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JPS6040668B2 - Manufacturing method of hydrogen storage electrode - Google Patents
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JPS6040668B2 - Manufacturing method of hydrogen storage electrode - Google Patents

Manufacturing method of hydrogen storage electrode

Info

Publication number
JPS6040668B2
JPS6040668B2 JP52019652A JP1965277A JPS6040668B2 JP S6040668 B2 JPS6040668 B2 JP S6040668B2 JP 52019652 A JP52019652 A JP 52019652A JP 1965277 A JP1965277 A JP 1965277A JP S6040668 B2 JPS6040668 B2 JP S6040668B2
Authority
JP
Japan
Prior art keywords
hydrogen
alloy
electrode
particles
hydrogen storage
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
Application number
JP52019652A
Other languages
Japanese (ja)
Other versions
JPS53103910A (en
Inventor
伸行 柳原
正一 池山
勉 岩城
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP52019652A priority Critical patent/JPS6040668B2/en
Publication of JPS53103910A publication Critical patent/JPS53103910A/en
Publication of JPS6040668B2 publication Critical patent/JPS6040668B2/en
Expired legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Powder Metallurgy (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Description

【発明の詳細な説明】 本発明は、陰極に貯蔵されている水素と、陽極の例えば
酸素との電気化学的反応により電気ヱネルギを発生する
蓄電池の前記陰極などとして用いられる水素吸蔵電極の
製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for producing a hydrogen storage electrode used as the cathode of a storage battery, which generates electrical energy through an electrochemical reaction between hydrogen stored in the cathode and, for example, oxygen at the anode. Regarding.

従来、この種の水素吸蔵電極は、その活性物質である水
素を吸蔵する合金、例えばTi2Ni合金の粉末を次の
ようにして製造していた。
Conventionally, this type of hydrogen storage electrode has been manufactured using powder of an alloy that stores hydrogen, which is an active substance, such as a Ti2Ni alloy, in the following manner.

まず金属単体、例えばチタンとニッケルを合金組成とす
るように秤量し、これをアーク溶解炉、真空電気炉など
で加熱溶解して合金を作り、次にこの合金を不・活性気
流中で粉砕して粉末とする方法である。しかし、この種
の合金は機械的に細かく粉砕するのが困難であり、かつ
長時間を要するので、電極こ用いる合金粉末の粒度は1
0〜60#程度であった。このような合金粉末を用いて
暁結あるいは結着剤で結合した電極は、充電(水素吸蔵
)と放電(水素放出)を繰り返すと、上記合金粉末は破
嬢されてさらに細かい粒子となっていくため、粒子間の
結合力が弱くなり、電極の膨張、亀裂あるし、は合金粉
末の脱落を生じる。そして充放電サイクルの増加ととも
に上記の現象が一層顕著に現われてくる。このようにな
ると、電極の内部抵抗が著しく増加し、放電容量が低下
することになる。上記の現象は、合金の水素吸蔵、放出
により合金の一次粒子が破壊され、二次粒子へ変化する
ことによるものであるから、あらかじめ合金粉末に水素
の吸蔵、放出を行わせて微細化しておけば、合金の二次
粒子化発生はなくなる。本発明は、この点に着目して、
上記従来の欠点を解決しようとするものである。
First, single metals, such as titanium and nickel, are weighed to form an alloy composition, heated and melted in an arc melting furnace or vacuum electric furnace to create an alloy, and then this alloy is pulverized in an inert air stream. This method is used to make powder. However, this type of alloy is difficult to mechanically grind into fine particles and requires a long time, so the particle size of the alloy powder used in the electrode is 1.
It was about 0-60#. When an electrode made of such an alloy powder is bonded with a binder or bonded with a binder, the alloy powder breaks down and becomes even finer particles when it is repeatedly charged (hydrogen absorption) and discharged (hydrogen release). As a result, the bonding force between particles becomes weaker, causing expansion and cracking of the electrode, and the alloy powder falling off. As the number of charge/discharge cycles increases, the above phenomenon becomes more noticeable. When this happens, the internal resistance of the electrode increases significantly and the discharge capacity decreases. The above phenomenon is due to the primary particles of the alloy being destroyed by the hydrogen absorption and release of the alloy, and changing into secondary particles. Therefore, it is necessary to make the alloy powder finer by allowing it to absorb and release hydrogen in advance. In this case, the occurrence of secondary particles in the alloy is eliminated. The present invention focuses on this point, and
This is an attempt to solve the above-mentioned conventional drawbacks.

すなわち、本発明は、水素を吸蔵する合金粉末に水素の
吸蔵、放出を交互に行わせて微細化した粉末により電極
を構成することを特徴とする水素吸蔵電極の製造法であ
る。本発明の方法によれば合金粉末に対して水素活性化
処理が繰り返されるので、容量の増加を図れる利点もあ
る。以下、本発明をその実施例により説明する。
That is, the present invention is a method for manufacturing a hydrogen storage electrode, which is characterized in that the electrode is made of a fine powder obtained by making a hydrogen storage alloy powder alternately store and release hydrogen. According to the method of the present invention, since the hydrogen activation treatment is repeated on the alloy powder, there is an advantage that the capacity can be increased. Hereinafter, the present invention will be explained with reference to examples thereof.

市販のチタン粉末(純度99.5%2久上)629と市
販のニッケル粉末(純度99.5%以上)滋夕を混合し
、加圧成形した後、アーク溶解炉で溶解してTi2Ni
合金製造する。次にこの合金を不活性気流中で粉砕し、
300メッシュ(46〃)のふるいを通過した粉末を電
気炉の反応容器に入れ、容器内を10‐5Tom.まで
減圧にした後、炉内温度を100qo程度までに上げ、
1疎気圧の水素で容器内を充満させる。こうして合金に
水素を吸蔵させ、飽和に達した後、水冷により容器内温
度を室温程度に下げ、容器内の水素を真空ポンプで吸引
除去し、合金の吸蔵している水素を放出させる。水素を
完全に放出させた後、再度容器内を1ぴ気圧以上の水素
で充満し、100oo程度まで上昇させて水素を吸蔵さ
せる。このような水素の吸蔵、放出操作を5回繰り返し
、最後に脱気する。こうして得た合金微粉末に1の重量
%の弗素樹脂を混合ししニッケル製発泡メタルに充てん
し、加圧の後、アルゴンガス気流中で※素樹脂の融点よ
り少し高い温度300午0で約1時間熱処理する。
Commercially available titanium powder (purity 99.5% 2Kugami) 629 and commercially available nickel powder (purity 99.5% or higher) Shiyu are mixed, pressure molded, and then melted in an arc melting furnace to form Ti2Ni.
Manufacture alloys. This alloy is then ground in an inert air stream,
The powder that passed through a 300 mesh (46〃) sieve was put into a reaction container of an electric furnace, and the inside of the container was heated to 10-5 Tom. After reducing the pressure to
1 Fill the container with hydrogen at an aphobic pressure. In this way, the alloy absorbs hydrogen, and after reaching saturation, the temperature inside the container is lowered to about room temperature by water cooling, and the hydrogen in the container is removed by suction using a vacuum pump, thereby releasing the hydrogen stored in the alloy. After the hydrogen is completely released, the inside of the container is again filled with hydrogen at a pressure of 1 pressure or more, and the pressure is increased to about 100 oo to store hydrogen. Such hydrogen storage and release operations are repeated five times, and finally, deaeration is performed. The fine alloy powder obtained in this way was mixed with 1% by weight of fluororesin, filled into a nickel foam metal, and after pressurized, in an argon gas stream *at a temperature slightly higher than the melting point of the base resin at 300 pm. Heat treat for 1 hour.

上記のようにして得た本発明の電極を負極とし、これよ
り容量の大きい公知の酸化ニッケル電極を正極としてア
ルカリ蓄電池を構成し、充放電試験をした。充放電々流
は負極の合金1夕当たり50mA、充放電速度は0.本
であり、充轟々気量は負極容量の130%相当である。
第1図曲線Aに、この電池の充放電に伴う放電容量の変
化を示す。
An alkaline storage battery was constructed using the electrode of the present invention obtained as described above as a negative electrode and a known nickel oxide electrode having a larger capacity as a positive electrode, and a charge/discharge test was conducted. The charging/discharging current is 50 mA per night for the negative electrode alloy, and the charging/discharging rate is 0. The charging volume is equivalent to 130% of the negative electrode capacity.
Curve A in FIG. 1 shows the change in discharge capacity accompanying charging and discharging of this battery.

放電容量は負極の合金1夕当たりの値で示した。曲線B
は、水素の吸蔵、放出操作を行わない合金粉末を用いて
構成した負極を用いた電池の特性を示す。図から明らか
なように、本発明の電極を用いた電池は、従来の電極を
用いた電池に比べて、寿命が2倍以上に向上している。
従来の電極では、合金粒子の破壊による二次粒子、三次
粒子への微細化が進行していることが電子顕微鏡で観察
され、このような合金粒子の微細化により電極の内部抵
抗が増大して容量低下を生じたものであることが明らか
である。
The discharge capacity was expressed as a value per hour of negative electrode alloy. curve B
shows the characteristics of a battery using a negative electrode constructed using an alloy powder that does not absorb or release hydrogen. As is clear from the figure, the life of the battery using the electrode of the present invention is more than twice as long as that of the battery using the conventional electrode.
In conventional electrodes, it has been observed using an electron microscope that the alloy particles are broken down and refined into secondary and tertiary particles, and this miniaturization of alloy particles increases the internal resistance of the electrode. It is clear that this caused a decrease in capacity.

一方本発明の電極は数回の水素活性化処理によりあらか
じめ微細化された合金粒子で構成されているので、充放
電による合金粒子の二次、三次粒子への破壊も少なく、
結着剤の弗素樹脂粒子(約0.5仏程度)と数山〜20
仏の初期の合金粒子とが強く結合していることが確認さ
れた。次に合金としてTi2Ni合金を用いた場合の初
回水素活性化処理の条件について説明する。
On the other hand, since the electrode of the present invention is composed of alloy particles that have been refined in advance through several hydrogen activation treatments, the alloy particles are less likely to be destroyed into secondary and tertiary particles by charging and discharging.
Binder fluororesin particles (approximately 0.5 degrees) and several to 20 particles
It was confirmed that the particles were strongly bonded to the initial alloy particles of France. Next, conditions for the initial hydrogen activation treatment when a Ti2Ni alloy is used as the alloy will be explained.

まず水素吸蔵の場合は、温度は室温〜10000が好ま
しい。すなわち、室温以下の温度では水素の吸蔵反応が
容易に進行せず長時間を要する。又100q0以上にな
ると、初期は水素化が進むが1ぴ気圧程度以上の高圧を
必要とし、設備の点でも不利である。最初の水素活性化
は比較的高い温度と圧力(1の気圧程度以上)で行った
方が効果的であるが、2〜3回目以後は温度がそれより
低くなっても水素化は容易に進行する。脱気工程は、1
0‐ITon.以下に減圧しないと十分な脱ガスは起ら
ない。
First, in the case of hydrogen storage, the temperature is preferably room temperature to 10,000 ℃. That is, at temperatures below room temperature, the hydrogen storage reaction does not proceed easily and requires a long time. Further, when the pressure exceeds 100q0, hydrogenation progresses initially, but a high pressure of about 1 pi atmosphere or more is required, which is disadvantageous in terms of equipment. It is more effective to perform the first hydrogen activation at a relatively high temperature and pressure (about 1 atm or higher), but after the second or third time, hydrogenation proceeds easily even if the temperature is lower than that. do. The degassing process is 1
0-ITon. Sufficient degassing will not occur unless the pressure is reduced to below.

脱ガスが不十分な状態で水素の吸蔵、放出を行っても合
金の微細化の効率が悪く、比較的大きな粒子が残存し、
電極に構成した後にその粒子が微細化し、電極の崩壊に
つながる。従って、水素の吸蔵、放出操作をして得られ
る合金の平均粒径は0.1〜20仏が良好である。0.
1は以下の微細粒子が主要素になると、非常に酸化され
易くなり、取扱いも困難となる。
Even if hydrogen is absorbed and released in a state where degassing is insufficient, the efficiency of refining the alloy is poor, and relatively large particles remain.
After being formed into an electrode, the particles become microscopic, leading to the collapse of the electrode. Therefore, the average grain size of the alloy obtained by hydrogen storage and release operations is preferably 0.1 to 20 mm. 0.
When the following fine particles become the main elements, No. 1 becomes very easily oxidized and becomes difficult to handle.

又20仏より大きい粒子が主要素になると、電極に構成
してから二次粒子、三次粒子への破壊を生じる。第2図
は、前記実施例に示した条件で水素の吸蔵、放出処理を
行わせた場合の処理回数と、処理後の粉末から構成した
電極を用いた前記と同様の電池の寿命との関係を示す。
なお寿命は放電容量が0.1虫h′夕となるまでの充放
電サイクル数で表した。図から明らかなように、5回程
度までは処理回数の増加とともに寿命は伸びるが、それ
以上処理をかさねても効果はない。このような水素化処
理は単に合金粉末を微粒子とするだけでなく、水素の吸
蔵、放出を容易にし、特性の向上に役立つ効果を有する
Furthermore, if particles larger than 20 mm become the main element, they will break down into secondary particles and tertiary particles after being formed into an electrode. Figure 2 shows the relationship between the number of hydrogen storage and desorption treatments performed under the conditions shown in the example above and the life of a battery similar to the one described above using an electrode made of the treated powder. shows.
The lifespan was expressed as the number of charge/discharge cycles until the discharge capacity reached 0.1 hours. As is clear from the figure, the life span increases as the number of treatments increases up to about 5 times, but there is no effect even if the treatments are repeated beyond that point. Such hydrogenation treatment not only turns the alloy powder into fine particles, but also facilitates the absorption and release of hydrogen, which has the effect of improving properties.

これは合金粒子表面でのガス状水素のイオン化及びその
逆の反応を容易にする一種の電気化学的触媒作用の効果
をもたらすことによるものと思われる。以上のように本
発明によればサイクル寿命のすぐれた水素吸蔵電極を得
ることができる。なお上記の実施例では、合金粉末を結
着剤により結合した電極について説明したが、電極支持
体、例えば発泡メタル、パンチングメチルとともに合金
の融点以下の温度で焼結して構成する電極にも同様に適
用することができる。
This is believed to be due to the effect of a kind of electrochemical catalysis that facilitates the ionization of gaseous hydrogen on the surface of the alloy particles and vice versa. As described above, according to the present invention, a hydrogen storage electrode with excellent cycle life can be obtained. In the above example, an electrode was explained in which alloy powder was bonded with a binder, but the same applies to an electrode constructed by sintering the alloy powder together with an electrode support, such as foamed metal or punched methyl, at a temperature below the melting point of the alloy. It can be applied to

又本発明による電極は、燃料電池の水素電極にも用いる
ことができる。
The electrode according to the invention can also be used as a hydrogen electrode for fuel cells.

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

第1図は本発明の電極と酸化ニッケル電極を総合せたア
ルカリ電池及び従来の電極を用いた電池の充放電に伴う
放電容量の変化を比較した図、第2図は本発明による水
素の吸蔵、放出処理回数と充放電サイクル寿命との関係
を示す。 第1図 第2図
Figure 1 is a diagram comparing the changes in discharge capacity during charging and discharging of an alkaline battery that combines the electrode of the present invention and a nickel oxide electrode, and a battery that uses a conventional electrode. Figure 2 shows the hydrogen occlusion according to the present invention. , shows the relationship between the number of discharge treatments and the charge/discharge cycle life. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1 水素を吸蔵する合金粉末に水素を吸蔵させる工程と
脱気させる工程とを交互に行わせて微粉化した粉末を用
いることを特徴とする水素吸蔵電極の製造法。
1. A method for manufacturing a hydrogen storage electrode, which uses a powder obtained by alternately performing a process of storing hydrogen and a process of degassing hydrogen in an alloy powder that stores hydrogen.
JP52019652A 1977-02-23 1977-02-23 Manufacturing method of hydrogen storage electrode Expired JPS6040668B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52019652A JPS6040668B2 (en) 1977-02-23 1977-02-23 Manufacturing method of hydrogen storage electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52019652A JPS6040668B2 (en) 1977-02-23 1977-02-23 Manufacturing method of hydrogen storage electrode

Publications (2)

Publication Number Publication Date
JPS53103910A JPS53103910A (en) 1978-09-09
JPS6040668B2 true JPS6040668B2 (en) 1985-09-12

Family

ID=12005170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52019652A Expired JPS6040668B2 (en) 1977-02-23 1977-02-23 Manufacturing method of hydrogen storage electrode

Country Status (1)

Country Link
JP (1) JPS6040668B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59181459A (en) * 1983-03-31 1984-10-15 Toshiba Corp Metal oxide hydrogen battery
JPS60119079A (en) * 1983-11-30 1985-06-26 Matsushita Electric Ind Co Ltd Hydrogen storage electrode
US4551400A (en) * 1984-04-18 1985-11-05 Energy Conversion Devices, Inc. Hydrogen storage materials and methods of sizing and preparing the same for electrochemical applications
JPS6149375A (en) * 1984-08-17 1986-03-11 Matsushita Electric Ind Co Ltd Manufacturing method of hydrogen storage electrode
JPS62238304A (en) * 1986-04-09 1987-10-19 Mitsui Mining & Smelting Co Ltd Production of magnet powder containing rare earth element
JPH0812777B2 (en) * 1987-04-22 1996-02-07 松下電器産業株式会社 Manufacturing method of hydrogen storage electrode
JP2001313052A (en) * 2000-04-28 2001-11-09 Japan Metals & Chem Co Ltd Initial activation method of hydrogen storage alloy

Also Published As

Publication number Publication date
JPS53103910A (en) 1978-09-09

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