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JP3290895B2 - Hydrogen storage alloy powder for nickel-metal hydride batteries - Google Patents
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JP3290895B2 - Hydrogen storage alloy powder for nickel-metal hydride batteries - Google Patents

Hydrogen storage alloy powder for nickel-metal hydride batteries

Info

Publication number
JP3290895B2
JP3290895B2 JP21077596A JP21077596A JP3290895B2 JP 3290895 B2 JP3290895 B2 JP 3290895B2 JP 21077596 A JP21077596 A JP 21077596A JP 21077596 A JP21077596 A JP 21077596A JP 3290895 B2 JP3290895 B2 JP 3290895B2
Authority
JP
Japan
Prior art keywords
powder
nickel
gas
hydrogen storage
sieve
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
Application number
JP21077596A
Other languages
Japanese (ja)
Other versions
JPH1053801A (en
Inventor
勝 柳本
大助 木村
俊一郎 西川
忠之 圓尾
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.)
Sanyo Special Steel Co Ltd
Original Assignee
Sanyo Special Steel 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 Sanyo Special Steel Co Ltd filed Critical Sanyo Special Steel Co Ltd
Priority to JP21077596A priority Critical patent/JP3290895B2/en
Publication of JPH1053801A publication Critical patent/JPH1053801A/en
Application granted granted Critical
Publication of JP3290895B2 publication Critical patent/JP3290895B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水素吸蔵合金粉
末、特にニッケル水素電池用の負極材料用のAB5型水
素吸蔵合金粉末に関するものである。
The present invention relates to a hydrogen absorbing alloy powder, and in particular to AB 5 -type hydrogen absorbing alloy powder for the negative electrode material for a nickel-hydrogen battery.

【0002】[0002]

【従来の技術】近年、ニッケルカドミウム電池に代わる
二次電池としてニッケル水素電池が注目され、そのため
の水素吸蔵合金粉末が研究されているが、中でもAB5
型水素吸蔵合金粉末は電池用の負極材料として優れた特
性を備えて、利用されている。これは、例えばCe50
%、La25%、Nd15%、残りPrなどからなるミ
ッシュメタルMmと、例えばMn、Al、Co等を含む
ニッケル合金とを混合溶融したもので、例えば、Mm
1.0 Ni(5−x−y−z)Mnx Aly Cozのよう
な型の金属間化合物である。従来はこれを鋳造材の粉砕
や回転ドラムに接触させる急冷凝固薄帯の粉砕、アルゴ
ンなどの不活性ガスアトマイズ等の諸手法によって粉末
化していた。
In recent years, nickel-hydrogen battery is attracting attention as a secondary battery in place of nickel-cadmium battery, a hydrogen absorbing alloy powder therefor have been studied, among others AB 5
Hydrogen storage alloy powders are used with excellent characteristics as negative electrode materials for batteries. This is, for example, Ce50
%, La 25%, Nd 15%, remaining Pr, etc., and a mixture of a misch metal Mm and a nickel alloy containing, for example, Mn, Al, Co, or the like.
Is the type of intermetallic compounds such as 1.0 Ni (5-x-y -z) Mn x Al y Co z. Conventionally, this has been pulverized by various methods such as pulverization of a cast material, pulverization of a rapidly solidified thin ribbon brought into contact with a rotating drum, and atomization of an inert gas such as argon.

【0003】[0003]

【発明が解決しようとする課題】上述の諸粉末化方法の
うち、鋳造材を粉砕する方法は材料の偏析などにより各
粉末粒子の組成が均一にならず、二次電池に用いた場合
の性能はガスアトマイズ法や急冷凝固薄帯の粉砕などで
得た粉末に劣る。そして、ガスアトマイズ法によって得
た粉末は粒子の形状が球状であるために、鋳造材や急冷
薄帯を粉砕して得た粉末に比べて電池電極に組み入れた
場合の充填密度が優れ、同じ水素吸蔵特性を持つ粉末を
電極に使用した場合でも、電極のエネルギー密度を高く
することができ、容量の大きい電池の製造が可能である
と共に、急冷薄帯法よりも大量生産に適しており、コス
ト的にも有利に製造できる利点がある。
Among the various powdering methods described above, the method of pulverizing a cast material does not have a uniform composition of each powder particle due to segregation of the material and the like, and the performance when used in a secondary battery is reduced. Is inferior to powders obtained by gas atomization or crushing of rapidly solidified ribbons. Since the powder obtained by the gas atomization method has a spherical particle shape, the packing density when incorporated into a battery electrode is superior to that obtained by pulverizing a cast material or a quenched ribbon, and has the same hydrogen storage capacity. Even when a powder having characteristics is used for the electrode, the energy density of the electrode can be increased, a battery with a large capacity can be manufactured, and it is more suitable for mass production than the quenched ribbon method. Also has the advantage that it can be advantageously manufactured.

【0004】しかし、粒子が球状であることは同時に、
電池電極中に充填した際の電気的接触を保つことに技術
的課題があり、接触が不完全な場合は充填密度が高く、
偏析がなく安定した特性を発揮できるというアトマイズ
粉末のメリットが充分に発揮できないという問題点があ
った。この課題の解決法として、アトマイズ粉末と鋳造
粉砕法で得られた粉末とを混合して、充填密度が高いと
いうアトマイズ粉末のメリットと電気的接触が安定して
いるという鋳造粉砕粉末のメリットを両立させることが
考えられる。しかし、このように製造方法が異なる粉末
を混合した場合、偏析が大きく特性的に安定しないとい
う鋳造粉砕粉のデメリットが残るため、経済的で効果的
な解決方法が望まれていた。
[0004] However, the fact that the particles are spherical
There is a technical problem in maintaining electrical contact when filling into the battery electrode, if the contact is incomplete, the packing density is high,
There is a problem that the merit of the atomized powder, which can exhibit stable characteristics without segregation, cannot be sufficiently exhibited. A solution to this problem is to mix the atomized powder with the powder obtained by the casting and pulverizing method to combine the advantages of the atomized powder with a high packing density and the advantages of the cast and pulverized powder with stable electrical contact. It is possible to make it. However, when powders having different production methods are mixed as described above, the disadvantage of cast ground powder that segregation is large and characteristics are not stable remains, and an economical and effective solution has been desired.

【0005】[0005]

【課題を解決するための手段】上述したような問題を解
消すべく、発明者らは鋭意開発を進めた結果、水素吸蔵
アトマイズ合金粉末を所望の粒度で分級し、分級でふる
いに残った粗い粒度の粉末を粉砕してふるいを通った細
かい粒度の粉末と混合して、アトマイズ粉末の安定した
特性を維持しながら、球状粉末特有の問題である電極内
の電気的接触を改善すると共に、経済的なメリットを併
せて得る水素吸蔵合金粉末を提供することを見い出し
た。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have intensively developed and as a result, the hydrogen storage atomized alloy powder is classified with a desired particle size, and the coarse particles remaining on the sieve after the classification are obtained. The powder of the particle size is pulverized and mixed with the powder of the fine particle size passed through a sieve to improve the electrical contact in the electrode, which is a problem peculiar to the spherical powder, while maintaining the stable characteristics of the atomized powder, and to reduce the cost. It has been found that a hydrogen storage alloy powder can be provided which can also obtain a special merit.

【0006】その発明の要旨とするところは、 (1)ニッケル水素電池用水素吸蔵合金粉末において、
ガスアトマイズ粉末を50〜300μで分級し、分級粒
度よりも粗い粉末を粉砕して分級粒度以下の粉末にした
ガスアトマイズ粉砕粉末と分級粒度以下のガスアトマイ
ズ粉末とが混合されていることを特徴とするニッケル水
素電池用水素吸蔵合金粉末。 (2)ガスアトマイズ粉砕粉末及びガスアトマイズ粉末
は熱処理されていることを特徴とする前記(1)記載の
ニッケル水素電池用水素吸蔵合金粉末。 (3)ガスアトマイズ粉砕粉末及びガスアトマイズ粉末
は熱処理された後、酸やアルカリの溶液で表面処理され
ていることを特徴とする前記(1)記載のニッケル水素
電池用水素吸蔵合金粉末にある。
The gist of the invention is as follows: (1) In a hydrogen storage alloy powder for a nickel-metal hydride battery,
Nickel-metal hydride, characterized in that gas atomized powder is classified at 50 to 300 μm, and a gas atomized powder obtained by pulverizing a powder coarser than the classification particle size into a powder having a classification particle size or less and a gas atomizing powder having a classification particle size or less are mixed. Hydrogen storage alloy powder for batteries. (2) The hydrogen storage alloy powder for a nickel-metal hydride battery according to the above (1), wherein the gas atomized pulverized powder and the gas atomized powder are heat-treated. (3) The hydrogen storage alloy powder for a nickel-metal hydride battery according to the above (1), wherein the powdered gas atomized powder and the gas atomized powder are heat-treated and then surface-treated with an acid or alkali solution.

【0007】以下、本発明について詳細に説明する。通
常、ふるい分けする粒度は電池の電極設計によって異な
るが、通常の電池の正極と負極の極板ギャップが最大3
00μ程度であることからして、粉砕せずに使用できる
アトマイズ粉末の最大直径は300μであり、また経済
的な観点からは粉砕する粉末をできるだけ少なくする方
が有利であることや微粉末を多くしすぎると充填密度が
減少する傾向があるため、ふるい分けする際の最小ふる
い分け直径は50μ程度が適当である。
Hereinafter, the present invention will be described in detail. Usually, the particle size to be sieved varies depending on the electrode design of the battery.
Since it is about 00μ, the maximum diameter of the atomized powder that can be used without pulverization is 300μ. From the economical viewpoint, it is advantageous to reduce the powder to be pulverized as much as possible. If the sieving is too large, the packing density tends to decrease. Therefore, it is appropriate that the minimum sieving diameter in sieving is about 50 μm.

【0008】[0008]

【発明の実施の形態】ふるいを通った細かい粉末は前述
の通り、球状で充填密度が高く、偏析が少なく特性が安
定しているというガスアトマイズのメリットをそのまま
発揮する粉末である。またふるい残った粗い粉末を粉砕
した粉末は、鋳造粉砕粉末と同様に不規則形状になり、
球状粉末と混合することによって球状粉末の電気的接触
を効果的に改善するという役割を果たす。ここで、粉砕
した粉末も元は急冷法であるガスアトマイズで製造され
た粉末であるため、偏析が少なく安定した特性を発揮す
るというメリットはそのまま発揮され、鋳造粉砕粉末と
アトマイズ粉末とを混合したときのような不安定要因は
みられない。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As described above, a fine powder that has passed through a sieve is a powder that exhibits the advantages of gas atomization, that is, a spherical shape, a high packing density, low segregation, and stable characteristics. In addition, the powder obtained by grinding the coarse powder remaining in the sieve becomes irregularly shaped like the cast ground powder,
By mixing with the spherical powder, it plays a role of effectively improving the electrical contact of the spherical powder. Here, since the ground powder is originally a powder manufactured by gas atomization which is a quenching method, the advantage of exhibiting stable characteristics with less segregation is exhibited as it is, and when the cast ground powder and the atomized powder are mixed. There are no such instability factors.

【0009】さらにふるい残ったアトマイズ粉末の粗粉
末を粉砕して使用するため、従来のアトマイズ粉末を使
用して電極を作る工程では使用できずにリターンとして
再溶解に使用したり廃却処分にしていた粗粉末も同時に
使用できるようになり、経済的に大きな効果がある。こ
のように、アトマイズされた粉末をふるい分け後、粗粉
末を粉砕してふるいを通った粉末と混合することによ
り、高い充填密度と安定した電気的接触を両立させるこ
とができると共に、コスト的に有利なガスアトマイズ粉
末のメリットをさらに優位にすることが可能になった。
Further, since the remaining coarse powder of the atomized powder is crushed and used, it cannot be used in the process of making an electrode using the conventional atomized powder, and is used as a return for re-dissolution or disposal. Coarse powder can be used at the same time, which has a great economic effect. As described above, after sieving the atomized powder, the coarse powder is crushed and mixed with the powder that has passed through the sieving, so that a high packing density and stable electrical contact can be achieved at the same time, and it is cost-effective. It has become possible to further enhance the advantages of the gas atomized powder.

【0010】[0010]

【実施例】【Example】

(実施例1)Mm1.0 Ni3.4 Co0.8 Mn0.6 Al
0.2 を構成するように配合した金属原料をアルミナ坩堝
に収容し、誘導溶解炉で溶解し、1500℃の溶湯を直
径3mmのアルミナノズルを通して落下させ、これにア
ルゴンガスを吹き付けることによってガスアトマイズ粉
末を製造した。この粉末を目開き150μのふるいで分
級し、ふるいを通った微粉末とふるいに残った粗粉末と
に分けた。ふるいに残った粉末とふるいを通った粉末と
の重量比は25対75であった。ふるいに残った粗粉末
は粉末と同重量の直径10mmのメノウ製ボール及び粉
末容積の5倍の純水と共にメノウ製のポットに収容し、
遊星型ボールミルで30分間粉砕処理を施した。粉砕後
の粉末は全て目開き150μのふるいを通過し、良好に
粉砕されていた。粉砕した粉末と先にふるった微粉末と
をV型混合機に投入して混合した。
(Example 1) Mm 1.0 Ni 3.4 Co 0.8 Mn 0.6 Al
A metal raw material blended to form 0.2 is placed in an alumina crucible, melted in an induction melting furnace, a 1500 ° C molten metal is dropped through an alumina nozzle having a diameter of 3 mm, and a gas atomized powder is produced by blowing argon gas onto the molten metal. did. This powder was classified with a sieve having an opening of 150 μm, and divided into a fine powder passed through the sieve and a coarse powder remaining in the sieve. The weight ratio of the powder remaining in the sieve to the powder passed through the sieve was 25:75. The coarse powder remaining in the sieve is stored in an agate pot together with a powder of agate having the same weight as the powder and having a diameter of 10 mm and pure water having a volume five times the powder volume.
Grinding treatment was performed for 30 minutes with a planetary ball mill. All of the pulverized powders passed through a sieve with a mesh size of 150 μm and were pulverized well. The pulverized powder and the previously sieved fine powder were put into a V-type mixer and mixed.

【0011】表1に示す本発明に係る混合粉末Aを50
0g取り、タップ充填機にセットして100回タッピン
グした後の容積を測定して充填密度を測定した。比較の
ために目開き150μを通ったガスアトマイズ微粉末
(粉砕なし)Bとふるいに残ったガスアトマイズ粉末を
粉砕して目開き150μのふるいを通過した粉末C、さ
らに小型の誘導溶解炉で溶解・鋳造した後遊星型ボール
ミルで微粉砕した目開き150μを通る鋳造粉砕粉末D
についても充填密度を測定した。さらに、これらの粉末
の電気化学特性を測定するために混合粉末1gに加えて
導電剤として粒径3μのNi粉末(0.5及び2g)、
結着剤としてPTFE(ポリテトラフルオロエチレン)
粉末0.2gを混合して直径20mmのダイでプレスし
てコイン状にし、Niメッシュで挟んでNiの導電板を
スポット溶接して負極を作製した。この負極を市販のN
iCd電池から取り出したNiOOH/NiOH正極
(容量1400mAh)と共にテフロン製のセル内に装
着し、6規定のKOH溶液中に浸漬させて5気圧のアル
ゴンガスで封入したテスト電池の放電容量を測定した。
The mixed powder A according to the present invention shown in Table 1 was mixed with 50
The packing density was measured by measuring 0 g, setting the volume in a tap filling machine, and tapping 100 times. For comparison, a fine gas atomized powder (no pulverization) B passed through a 150 μm aperture, a powder C that was pulverized from a gas atomized powder remaining in a sieve and passed through a 150 μm aperture, and melted and cast in a small induction melting furnace And then finely pulverized with a planetary ball mill, and then cast and pulverized powder D passing through an opening of 150 μm.
Was also measured for packing density. Further, in order to measure the electrochemical properties of these powders, Ni powder (0.5 and 2 g) having a particle size of 3 μm as a conductive agent was added to 1 g of the mixed powder,
PTFE (polytetrafluoroethylene) as binder
0.2 g of the powder was mixed, pressed with a die having a diameter of 20 mm into a coin shape, and sandwiched between Ni meshes, and a Ni conductive plate was spot-welded to produce a negative electrode. This negative electrode is commercially available N
The battery was mounted in a Teflon cell together with a NiOOH / NiOH positive electrode (capacity: 1400 mAh) taken out of the iCd battery, immersed in a 6N KOH solution, and sealed with 5 atm of argon gas to measure the discharge capacity of the test battery.

【0012】[0012]

【表1】 [Table 1]

【0013】(実施例2)実施例1と同様にして製作し
たアルゴンガスアトマイズ水素吸蔵合金粉末を目開き2
00μのふるいで分級し、ふるいを通った微粉末とふる
いに残った粗粉末とに分けた。ふるいに残った粉末とふ
るいを通った粉末との重量比は20対80であった。そ
れぞれの粉末について軟鋼性の容器に収納し、700℃
のアルゴンガス雰囲気中で5時間熱処理を行った後、粗
粉末については実施例1と同様の条件で粉砕して目開き
200μを通る粉砕粉末を作製した。粉砕した粉末と先
にふるった微粉末とをV型混合機に投入して混合した。
表2に示す本発明に係る混合粉末A及び比較材として上
記と同様の熱処理を施した目開き200μを通ったガス
アトマイズ微粉末(粉砕なし)B、ふるいに残ったガス
アトマイズ粉末を粉砕して目開き200μのふるいを通
過した粉末C、さらに小型の誘導溶解炉で溶解・鋳造し
た後遊星型ボールミルで微粉砕した目開き200μを通
る鋳造粉砕粉末Dについて実施例1と同じ条件でテスト
電池を作製し、放電容量を測定した。
Example 2 An argon gas atomized hydrogen storage alloy powder produced in the same manner as in Example 1 was
The mixture was classified with a 00μ sieve and divided into a fine powder passed through the sieve and a coarse powder remaining in the sieve. The weight ratio of the powder remaining in the sieve to the powder passed through the sieve was 20:80. Store each powder in a mild steel container at 700 ° C
After the heat treatment was performed in an argon gas atmosphere for 5 hours, the coarse powder was pulverized under the same conditions as in Example 1 to prepare a pulverized powder passing through a mesh of 200 μm. The pulverized powder and the previously sieved fine powder were put into a V-type mixer and mixed.
The mixed powder A according to the present invention shown in Table 2 and a gas atomized fine powder (no pulverization) B having passed through a mesh 200 μm subjected to the same heat treatment as above as a comparative material and a gas atomized powder remaining in the sieve were pulverized and pulverized. A test battery was prepared under the same conditions as in Example 1 for powder C that passed through a 200 μ sieve, and cast and ground powder D that passed through an opening of 200 μ that was melted and cast in a small induction melting furnace and then finely ground with a planetary ball mill. And the discharge capacity was measured.

【0014】[0014]

【表2】 [Table 2]

【0015】(実施例3)実施例1と同様にして製作し
たアルゴンガスアトマイズ水素吸蔵合金粉末を目開き1
00μのふるいで分級し、ふるいを通った微粉末とふる
いに残った粗粉末とに分けた。ふるいに残った粉末とふ
るいを通った粉末との重量比は30対70であった。そ
れぞれの粉末について軟鋼性の容器に収納し、700℃
のアルゴンガス雰囲気中で5時間熱処理を行った後、粗
粉末については実施例1と同様の条件で粉砕して目開き
100μを通る粉砕粉末を作製した。粉砕した粉末と先
にふるった微粉末とをV型混合機に投入して混合した。
さらにこの混合粉末とpH=1.0に調整した粉末の容
量の5倍の塩酸溶液と共にビーカーに入れてpH=6.
5になるまで攪拌しながら表面処理を行った。この表面
処理後の表3に示す本発明に係る混合粉末A及び上記と
同様の熱処理、表面処理を施した目開き100μを通っ
たガスアトマイズ微粉末(粉砕なし)B、ふるいに残っ
たガスアトマイズ粉末を粉砕して目開き100μのふる
いを通過した粉末C、さらに小型の誘導溶解炉で溶解・
鋳造した後遊星型ボールミルで微粉砕した目開き100
μを通る鋳造粉砕粉末Dについて実施例1と同じ条件で
テスト電池を作製し、放電容量を測定した。
Example 3 An argon gas atomized hydrogen storage alloy powder produced in the same manner as in Example 1 was
The mixture was classified with a 00μ sieve and divided into a fine powder passed through the sieve and a coarse powder remaining in the sieve. The weight ratio of the powder remaining in the sieve to the powder passed through the sieve was 30:70. Store each powder in a mild steel container at 700 ° C
After performing a heat treatment in an argon gas atmosphere for 5 hours, the coarse powder was pulverized under the same conditions as in Example 1 to prepare a pulverized powder passing through a mesh of 100 μm. The pulverized powder and the previously sieved fine powder were put into a V-type mixer and mixed.
Further, the mixed powder and a hydrochloric acid solution 5 times the volume of the powder adjusted to pH = 1.0 were put into a beaker together with pH = 6.
The surface treatment was performed while stirring until the mixture reached 5. The mixed powder A according to the present invention shown in Table 3 after the surface treatment, the heat-treated as described above, the finely divided gas atomized powder (no pulverization) B having passed through an opening of 100 μm, and the gas atomized powder remaining on the sieve were subjected to the same surface treatment. Powder C, which has been crushed and passed through a sieve with an opening of 100μ, is further melted in a small induction melting furnace.
Aperture 100 finely pulverized with a planetary ball mill after casting
A test battery was manufactured under the same conditions as in Example 1 for the cast and ground powder D passing through μ, and the discharge capacity was measured.

【0016】[0016]

【表3】 [Table 3]

【0017】実施例1において、本発明粉末Aの充填密
度は球状であるガスアトマイズ微粉末Bと同等の高い充
填密度であり、ガスアトマイズ粉末を粉砕したものCや
鋳造粉砕粉末Dに比べて15%以上高い密度を示した。
さらに実施例1から3のいずれの場合においても本発明
粉末は導電剤であるNi粉末の混合量を減少させた電極
においても、Ni粉末を多量に加えた場合と同等の極め
て良好な放電容量を示し、その放電容量は球状ガスアト
マイズ微粉末にNi粉末を多量に加えた場合と同等であ
る。
In Example 1, the packing density of the powder A of the present invention is as high as that of the gas atomized fine powder B having a spherical shape, and is at least 15% higher than that of the gas atomized powder C or the cast and ground powder D. It showed a high density.
Further, in any of the cases of Examples 1 to 3, the powder of the present invention has an extremely good discharge capacity equivalent to that when a large amount of Ni powder is added even in an electrode in which the amount of Ni powder as a conductive agent is reduced. The discharge capacity is equivalent to the case where a large amount of Ni powder is added to the spherical gas atomized fine powder.

【0018】一方、比較材であるガスアトマイズ微粉末
Bは導電剤であるNi粉末が多い場合は良好な放電容量
を示すが、Ni粉末を減らした場合は電気的接触が減少
し、放電容量も減少する。ガスアトマイズ粉末を粉砕し
たものCや鋳造粉砕粉末DはNi粉末を減少させても電
気的接触が良好なため放電容量はNi粉末が多い場合と
同等の放電容量を示すが、鋳造粉砕粉末はガスアトマイ
ズ粉末に比べて組織的な不均一性があり、ガスアトマイ
ズ粉末に比べて低い値である。 以上の結果の通り、本
発明によって、球状ガスアトマイズ粉末と同等の極めて
高い充填密度を維持しながら、さらに球状粉末の課題で
あった電気的接触が不利な状況下における放電容量を改
善できた。
On the other hand, the gas atomized fine powder B as the comparative material shows a good discharge capacity when the amount of the Ni powder as the conductive agent is large, but when the amount of the Ni powder is reduced, the electric contact decreases and the discharge capacity also decreases. I do. Although the gas atomized powder C and the cast and ground powder D have good electrical contact even when the amount of Ni powder is reduced, the discharge capacity shows the same discharge capacity as the case where the amount of Ni powder is large, but the cast and ground powder is gas atomized powder. There is a structural non-uniformity as compared with that of the gas atomized powder, and the value is lower than that of the gas atomized powder. As described above, according to the present invention, it was possible to improve the discharge capacity in a situation where electrical contact, which was a problem of the spherical powder, was disadvantageous while maintaining an extremely high packing density equivalent to that of the spherical gas atomized powder.

【0019】[0019]

【発明の効果】以上述べたように、本発明による混合し
たアトマイズ粉末を用いることにより、極めて安定した
特性が図られると共に、経済的にも極めて有利な製造方
法を提供することにある。
As described above, it is an object of the present invention to provide an extremely economically advantageous production method while using the atomized powder mixed according to the present invention to achieve extremely stable characteristics.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 圓尾 忠之 兵庫県姫路市飾磨区中島字一文字3007番 地 山陽特殊製鋼株式会社内 (58)調査した分野(Int.Cl.7,DB名) B22F 9/08 B22F 1/00 H01M 4/38 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Tadayuki Maruo 3007 one-letter Nakajima character in Shima, Himeji City, Hyogo Prefecture Inside Sanyo Special Steel Co., Ltd. (58) Field surveyed (Int. Cl. 7 , DB name) B22F 9 / 08 B22F 1/00 H01M 4/38

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ニッケル水素電池用水素吸蔵合金粉末に
おいて、ガスアトマイズ粉末を50〜300μで分級
し、分級粒度よりも粗い粉末を粉砕して分級粒度以下の
粉末にしたガスアトマイズ粉砕粉末と分級粒度以下のガ
スアトマイズ粉末とが混合されていることを特徴とする
ニッケル水素電池用水素吸蔵合金粉末。
In a hydrogen storage alloy powder for a nickel-metal hydride battery, a gas atomized powder is classified at 50 to 300 μm, and a powder coarser than the classified particle size is pulverized into a powder having a size smaller than the classified particle size. A hydrogen storage alloy powder for a nickel-metal hydride battery, wherein the powder is mixed with a gas atomized powder.
【請求項2】 ガスアトマイズ粉砕粉末及びガスアトマ
イズ粉末は熱処理されていることを特徴とする請求項第
1項記載のニッケル水素電池用水素吸蔵合金粉末。
2. The hydrogen storage alloy powder for a nickel metal hydride battery according to claim 1, wherein the gas atomized powder and the gas atomized powder are heat-treated.
【請求項3】 ガスアトマイズ粉砕粉末及びガスアトマ
イズ粉末は熱処理された後、酸やアルカリの溶液で表面
処理されていることを特徴とする請求項第1項記載のニ
ッケル水素電池用水素吸蔵合金粉末。
3. The hydrogen-absorbing alloy powder for a nickel-metal hydride battery according to claim 1, wherein the gas-atomized powder and the gas-atomized powder are heat-treated and then surface-treated with an acid or alkali solution.
JP21077596A 1996-08-09 1996-08-09 Hydrogen storage alloy powder for nickel-metal hydride batteries Expired - Fee Related JP3290895B2 (en)

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JP3290895B2 true JP3290895B2 (en) 2002-06-10

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