high energy density, long-life, pollution-free alkaline storage battery.
この水素吸蔵合金を用いた水素吸蔵電極の製造方法とし
ては、従来から水素吸蔵合金を多孔性導電体と共に焼結
して電極を得る焼結体や発泡金属や金属繊維、パンチン
グメタルやエキスパンドメタル、金属ネットなどの多孔
性導電体に水素吸蔵合金を結着剤などと共に充填した方
式がよく用いられていた。これらに用いられる水素吸蔵
合金は粉末状であり、一般には機械的な粉砕で粉末化さ
れている。一方この粉砕を水素ガスでの水素化と脱水素
化で行なう例も特開昭53−103910号公報などで知られて
いる。As a method for producing a hydrogen storage electrode using this hydrogen storage alloy, conventionally, a sintered body to obtain an electrode by sintering a hydrogen storage alloy together with a porous conductor or a foam metal or metal fiber, punching metal or expanded metal, A method in which a porous conductor such as a metal net is filled with a hydrogen storage alloy together with a binder and the like is often used. The hydrogen storage alloy used for these is in powder form, and is generally pulverized by mechanical pulverization. On the other hand, an example in which this pulverization is carried out by hydrogenation and dehydrogenation with hydrogen gas is also known from JP-A-53-103910.
発明が解決しようとする問題点 水素吸蔵合金を用いた水素吸蔵電極はこのように高エネ
ルギー密度の向上には有効であるが、これまでのとこ
ろ、アルカリ蓄電池の水素吸蔵合金負極に使用する際に
次のような問題があった。すなわち、水素の吸蔵と放
出、つまり充電と放電を繰返すと、合金粉末の微粉化が
進み電極が変形したり、粉末の脱落が生じたりする。こ
のことによって、電極の性能低下を招くことがある。ま
た、粉砕を水素ガスでの水素化と脱水素化で行なうこと
は効果的である半面、非常に水素吸蔵合金が化学的に活
性な状態になっており、これにより酸化を受けやすく酸
化により水素吸蔵能力が低下し、先と同様に水素吸蔵電
極の性能低下を起こしやすい問題があった。Problems to be Solved by the Invention Although a hydrogen storage electrode using a hydrogen storage alloy is effective in improving high energy density as described above, so far, when it is used for a hydrogen storage alloy negative electrode of an alkaline storage battery, There were the following problems. That is, when hydrogen is occluded and released, that is, charging and discharging are repeated, the alloy powder is pulverized, the electrodes are deformed, and the powder is dropped. This may lead to a decrease in electrode performance. While it is effective to carry out pulverization by hydrogenation and dehydrogenation with hydrogen gas, the hydrogen storage alloy is in a chemically active state, which makes it vulnerable to oxidation and hydrogen There has been a problem that the storage capacity is lowered and the performance of the hydrogen storage electrode is likely to be lowered as before.
本発明はこの水素吸蔵合金をアルカリ蓄電池の水素吸蔵
合金負極に使用する際に、これまで問題であった微粉化
や電極の酸化などを解決し、高性能で長寿命な水素吸蔵
電極の簡易な製造方法を提供することを目的にする。The present invention, when using this hydrogen storage alloy in a hydrogen storage alloy negative electrode of an alkaline storage battery, solves problems such as pulverization and electrode oxidation, which have been problems so far, and realizes a high-performance and long-life hydrogen storage electrode with a simple structure. It is intended to provide a manufacturing method.
問題点を解決するための手段 本発明は、水素吸蔵合金を圧力容器に収納し、水素ガス
での水素化と、脱水素化を行ない微粉末とし、その後、
この水素吸蔵合金粉末に直接ペースト用溶液を導入しペ
ースト化し、得られたペーストを多孔性導電体に充てん
することを特徴とする水素吸蔵電極の製造方法である。Means for Solving the Problems The present invention is to store a hydrogen storage alloy in a pressure vessel, perform hydrogenation with hydrogen gas, and dehydrogenate to obtain fine powder, and then
A method for producing a hydrogen storage electrode, characterized in that a paste solution is directly introduced into this hydrogen storage alloy powder to form a paste, and the obtained paste is filled in a porous conductor.
また、水素ガスでの水素化と、脱水素化を行ない、前記
水素化と脱水素化により微粉末化が不十分な部分だけを
除く工程が篩分法であり、その粒径が100ミクロン以下
であることがよい。Further, the step of performing hydrogenation with hydrogen gas and dehydrogenation, and removing only the portion where the fine powder is insufficient due to the hydrogenation and dehydrogenation is a sieving method, and the particle size is 100 microns or less. Be good.
作用 水素ガスでの水素化と、脱水素化を行なうことにより微
粉化が進むが、この方法による微粉化は機械的粉砕と比
較して、より微細な粉末が得られそのことによって水素
吸蔵電極で充放電を繰返してもそれ以上微粉化が進みに
くい。圧力容器内で水素ガスによる水素化と脱水素化を
繰返して微粉化した後に、この圧力容器に直接ペースト
用溶液を導入し水素吸蔵合金粉末をペースト化し、得ら
れたペーストを多孔性導電体に充てんしているので水素
吸蔵合金の酸化を促進することなく電極材料として用い
ることができるので長寿命化をはかれる。Action Hydrogenation with hydrogen gas and dehydrogenation lead to pulverization, but pulverization by this method produces finer powder than mechanical pulverization, which results in hydrogen storage electrodes. Even if charging and discharging are repeated, it is difficult to further reduce the pulverization. After pulverizing by repeating hydrogenation and dehydrogenation with hydrogen gas in a pressure vessel, the paste solution is directly introduced into this pressure vessel to make a hydrogen storage alloy powder into a paste, and the obtained paste is made into a porous conductor. Since it is filled, it can be used as an electrode material without accelerating the oxidation of the hydrogen storage alloy, so that the life can be extended.
実施例 以下、本発明の実施例について説明する。Examples Examples of the present invention will be described below.
水素吸蔵合金として市販のMm(ミッシュメタル),Ni,C
o,Mn,Alの各原材料を一定の組成比に秤量してアルゴン
アーク溶解炉によってMmNl3.7Co0.6Mn0.4Al0.3合金を製
造した。ついでこの合金を公知の方法に従って真空熱処
理炉で熱処理し、その後、第1図に示すような装置に収
納した。第1図は本発明の水素吸蔵電極の一製造装置で
ある。1〜10cm角程度の塊状の水素吸蔵合金1は、圧力
容器2の上部の粗い金属メッシュ3上に収納した。この
圧力容器2はガスバルブ4、溶液バルブ5、ペーストバ
ルブ6を有した密閉が可能な構造である。ガスバルブ4
は、真空引きや水素ガス導入に用い、溶液バルブ5は、
ペースト用溶液の導入用でありこの先にペースト用溶液
を噴出するためのノズル8が設けられている。そしてペ
ーストバルブ6は、ペーストの取り出し用である。また
圧力容器2内には篩分のためのメッシュ篩7を設けた。Commercially available Mm (Misch metal), Ni, C as hydrogen storage alloy
Raw materials of o, Mn, and Al were weighed to a constant composition ratio, and an MmNl 3.7 Co 0.6 Mn 0.4 Al 0.3 alloy was manufactured by an argon arc melting furnace. Then, this alloy was heat-treated in a vacuum heat treatment furnace according to a known method, and then housed in an apparatus as shown in FIG. FIG. 1 shows an apparatus for producing a hydrogen storage electrode of the present invention. The block-shaped hydrogen storage alloy 1 of about 1 to 10 cm square was stored on the coarse metal mesh 3 on the upper part of the pressure vessel 2. The pressure vessel 2 has a gas valve 4, a solution valve 5 and a paste valve 6 and has a structure capable of being hermetically sealed. Gas valve 4
Is used for evacuation and hydrogen gas introduction, and the solution valve 5 is
A nozzle 8 for introducing the paste solution and for ejecting the paste solution is provided ahead of this. The paste valve 6 is for taking out the paste. A mesh sieve 7 for sieving was provided in the pressure vessel 2.
第1図をもとに本発明の一実施例を説明する。まず水素
吸蔵合金1を収納した圧力容器2内をガスバルブ4を介
して真空ポンプにより脱ガスした。そして次に同じバル
ブ4から市販の水素ガスを導入し、約30気圧まで加圧し
た。これにより水素吸蔵合金1はまもなく水素吸蔵反応
を開始した。この水素化を充分行なった後、バルブ4か
ら水素ガスを放出し、放出を充分行なうために真空ポン
プにより脱ガスした。この水素化と脱水素化を3回繰返
すことにより、殆どの水素吸蔵合金1は粗い金属メッシ
ュ3を通過して圧力容器2の下部に集まった。そこで溶
液バルブ5を開き少量のペースト用溶液としてのポリビ
ニルアルコールの5%(重量)のエチレングリコール溶
液をノズル8から噴出させ、水素吸蔵合金粉末をペース
ト化させ、最後にペーストバルブ6を開いて圧力容器2
内から取り出した。なお、この場合圧力容器2内には篩
分のためのメッシュ篩7は設けていない。An embodiment of the present invention will be described with reference to FIG. First, the inside of the pressure vessel 2 accommodating the hydrogen storage alloy 1 was degassed by the vacuum pump via the gas valve 4. Then, commercially available hydrogen gas was introduced from the same valve 4 and pressurized to about 30 atm. As a result, the hydrogen storage alloy 1 soon started the hydrogen storage reaction. After sufficient hydrogenation was performed, hydrogen gas was released from the valve 4, and degassing was performed by a vacuum pump in order to sufficiently release the hydrogen gas. By repeating this hydrogenation and dehydrogenation three times, most of the hydrogen storage alloy 1 passed through the coarse metal mesh 3 and collected in the lower part of the pressure vessel 2. Then, the solution valve 5 is opened, and a small amount of a 5% (weight) solution of ethylene glycol as a paste solution is sprayed from the nozzle 8 to make the hydrogen storage alloy powder into a paste, and finally the paste valve 6 is opened to apply pressure. Container 2
I took it out from inside. In this case, the pressure vessel 2 is not provided with a mesh sieve 7 for sieving.
このようにして得られたペーストをさらに重量比で0.8
%のポリエチレン微粉末、同じく0.5%の塩化ビニル−
アクリロニトリル短繊維を加えて混練し、厚さ0.15mm、
孔径1.8mm、開孔度50%の鉄製でニッケルメッキを施し
たパンチングメタル板に塗着し、0.6mm幅のスリットを
通して平滑化し、その後120℃で1時間乾燥して水素吸
蔵電極を得た。このようにして得た水素吸蔵電極を電極
Aとする。The paste thus obtained is further mixed in a weight ratio of 0.8
% Polyethylene fine powder, also 0.5% vinyl chloride-
Add acrylonitrile short fibers and knead to a thickness of 0.15 mm,
It was applied to a nickel-made punching metal plate made of iron having a hole diameter of 1.8 mm and a porosity of 50%, smoothed through a slit having a width of 0.6 mm, and then dried at 120 ° C. for 1 hour to obtain a hydrogen storage electrode. The hydrogen storage electrode thus obtained is referred to as an electrode A.
次に、先と同様に水素化と脱水素化を3回繰返した後、
第1図に示すように圧力容器2を振動させ微細化した水
素吸蔵合金粉末を200メッシュのメッシュ篩7で篩分し
た。メッシュ篩7を通過した粉末は、その後先と同様に
ポリビニルアルコールの5%(重量)のエチレングリコ
ール溶液をノズル8から噴出させ水素吸蔵合金粉末をペ
ースト化させ、最後にペーストバルブ6を開いて圧力容
器2内から取り出した。このようにして得られたペース
トを同様に処理して水素吸蔵電極を得た。このようにし
て得た水素吸蔵電極を電極Bとする。Then, after repeating hydrogenation and dehydrogenation three times as before,
As shown in FIG. 1, the pressure vessel 2 was vibrated and the finely divided hydrogen storage alloy powder was sieved with a 200-mesh mesh sieve 7. The powder that has passed through the mesh sieve 7 is sprayed with a 5% (by weight) ethylene glycol solution of polyvinyl alcohol from the nozzle 8 to make the hydrogen storage alloy powder into a paste, and finally the paste valve 6 is opened to press the powder. It was taken out of the container 2. The paste thus obtained was treated in the same manner to obtain a hydrogen storage electrode. The hydrogen storage electrode thus obtained is designated as electrode B.
また比較のために水素化と脱水素化を行なった後篩分と
ペースト用溶液を噴出することなくアルゴンガスで置換
し20時間放置後水素吸蔵合金粉末を取り出しその後ペー
スト用溶液やポリエチレン微粉末などを添加し混練して
得た水素吸蔵電極を電極Cとして加えた。For comparison, after hydrogenation and dehydrogenation, the sieve and the paste solution were replaced with argon gas without being sprayed and left for 20 hours, then the hydrogen storage alloy powder was taken out and then the paste solution or polyethylene fine powder was used. Was added and kneaded to obtain a hydrogen storage electrode as an electrode C.
このようにして得た水素吸蔵電極A〜Cは、その後密閉
形ニッケル−水素二次電池として単2形で評価を行なっ
た。The hydrogen storage electrodes A to C obtained in this manner were then evaluated as a sealed nickel-hydrogen secondary battery in a C1 type.
すなわち、先の水素吸蔵電極を各々幅3.9cm長さ26cmに
裁断し、リード板を所定の2カ所にスポット溶液により
取り付けた。相手極としては、公知の発泡式ニッケル極
を選び、幅3.9cm長さ22cmとして用いた。この場合もリ
ード板を2カ所取り付けた。That is, each of the above-mentioned hydrogen storage electrodes was cut into a width of 3.9 cm and a length of 26 cm, and lead plates were attached to two predetermined places with a spot solution. A well-known foamed nickel electrode was selected as a counter electrode and used with a width of 3.9 cm and a length of 22 cm. Also in this case, the lead plates were attached at two places.
セパレータとしては、ポリアミド不織布、電解液として
は、比重1.30の苛性カリ水溶液に水酸化リチウムを30g/
1溶解して用いた。公称容量は3.0Ahである。As the separator, a polyamide nonwoven fabric, and as the electrolytic solution, 30 g of lithium hydroxide in a caustic potash aqueous solution having a specific gravity of 1.30 /
1 was used after dissolution. The nominal capacity is 3.0 Ah.
これらの電池を通常の充放電サイクル試験によって20℃
で評価した結果を説明する。These batteries are tested at 20 ° C by a normal charge / discharge cycle test.
The results evaluated in Section 2 will be explained.
充電は、0.2C(5時間率)で130%まで、放電は0.5C
(2時間率)で終止電圧0.8Vとし充放電サイクルを繰り
返し行なった。Charge up to 130% at 0.2C (5-hour rate), discharge at 0.5C
The final voltage was set to 0.8 V (at a rate of 2 hours), and the charge / discharge cycle was repeated.
その結果、電極Aを用いて構成した単2形密閉形ニッケ
ル−水素二次電池は、100サイクルの放電容量が3.12A
h、300サイクル3.11Ah、600サイクルで3.10Ahであり寿
命性能は、優れている。As a result, the AA sealed nickel-metal hydride rechargeable battery constructed by using the electrode A has a discharge capacity of 3.12 A at 100 cycles.
h, 300 cycles 3.11Ah, 600 cycles 3.10Ah, excellent life performance.
また電極Bで構成した電池は、100サイクルで3.16Ah、3
00サイクルで3.15Ah、600サイクルで3.15Ahと電極Aで
構成した電池以上に優れた性能を有していた。さらに電
極Cで構成した電池は当初公称容量の3.0Ahを満たして
いたものの100サイクルでは2.81Ahの放電容量が得られ
たに過ぎず、その後はサイクルの経過とともに急激に放
電容量が低下した。また電極Cで構成した電池は電極
A、電極Bで構成した電池と比較して放電電圧が低いこ
ともわかった。The battery composed of electrode B is 3.16Ah, 3 in 100 cycles.
The battery had superior performance to the battery composed of electrode A with 3.15 Ah at 00 cycles and 3.15 Ah at 600 cycles. Further, although the battery constituted by the electrode C initially satisfied the nominal capacity of 3.0 Ah, the discharge capacity of 2.81 Ah was only obtained in 100 cycles, and thereafter, the discharge capacity drastically decreased with the progress of the cycle. It was also found that the battery composed of the electrode C had a lower discharge voltage than the battery composed of the electrodes A and B.
このような電池を構成した充放電試験結果から水素ガス
での水素吸蔵と水素放出を行なった後、直接ペースト用
溶液を導入し水素吸蔵合金粉末をペースト化したことに
よる水素吸蔵電極A、および水素ガスでの水素吸蔵と水
素放出を行なった後、水素吸蔵合金粉末を篩分により有
効合金相だけを分離し、その後直接ペースト用溶液を導
入し水素吸蔵合金粉末をペースト化したことによる水素
吸裏電極Bが、寿命性能に優れていることが確認でき
た。The hydrogen storage electrode A and the hydrogen storage electrode A obtained by directly introducing the solution for paste and forming the hydrogen storage alloy powder into a paste after hydrogen storage and hydrogen release with hydrogen gas based on the charge and discharge test results that constituted such a battery were performed. After occluding and desorbing hydrogen with gas, the hydrogen-absorbing alloy powder is separated by sieving to separate only the effective alloy phase, and then the solution for paste is directly introduced to make the hydrogen-absorbing alloy powder into a paste. It was confirmed that the electrode B had excellent life performance.
すなわち、この際水素化と、脱水素化の後に、微粉末化
が不十分な部分だけを、例えば篩分法などにより100ミ
クロン以下の一定の粒径で分離しする工程を有している
ことが好ましい。つまり篩分により選択的に微粉化した
有効合金相だけが利用でき電解液中で溶解しやすい合金
中の不純物相が粗い粒子として分離できる。この両者の
組合せにより、つまり篩分とこの圧力容器に直接ペース
ト用溶液を導入し水素吸蔵合金粉末をペースト化するこ
ととにより活性の高い水素吸蔵合金粉末でも酸素などに
よる被毒を全く受けずにペースト化でき、性能の確保や
製法の合理化とともに安全性が向上することがわかっ
た。That is, at this time, after hydrogenation and dehydrogenation, there is a step of separating only a portion where the fine powdering is insufficient, for example, by a sieving method or the like with a constant particle size of 100 microns or less Is preferred. That is, only the effective alloy phase selectively pulverized by sieving can be used, and the impurity phase in the alloy which is easily dissolved in the electrolytic solution can be separated as coarse particles. By the combination of both, that is, by introducing the paste solution directly into the sieve and this pressure vessel to make the hydrogen storage alloy powder into a paste, even a highly active hydrogen storage alloy powder is not poisoned by oxygen at all. It was found that it can be made into a paste, and the safety is improved as the performance is secured and the manufacturing method is rationalized.
なお、先の説明以外に本発明に関して種々の検討を行な
った結果、以下のことが重要であった。As a result of various studies on the present invention other than the above explanation, the following were important.
まず水素ガスの水素化と、脱水素化の工程は実施例では
3回としたが2回以上行なうことが電池性能上好まし
い。用いるペースト用溶液としては、エチレングリコー
ル、エチレングリコール水溶液、カルボキシメチルセル
ロース水溶液、ポリビニルアルコール水溶液などが適当
である。そして篩分により一定の粒径で分離しする工程
の粒径が100ミクロン以下であることが好ましい。First, the steps of hydrogenating and dehydrogenating hydrogen gas were three times in the examples, but it is preferable to perform the steps twice or more in terms of battery performance. As the paste solution to be used, ethylene glycol, ethylene glycol aqueous solution, carboxymethyl cellulose aqueous solution, polyvinyl alcohol aqueous solution, etc. are suitable. The particle size in the step of separating the particles with a constant particle size by sieving is preferably 100 μm or less.
発明の効果 以上のように本発明の製造方法になる水素吸蔵合金を、
たとえばアルカリ蓄電池の水素吸蔵合金負極に使用する
とき、これまで問題であった微粉化や酸化などを解決し
長寿命化を図れる。Effects of the Invention As described above, the hydrogen storage alloy according to the production method of the present invention,
For example, when it is used for a hydrogen storage alloy negative electrode of an alkaline storage battery, it is possible to solve problems such as pulverization and oxidation, which have been problems so far, and prolong the service life.
図は本発明の一実施例の水素吸蔵電極の製造法を用いた
水素吸蔵電極の製造装置の断面図である。 1……水素吸蔵合金、2……圧力容器、3……粗い金属
メッシュ、4……ガスバルブ、5……溶液バルブ、6…
…ペーストバルブ、7……メッシュ篩、8……ノズル。FIG. 1 is a cross-sectional view of a hydrogen storage electrode manufacturing apparatus using the hydrogen storage electrode manufacturing method of one embodiment of the present invention. 1 ... Hydrogen storage alloy, 2 ... Pressure vessel, 3 ... Coarse metal mesh, 4 ... Gas valve, 5 ... Solution valve, 6 ...
... paste valve, 7 ... mesh sieve, 8 ... nozzle.
Claims (5)
スでの水素化と、脱水素化を行ない微粉末とし、その後
この圧力容器に直接ペースト用溶液を導入し水素吸蔵合
金粉末をペースト化し、得られたペーストを多孔性導電
体に充填することを特徴とする水素吸蔵電極の製造法。1. A hydrogen storage alloy is housed in a pressure vessel, hydrogenated with hydrogen gas and dehydrogenated to obtain fine powder, and then a paste solution is directly introduced into this pressure vessel to paste the hydrogen storage alloy powder. A method for producing a hydrogen storage electrode, characterized in that the obtained paste is filled in a porous conductor.
スでの水素化と、脱水素化を行ない、前記水素化と脱水
素化により微粉末化が不十分な部分だけを除き、その後
この圧力容器に直接ペースト用溶液を導入し水素吸蔵合
金粉末をペースト化することを特徴とする特許請求の範
囲第1項記載の水素吸蔵電極の製造法。2. A hydrogen storage alloy is housed in a pressure vessel, hydrogenated with hydrogen gas, and dehydrogenated, and the fine powder is insufficiently removed by the hydrogenation and dehydrogenation. The method for producing a hydrogen storage electrode according to claim 1, wherein the hydrogen storage alloy powder is made into a paste by directly introducing the paste solution into the pressure vessel.
2回以上行うことを特徴とする特許請求の範囲第1項ま
たは第2項記載の水素吸蔵電極の製造法。3. The method for producing a hydrogen storage electrode according to claim 1 or 2, wherein the steps of hydrogenation with hydrogen gas and dehydrogenation are performed twice or more.
エチレングリコール水溶液、カルボキシメチルセルロー
ス水溶液、ポリビニルアルコール水溶液の中の少なくと
も1種を含むことを特徴とする特許請求の範囲第1項ま
たは第2項記載の水素吸蔵電極の製造法。4. A paste solution containing ethylene glycol,
The method for producing a hydrogen storage electrode according to claim 1 or 2, further comprising at least one selected from an ethylene glycol aqueous solution, a carboxymethyl cellulose aqueous solution, and a polyvinyl alcohol aqueous solution.
な部分だけを除く工程が篩分法により一定の粒径で分離
し、用いる粉末の粒径は100ミクロン以下であることを
特徴とする特許請求の範囲第2項記載の水素吸蔵電極の
製造法。5. The step of removing only the part in which the fine powder is insufficient by hydrogenation and dehydrogenation is separated by a sieving method with a constant particle size, and the particle size of the powder used is 100 μm or less. The method for producing a hydrogen storage electrode according to claim 2, which is characterized in that.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62098939A JPH07101607B2 (en) | 1987-04-22 | 1987-04-22 | Manufacturing method of hydrogen storage electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62098939A JPH07101607B2 (en) | 1987-04-22 | 1987-04-22 | Manufacturing method of hydrogen storage electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63264868A JPS63264868A (en) | 1988-11-01 |
| JPH07101607B2 true JPH07101607B2 (en) | 1995-11-01 |
Family
ID=14233088
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62098939A Expired - Fee Related JPH07101607B2 (en) | 1987-04-22 | 1987-04-22 | Manufacturing method of hydrogen storage electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07101607B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2486175A (en) | 2010-12-02 | 2012-06-13 | Univ Birmingham | Separating rare earth magnetic materials from electronic devices |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63162830A (en) * | 1986-12-25 | 1988-07-06 | Hitachi Metals Ltd | Structure of hydrogen storage alloy and its production |
-
1987
- 1987-04-22 JP JP62098939A patent/JPH07101607B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63264868A (en) | 1988-11-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3825548B2 (en) | Nickel metal hydride secondary battery | |
| JPS6119063A (en) | Hydrogen occlusion electrode | |
| JPH07101607B2 (en) | Manufacturing method of hydrogen storage electrode | |
| JPH11162468A (en) | Alkaline secondary battery | |
| JP2944152B2 (en) | Method for manufacturing nickel-hydrogen storage battery | |
| JP2001118597A (en) | Alkaline secondary cell | |
| JP3567021B2 (en) | Alkaline secondary battery | |
| JPH0812777B2 (en) | Manufacturing method of hydrogen storage electrode | |
| JPS6215769A (en) | Nickel-hydrogen alkaline storage battery | |
| JP2823301B2 (en) | Hydrogen storage alloy electrode | |
| JPH05101821A (en) | Manufacture of hydrogen storage alloy electrode | |
| JP2629807B2 (en) | Hydrogen storage alloy electrode and its manufacturing method | |
| JP2642144B2 (en) | Method for producing hydrogen storage electrode | |
| JPH08138658A (en) | Hydrogen storage alloy-based electrode | |
| JP2857148B2 (en) | Construction method of sealed nickel-hydrogen storage battery | |
| JP2000021398A (en) | Alkaline secondary battery | |
| JP3464717B2 (en) | Manufacturing method of metal oxide / hydrogen secondary battery | |
| JP2733230B2 (en) | Sealed nickel-hydrogen storage battery using hydrogen storage alloy | |
| JP2000090921A (en) | Alkaline secondary battery | |
| JP2558624B2 (en) | Nickel-hydrogen alkaline storage battery | |
| JP2586752B2 (en) | Hydrogen storage alloy electrode | |
| JP3742149B2 (en) | Alkaline secondary battery | |
| JPH11111280A (en) | Hydride rechargeable battery | |
| JP2568967B2 (en) | Manufacturing method of sealed nickel-hydrogen secondary battery | |
| JPH09289036A (en) | Manufacturing method of alkaline storage battery |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |