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JP3462682B2 - Method for producing hydrogen storage alloy powder - Google Patents
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JP3462682B2 - Method for producing hydrogen storage alloy powder - Google Patents

Method for producing hydrogen storage alloy powder

Info

Publication number
JP3462682B2
JP3462682B2 JP32125396A JP32125396A JP3462682B2 JP 3462682 B2 JP3462682 B2 JP 3462682B2 JP 32125396 A JP32125396 A JP 32125396A JP 32125396 A JP32125396 A JP 32125396A JP 3462682 B2 JP3462682 B2 JP 3462682B2
Authority
JP
Japan
Prior art keywords
hydrogen storage
storage alloy
nickel
alloy powder
treatment liquid
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
JP32125396A
Other languages
Japanese (ja)
Other versions
JPH10162814A (en
Inventor
宏 中村
修一 鈴木
伸 藤谷
光造 野上
育郎 米津
晃治 西尾
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 Electric Co Ltd
Original Assignee
Sanyo Electric 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 Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP32125396A priority Critical patent/JP3462682B2/en
Publication of JPH10162814A publication Critical patent/JPH10162814A/en
Application granted granted Critical
Publication of JP3462682B2 publication Critical patent/JP3462682B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

  • Battery Electrode And Active Subsutance (AREA)
  • Powder Metallurgy (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、例えばニッケル−
水素二次電池の電極(負極)の材料として用いる水素吸蔵
合金粉末の製造方法に関するものである。
BACKGROUND OF THE INVENTION The present invention relates to, for example, nickel-
The present invention relates to a method for producing a hydrogen storage alloy powder used as a material for an electrode (negative electrode) of a hydrogen secondary battery.

【0002】[0002]

【従来の技術】ニッケル−水素二次電池の負極となる水
素吸蔵合金電極は、水素吸蔵合金塊を粉砕して得られる
水素吸蔵合金粉末に結着剤を加え、これを電極形状に成
形することによって作製される。水素吸蔵合金として
は、AB5型やAB2型の希土類系の水素吸蔵合金、例え
ばMm−Ni系や、Laを含むZr−Ni系の水素吸蔵合金
が用いられる。ところで、ニッケル−水素二次電池にお
いては、水素吸蔵合金の活性向上を図るため、水素吸蔵
合金粉末を塩酸等の酸性水溶液中に所定時間浸漬する表
面処理が施される。この表面処理によって、合金粒子の
表面に形成されている酸化被膜が除去されると共に、希
土類元素(La等)が溶解して、粒子表面にニッケルなど
の金属面が露出し、この結果、電気化学的な触媒活性が
向上するのである。
2. Description of the Related Art A hydrogen storage alloy electrode which serves as a negative electrode of a nickel-hydrogen secondary battery is obtained by adding a binder to a hydrogen storage alloy powder obtained by crushing a hydrogen storage alloy lump and molding the powder into an electrode shape. Made by. As the hydrogen storage alloy, an AB 5 type or AB 2 type rare earth-based hydrogen storage alloy, for example, an Mm-Ni-based or Zr-Ni-based hydrogen storage alloy containing La is used. By the way, in the nickel-hydrogen secondary battery, in order to improve the activity of the hydrogen storage alloy, a surface treatment is carried out by immersing the hydrogen storage alloy powder in an acidic aqueous solution such as hydrochloric acid for a predetermined time. By this surface treatment, the oxide film formed on the surface of the alloy particles is removed, the rare earth elements (La, etc.) are dissolved, and a metal surface such as nickel is exposed on the surface of the particles. The catalytic activity is improved.

【0003】しかしながら、従来の表面改質方法におい
ては、処理中に処理液のpHが急激に上昇することによ
って、合金粒子の表面からの金属の溶出速度が場所によ
って区々となり、均一な表面改質を図ることが困難であ
った。又、金属が水酸化物となって表面に析出し、厚い
層を形成するため、十分な活性向上を図ることが出来な
いばかりでなく、水素吸蔵合金の水素ガス吸収能も低下
する問題があった。
However, in the conventional surface modification method, the pH of the treatment liquid rapidly rises during the treatment, so that the elution rate of the metal from the surface of the alloy particles varies depending on the location, and the uniform surface modification is performed. It was difficult to measure the quality. Further, the metal becomes a hydroxide and is deposited on the surface to form a thick layer, so that not only the activity cannot be sufficiently improved, but also the hydrogen gas absorption capacity of the hydrogen storage alloy is lowered. It was

【0004】そこで、出願人は、緩衝作用を有する酸性
の処理液によって、水素吸蔵合金粒子の表面を改質する
方法を提案している(特開平8-185856号)。該方法によれ
ば、処理液の緩衝作用によってpHが略一定に保持され
るので、水素吸蔵合金粒子の表面改質が均一に行なわれ
ると共に、水酸化物の析出が抑制されて、従来よりも高
い活性とガス吸収能が得られる。
Therefore, the applicant has proposed a method of modifying the surface of the hydrogen storage alloy particles with an acidic treatment liquid having a buffering action (JP-A-8-185856). According to this method, since the pH is kept substantially constant by the buffering action of the treatment liquid, the surface modification of the hydrogen-absorbing alloy particles is performed uniformly, and the precipitation of hydroxide is suppressed, so that the hydrogen-absorbing alloy particles are suppressed more than before. High activity and gas absorption capacity are obtained.

【0005】[0005]

【発明が解決しようとする課題】ところが、出願人の提
案に係る表面改質方法によっても、金属面の露出によっ
て得られるはずの高い活性が依然として得られていない
ことが判明した。発明者らは、鋭意研究の結果、以下の
様にその原因を究明し、本発明の完成に至った。即ち、
緩衝作用を有する酸性の処理液によって水素吸蔵合金粒
子に表面処理を施した場合、図4に示す如く、水素吸蔵
合金粒子(1)の表面からは、金属状態或いは酸化物状態
の構成元素(La、Ni、Mn等)が処理液(3)中に均等
に溶出することとなるため、活性向上に寄与すべきニッ
ケルの溶出によって、所期の活性が得られないのであ
る。
However, it has been found that the surface modification method proposed by the applicant has not yet obtained the high activity that should be obtained by exposing the metal surface. As a result of intensive research, the inventors of the present invention have clarified the cause thereof and completed the present invention as follows. That is,
When the hydrogen storage alloy particles are surface-treated with an acidic treatment liquid having a buffering action, as shown in FIG. 4, from the surface of the hydrogen storage alloy particles (1), a constituent element (La) in a metal state or an oxide state (La) is formed. , Ni, Mn, etc.) are evenly eluted in the treatment liquid (3), and the desired activity cannot be obtained due to the elution of nickel that should contribute to the activity improvement.

【0006】[0006]

【課題を解決する為の手段】そこで、本発明において
は、水素吸蔵合金粒子の表面改質に用いるべき処理液と
して、ニッケルイオンを含有し且つ緩衝作用を有する
期pHが4.1〜5に調整された酸性の処理液を採用す
る。即ち、水素吸蔵合金粉末の製造においては、水素吸
蔵合金塊を粉砕して水素吸蔵合金粉末を作製した後、該
水素吸蔵合金粉末に対し、ニッケルイオンを含有し且つ
緩衝作用を有する初期pHが4.1〜5に調整された
性の処理液による表面処理を施す。
Means for Solving the Problems] Therefore, in the present invention, as the processing liquid to be used for surface modification of the hydrogen storage alloy particles, the first and having a buffering action containing nickel ions
An acidic treatment liquid whose pH is adjusted to 4.1 to 5 is adopted. That is, in the production of the hydrogen storage alloy powder, after crushing the hydrogen storage alloy powder to prepare the hydrogen storage alloy powder, the initial pH of the hydrogen storage alloy powder containing nickel ions and having a buffering action is 4 Surface treatment with an acid treatment liquid adjusted to 0.1 to 5 is performed.

【0007】上記の如く、ニッケルイオンを含有し且つ
緩衝作用を有する酸性の処理液を用いた水素吸蔵合金粒
子の表面処理においては、処理液が有する酸性によっ
て、粒子表面の酸化被膜が除去されると共に、希土類元
素の溶解によって、粒子表面にはニッケルなどの金属面
が露出する。この際、処理液が発揮する緩衝作用によっ
て、処理液のpHが略一定に保持され、表面改質の均一
化が図られると共に、水酸化物の析出が抑制される。こ
こで、処理液には予めニッケルイオンが含まれており、
処理液中に存在し得るニッケルイオンの量には限界があ
るので、粒子表面からのニッケルの溶出が抑制される。
この結果、水素吸蔵合金粒子の表層部にはニッケルが富
化した層が形成され、例えば深さ10nm以内の表層部
において全構成元素に対するニッケルの相対比率が75
atm%以上の高い値となる。水素吸蔵合金粒子の表層部
のニッケルは、粒子表面における電気化学的な水素吸収
解離反応に対し、導電性、触媒活性の両面で寄与するこ
とになる。
As described above, in the surface treatment of hydrogen storage alloy particles using an acidic treatment liquid containing nickel ions and having a buffering action, the acid coating of the treatment liquid removes the oxide film on the surface of the particles. At the same time, the dissolution of the rare earth element exposes a metal surface such as nickel on the particle surface. At this time, the buffering action of the treatment liquid keeps the pH of the treatment liquid substantially constant, uniformizes the surface modification, and suppresses the precipitation of hydroxide. Here, the treatment liquid contains nickel ions in advance,
Since the amount of nickel ions that can be present in the treatment liquid is limited, the elution of nickel from the particle surface is suppressed.
As a result, a nickel-enriched layer is formed on the surface layer of the hydrogen storage alloy particles, and for example, in the surface layer within a depth of 10 nm, the relative ratio of nickel to all constituent elements is 75.
It becomes a high value of atm% or more. Nickel in the surface layer portion of the hydrogen storage alloy particles contributes to the electrochemical hydrogen absorption / dissociation reaction on the surface of the particle in terms of both conductivity and catalytic activity.

【0008】pHが1未満の処理液では、合金粒子の内
部まで浸食を受ける虞れがあり、pHが5を越える処理
液では、高い表面改質効果が得られない。
A treatment liquid having a pH of less than 1 may corrode the inside of the alloy particles, and a treatment liquid having a pH of more than 5 may not provide a high surface modification effect.

【0009】又、処理液は、緩衝作用を有する酸性溶液
に、ニッケルを含む添加剤を添加したものであって、添
加剤の濃度は0.001mol/l以上に設定することが望
ましい。添加剤の濃度が0.001mol/l未満では、ニ
ッケルの溶出を高い効果で抑制することが出来ない。但
し、添加剤の濃度が0.01mol/lを越えると、その効
果は飽和することになる。従って、添加剤の濃度として
は、0.001mol/l〜0.01mol/lが望ましい。
The treatment liquid is an acidic solution having a buffering action and an additive containing nickel is added, and the concentration of the additive is preferably set to 0.001 mol / l or more. If the concentration of the additive is less than 0.001 mol / l, nickel elution cannot be suppressed with high effect. However, when the concentration of the additive exceeds 0.01 mol / l, the effect is saturated. Therefore, the concentration of the additive is preferably 0.001 mol / l to 0.01 mol / l.

【0010】[0010]

【発明の効果】本発明によれば、ニッケルの富化した層
の形成によって高い活性とガス吸収能を発揮する水素吸
蔵合金粉末及び水素吸蔵合金電極を得ることが出来る。
According to the present invention, a hydrogen storage alloy powder and a hydrogen storage alloy electrode exhibiting high activity and gas absorption ability can be obtained by forming a nickel-enriched layer.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の形態につ
き、図面に沿って具体的に説明する。本発明に係る水素
吸蔵合金粉末は、後述の如く、ニッケルイオンを含有し
且つ緩衝作用を有する酸性の処理液によって表面処理を
施したものであって、該表面処理の結果、水素吸蔵合金
粒子は、深さ10nm以内の表層部において全構成元素
に対するニッケルの相対比率が75atm%以上となって
いる。ここで、水素吸蔵合金粒子は、AB5型の希土類
系水素吸蔵合金やAB2型の非希土類系水素吸蔵合金、
例えばMmNi3.3CoMn0.5Al0.2、ZrNi1.2
0.2Mn0.6、ZrLa0.05Ni1.20.2Mn0.6等から
形成されている。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be specifically described below with reference to the drawings. The hydrogen-absorbing alloy powder according to the present invention is, as described below, subjected to surface treatment with an acidic treatment liquid containing nickel ions and having a buffering action, and as a result of the surface treatment, the hydrogen-absorbing alloy particles are The relative ratio of nickel to all the constituent elements is 75 atm% or more in the surface layer portion within a depth of 10 nm. Here, the hydrogen storage alloy particles include AB 5 type rare earth hydrogen storage alloys, AB 2 type non-rare earth hydrogen storage alloys,
For example, MmNi 3.3 CoMn 0.5 Al 0.2 , ZrNi 1.2 V
It is formed of 0.2 Mn 0.6 , ZrLa 0.05 Ni 1.2 V 0.2 Mn 0.6, and the like.

【0012】図3は、上記の水素吸蔵合金粉末を負極材
料として用いたニッケル−水素二次電池の構造を表わし
ており、正極(11)、負極(12)、セパレータ(13)、正極リ
ード(14)、負極リード(15)、正極外部端子(16)、負極缶
(17)、封口蓋(18)等から密閉構造のニッケル−水素二次
電池が構成されている。正極(11)及び負極(12)は、セパ
レータ(13)を介して渦巻き状に巻き取られた状態で、負
極缶(17)内に収容されており、正極(11)は正極リード(1
4)を介して封口蓋(18)に、又負極(12)は負極リード(15)
を介して負極缶(17)に接続されている。負極缶(17)と封
口蓋(18)との接合部には、絶縁性のパッキング(20)が装
着されて電池の密閉化が為されている。正極外部端子(1
6)と封口蓋(18)との間にはコイルスプリング(19)が設け
られる。該コイルスプリング(19)は、電池内圧が異常に
上昇した時に圧縮されて、電池内部のガスを大気中に放
出するものである。
FIG. 3 shows a structure of a nickel-hydrogen secondary battery using the above hydrogen storage alloy powder as a negative electrode material. The positive electrode (11), the negative electrode (12), the separator (13) and the positive electrode lead ( 14), negative lead (15), positive external terminal (16), negative can
(17), the sealing lid (18) and the like constitute a nickel-hydrogen secondary battery having a sealed structure. The positive electrode (11) and the negative electrode (12) are housed in a negative electrode can (17) in a spirally wound state via a separator (13), and the positive electrode (11) is a positive electrode lead (1).
4) to the sealing lid (18) and the negative electrode (12) to the negative electrode lead (15).
It is connected to the negative electrode can (17) via. An insulating packing (20) is attached to the joint between the negative electrode can (17) and the sealing lid (18) to seal the battery. Positive external terminal (1
A coil spring (19) is provided between 6) and the sealing lid (18). The coil spring (19) is compressed when the internal pressure of the battery rises abnormally, and releases the gas inside the battery to the atmosphere.

【0013】上記ニッケル−水素二次電池の製造におい
ては、図1に示す如く、先ず、所定の組成を有する水素
吸蔵合金のインゴットを作製した後、これを粒径5μm
〜500μmに粉砕して、水素吸蔵合金粉末を作製する
(工程P1)。次に、水素吸蔵合金粉末を、ニッケルイオ
ンを含有し且つ緩衝作用を有する酸性の処理液中に浸漬
して、20分程度撹拌し、水素吸蔵合金粒子に表面処理
を施す。緩衝作用を有する溶液としては、弱酸とその弱
酸の塩とを1:9〜9:1のモル比で溶解させたもの、
例えばクエン酸とクエン酸塩の組合せ、リン酸とリン酸
塩の組合せ、リンゴ酸とリンゴ酸塩の組合せ、フタル酸
とフタル酸塩の組合せ、シュウ酸とシュウ酸塩の組合せ
等が採用可能であり、塩のカチオンとしては、ナトリウ
ム、カリウム、リチウム等が採用可能である。処理液の
pHは1〜5に調整することが望ましい。そして、これ
らの酸性溶液に、金属ニッケル、塩化ニッケル、ヨウ化
ニッケル等を添加して、ニッケルイオンを含有せしめ
る。添加剤の濃度は0.001mol/l以上に設定するこ
とが望ましい。続いて、水素吸蔵合金粉末に水洗、乾燥
を施し、本発明に係る表面処理の施された合金粉末を得
る。
In the manufacture of the above nickel-hydrogen secondary battery, as shown in FIG. 1, first, an ingot of a hydrogen storage alloy having a predetermined composition is prepared, and then the particle size is 5 μm.
To 500 μm to produce a hydrogen storage alloy powder
(Process P1). Next, the hydrogen storage alloy powder is immersed in an acidic treatment liquid containing nickel ions and having a buffering action, and stirred for about 20 minutes to subject the hydrogen storage alloy particles to a surface treatment. As the solution having a buffering action, a solution obtained by dissolving a weak acid and a salt of the weak acid in a molar ratio of 1: 9 to 9: 1,
For example, a combination of citric acid and citrate, a combination of phosphoric acid and phosphate, a combination of malic acid and malate, a combination of phthalic acid and phthalate, a combination of oxalic acid and oxalate, etc. can be adopted. Therefore, sodium, potassium, lithium or the like can be used as the cation of the salt. It is desirable to adjust the pH of the treatment liquid to 1-5. Then, metallic nickel, nickel chloride, nickel iodide, or the like is added to these acidic solutions to contain nickel ions. It is desirable to set the concentration of the additive to 0.001 mol / l or more. Then, the hydrogen storage alloy powder is washed with water and dried to obtain the surface-treated alloy powder according to the present invention.

【0014】その後、図3に示すニッケル−水素二次電
池を組み立てる(工程P3)。先ず、工程P2を経て得ら
れた水素吸蔵合金粉末と、PTFEなどの結着剤の水溶
液とを混合して、ペーストを調整し、該ペーストをニッ
ケル鍍金を施したパンチングメタルからなる基体の両面
に塗布し、室温で乾燥を施した後、所定寸法に切断し
て、水素吸蔵合金電極を作製する。そして、該水素吸蔵
合金電極を負極に用いて、図3に示す構造の正極支配型
ニッケル−水素電池(例えば電池容量1000mAh)を
作製する。尚、正極としては焼結式ニッケル極を、セパ
レータとしては耐アルカリ性の不織布を、又電解液とし
ては30重量%水酸化カリウム水溶液を用いることが出
来る。
After that, the nickel-hydrogen secondary battery shown in FIG. 3 is assembled (process P3). First, the hydrogen storage alloy powder obtained through the process P2 and an aqueous solution of a binder such as PTFE are mixed to prepare a paste, and the paste is applied to both sides of a nickel-plated base made of punching metal. After being applied and dried at room temperature, it is cut into a predetermined size to prepare a hydrogen storage alloy electrode. Then, using the hydrogen storage alloy electrode as a negative electrode, a positive electrode dominant nickel-hydrogen battery (for example, battery capacity 1000 mAh) having a structure shown in FIG. 3 is manufactured. A sintered nickel electrode can be used as the positive electrode, an alkali-resistant nonwoven fabric can be used as the separator, and a 30 wt% potassium hydroxide aqueous solution can be used as the electrolytic solution.

【0015】上記水素吸蔵合金粉末の表面処理(工程P
2)においては、処理液のpHがその緩衝作用によって
略一定に保持されるので、水素吸蔵合金粒子の表面改質
が均一に行なわれると共に、水酸化物の析出が抑制され
て、従来よりも高い活性とガス吸収能が得られる。
Surface treatment of the above hydrogen storage alloy powder (process P
In 2), the pH of the treatment liquid is kept substantially constant by its buffering action, so that the surface modification of the hydrogen-absorbing alloy particles is performed uniformly, and the precipitation of hydroxide is suppressed, so that it is better than before. High activity and gas absorption capacity are obtained.

【0016】又図2に示す如く、水素吸蔵合金粒子(1)
の表面からは、La等の希土類元素の他、Ni、Mnな
どの金属が溶出するが、処理液(2)中には予めニッケル
イオンが含まれており、処理液中に存在し得るニッケル
イオンの量には限界があるので、粒子表面からのニッケ
ルの溶出が抑制されることになる。希土類元素の溶出に
よって、水素吸蔵合金粒子(1)の表面には金属面が現わ
れると共に、上述の如く粒子表面からのニッケルの溶出
が抑制されて、水素吸蔵合金粒子の表層部にはニッケル
が富化した層が形成されるので、水素吸蔵合金の電気化
学的な触媒活性とガス吸収能の向上が図られる。
As shown in FIG. 2, hydrogen storage alloy particles (1)
Although rare earth elements such as La as well as metals such as Ni and Mn are eluted from the surface of the treatment solution, the treatment solution (2) contains nickel ions in advance, and nickel ions that may be present in the treatment solution are present. Since the amount of nickel is limited, the elution of nickel from the particle surface is suppressed. By elution of the rare earth element, a metal surface appears on the surface of the hydrogen storage alloy particles (1), and the elution of nickel from the particle surface is suppressed as described above, and the surface layer of the hydrogen storage alloy particles is rich in nickel. Since the converted layer is formed, the electrochemical catalytic activity and the gas absorption capacity of the hydrogen storage alloy can be improved.

【0017】図5及び図6は、上記本発明の効果を確認
するために行なった実験の結果を表わしている。実験に
は、組成MmNi3.3CoMn0.5Al0.2の水素吸蔵合
金粉末を用い、該水素吸蔵合金粉末50gを図5中に示
す各処理液(100ml)中に浸漬して、20分間の撹拌
後、水洗及び乾燥を施した。次に、処理後の各水素吸蔵
合金粉末を用いて試験電極を作製し、該試験電極を負極
とする試験セルを組み立てた。そして、該試験セルを用
いて充放電を繰り返し、放電容量を測定した。
FIG. 5 and FIG. 6 show the results of experiments conducted to confirm the effects of the present invention. In the experiment, a hydrogen storage alloy powder having a composition of MmNi 3.3 CoMn 0.5 Al 0.2 was used, and 50 g of the hydrogen storage alloy powder was immersed in each treatment liquid (100 ml) shown in FIG. 5, stirred for 20 minutes, and washed with water. And dried. Next, a test electrode was prepared using each hydrogen storage alloy powder after the treatment, and a test cell having the test electrode as a negative electrode was assembled. Then, charge and discharge were repeated using the test cell to measure the discharge capacity.

【0018】図5は、充放電の繰返しの中で得られた1
サイクル目の放電容量と、最大の放電容量と、最大容量
に対する1サイクル目の放電容量の比率(%)、即ち初期
活性化率とを表わしている。
FIG. 5 shows 1 obtained during repeated charging and discharging.
It represents the discharge capacity at the cycle, the maximum discharge capacity, and the ratio (%) of the discharge capacity at the first cycle to the maximum capacity, that is, the initial activation rate.

【0019】実験番号1〜3では、緩衝作用を有する酸
性溶液として、クエン酸及びクエン酸ナトリウムの溶液
を用い、添加剤として、塩化ニッケル、ヨウ化ニッケ
ル、或いは金属ニッケルを加えた3種類の処理液によっ
て表面処理を施した。添加剤の濃度は何れも0.1M(mo
l/l)である。これに対し、実験番号4では、緩衝作用
を有する酸性溶液に添加剤を加えない処理液を用いてい
る。実験番号1〜4の何れの場合も、処理液の緩衝作用
によって、処理前後のpHに大きな変化はないが、実験
番号1〜3で得られた初期活性化率は、実験番号4で得
られた値を上回っており、添加剤を用いた効果が顕れて
いる。一方、実験番号5及び6は、緩衝作用を有しない
酸性溶液を用いたものであって、添加剤の添加の有無に
拘わらず、初期活性化率は低い値を示している。この場
合、処理前後でpHが大きく増大している。
In Experiment Nos. 1 to 3, a solution of citric acid and sodium citrate was used as an acidic solution having a buffering action, and nickel chloride, nickel iodide, or nickel metal was added as an additive in three kinds of treatments. Surface treatment was performed with the liquid. The concentration of each additive was 0.1M (mo
l / l). On the other hand, in Experiment No. 4, a treatment liquid in which no additive is added to the acidic solution having a buffer action is used. In any of Experiment Nos. 1 to 4, there was no great change in the pH before and after the treatment due to the buffering effect of the treatment solution, but the initial activation rates obtained in Experiment Nos. 1 to 3 were obtained in Experiment No. 4. The value obtained by using the additive is apparent. On the other hand, Experiment Nos. 5 and 6 use an acidic solution having no buffering action, and show a low initial activation rate regardless of whether or not the additive is added. In this case, the pH is greatly increased before and after the treatment.

【0020】実験番号7及び8は、緩衝作用を有する酸
性溶液として、リン酸及びリン酸ナトリウムの溶液を用
いたものであって、塩化ニッケルを添加剤として加えた
実験番号7では、添加剤を加えなかった実験番号8の場
合に比べて、高い初期活性化率が得られている。又、実
験番号9及び10は、緩衝作用を有する酸性溶液とし
て、リンゴ酸及びリンゴ酸ナトリウムの溶液を用いたも
のであって、塩化ニッケルを添加剤として加えた実験番
号9では、添加剤を加えなかった実験番号10の場合に
比べて、高い初期活性化率が得られている。従って、緩
衝作用を有する酸性溶液としては、クエン酸及びクエン
酸ナトリウムの溶液に限らず、リン酸及びリン酸ナトリ
ウムの溶液や、リンゴ酸及びリンゴ酸ナトリウムの溶液
も有効であることが裏付けられる。
Experiment Nos. 7 and 8 used a solution of phosphoric acid and sodium phosphate as an acidic solution having a buffer action. In Experiment No. 7 in which nickel chloride was added as an additive, the additive was added. A high initial activation rate is obtained as compared to the case of Experiment No. 8 in which no addition was made. Further, in Experiment Nos. 9 and 10, a solution of malic acid and sodium malate was used as the acidic solution having a buffering action. In Experiment No. 9 in which nickel chloride was added as an additive, the additive was added. A high initial activation rate is obtained as compared with the case of Experiment No. 10 which did not exist. Therefore, it is proved that the acidic solution having a buffering effect is not limited to the solution of citric acid and sodium citrate, but the solution of phosphoric acid and sodium phosphate and the solution of malic acid and sodium malate are also effective.

【0021】更に実験番号11〜13は、クエン酸及び
クエン酸ナトリウムの溶液に加えるべき添加剤(塩化ニ
ッケル)の濃度を0.001M、0.01M及び0.1Mに
変化させたものであって、添加剤の濃度が0.001M
では、実験番号4の従来例に比べて高い初期活性化率が
得られているが、濃度を0.01Mに増大させることに
よって、十分に高い初期活性化率が得られる。しかし、
濃度を0.1Mまで上げたとしても、それ以上、初期活
性化率は増大せず、飽和している。従って、添加剤の濃
度は、0.001M〜0.01Mの範囲が好ましいと言え
る。
Further, in Experiment Nos. 11 to 13, the concentration of the additive (nickel chloride) to be added to the solution of citric acid and sodium citrate was changed to 0.001M, 0.01M and 0.1M. , The concentration of additives is 0.001M
In contrast, a higher initial activation rate was obtained than in the conventional example of Experiment No. 4, but a sufficiently high initial activation rate was obtained by increasing the concentration to 0.01M. But,
Even if the concentration is increased to 0.1 M, the initial activation rate does not increase any more, and it is saturated. Therefore, it can be said that the concentration of the additive is preferably in the range of 0.001M to 0.01M.

【0022】又、図6は、透過型電子顕微鏡−定量分析
装置(TEM−EDX)を用いて、各水素吸蔵合金粒子の
表面からの深さ5nm、10nm及び粒子中心部(バル
ク)におけるニッケル比率(全元素中にニッケルが占める
割合、atm%)を測定した結果を表わしている。本発明に
相当する実験番号1では、従来例に相当する実験番号4
及び5に比べて、深さ5nm及び10nmの何れにおい
てもニッケル比率が大きくなっており、本発明の処理液
を用いた表面処理によって、ニッケルの溶出が抑えられ
ていることが明らかである。尚、水素吸蔵合金粒子の中
心部では、水素吸蔵合金が有する本来のニッケル比率に
応じた値が得られている。
FIG. 6 is a transmission electron microscope-quantitative analyzer (TEM-EDX) used to measure the depth of each hydrogen storage alloy particle from the surface to a depth of 5 nm, 10 nm, and the nickel ratio at the particle center (bulk). It represents the result of measuring (the proportion of nickel in all elements, atm%). The experiment number 1 corresponding to the present invention is the experiment number 4 corresponding to the conventional example.
Compared with Nos. 5 and 5, the nickel ratio was high at both the depths of 5 nm and 10 nm, and it is clear that the elution of nickel is suppressed by the surface treatment using the treatment liquid of the present invention. At the center of the hydrogen storage alloy particles, a value corresponding to the original nickel ratio of the hydrogen storage alloy was obtained.

【0023】又、本発明に相当する実験番号7において
も、従来例に相当する実験番号8に比べて、深さ5nm
及び10nmでのニッケル比率が大きくなっており、ニ
ッケルの溶出が抑えられていることが明らかである。更
に、本発明に相当する実験番号11でも同様にニッケル
の溶出が抑えられていることが明らかである。
Also, in Experiment No. 7 corresponding to the present invention, the depth is 5 nm as compared with Experiment No. 8 corresponding to the conventional example.
And the nickel ratio at 10 nm is large, and it is clear that the elution of nickel is suppressed. Further, it is apparent that the elution of nickel is also suppressed in Experiment No. 11 corresponding to the present invention.

【0024】以上の結果から、ニッケルイオンを含有し
且つ緩衝作用を有する酸性の処理液を用いた表面処理に
よって、水素吸蔵合金粒子は、表面からの深さが10n
m以内の表層部においてニッケル比率が75atm%以上
となり、これによって水素吸蔵合金電極の初期活性及び
ガス吸収能が向上することが裏付けられる。
From the above results, the hydrogen storage alloy particles have a depth of 10 n from the surface by the surface treatment using the acidic treatment liquid containing nickel ions and having a buffering action.
The nickel ratio becomes 75 atm% or more in the surface layer portion within m, which proves that the initial activity and gas absorption capacity of the hydrogen storage alloy electrode are improved.

【0025】上記実施の形態の説明は、本発明を説明す
るためのものであって、特許請求の範囲に記載の発明を
限定し、或は範囲を減縮する様に解すべきではない。
又、本発明の各部構成は上記実施の形態に限らず、特許
請求の範囲に記載の技術的範囲内で種々の変形が可能で
あることは勿論である。
The above description of the embodiments is for explaining the present invention and should not be construed as limiting the invention described in the claims or reducing the scope.
Further, it goes without saying that the configuration of each part of the present invention is not limited to the above-described embodiment, and various modifications can be made within the technical scope described in the claims.

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

【図1】本発明に係る水素吸蔵合金電極の製造方法を表
わす工程図である。
FIG. 1 is a process drawing showing a method for producing a hydrogen storage alloy electrode according to the present invention.

【図2】ニッケルイオンを含む酸性の処理液の作用を説
明する図である。
FIG. 2 is a diagram illustrating the action of an acidic treatment liquid containing nickel ions.

【図3】ニッケル−水素二次電池の断面図である。FIG. 3 is a cross-sectional view of a nickel-hydrogen secondary battery.

【図4】ニッケルイオンを含まない酸性の処理液の作用
を説明する図である。
FIG. 4 is a diagram for explaining the action of an acidic treatment liquid that does not contain nickel ions.

【図5】本発明の効果を確認するために行なった実験の
結果を表わす図表である。
FIG. 5 is a chart showing the results of an experiment conducted to confirm the effect of the present invention.

【図6】同上の他の図表である。FIG. 6 is another diagram of the same as above.

【符号の説明】[Explanation of symbols]

(1) 水素吸蔵合金粒子 (2) 処理液 (11) 正極 (12) 負極 (13) セパレータ (1) Hydrogen storage alloy particles (2) Treatment liquid (11) Positive electrode (12) Negative electrode (13) Separator

───────────────────────────────────────────────────── フロントページの続き (72)発明者 野上 光造 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (72)発明者 米津 育郎 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (72)発明者 西尾 晃治 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (56)参考文献 特開 平10−12233(JP,A) 特開 平8−291391(JP,A) 国際公開95/023435(WO,A1) (58)調査した分野(Int.Cl.7,DB名) B22F 1/00 B22F 5/00 H01M 4/24 H01M 4/26 H01M 4/38 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kozo Nogami, 2-5-5 Keihan Hondori, Moriguchi City, Osaka Prefecture Sanyo Denki Co., Ltd. (72) Ikuro Yonezu 2-chome, Keihan Hondori, Moriguchi City, Osaka Prefecture No. 5 within Sanyo Electric Co., Ltd. (72) Inventor Koji Nishio 2-5-5 Keihan Hondori, Moriguchi City, Osaka Sanyo Electric Co., Ltd. (56) Reference JP-A-10-12233 (JP, A) Hei 8-291391 (JP, A) International publication 95/023435 (WO, A1) (58) Fields investigated (Int.Cl. 7 , DB name) B22F 1/00 B22F 5/00 H01M 4/24 H01M 4 / 26 H01M 4/38

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水素吸蔵合金塊を粉砕して水素吸蔵合金
粉末を作製した後、該水素吸蔵合金粉末に対し、ニッケ
ルイオンを含有し且つ緩衝作用を有する初期pHが4.
1〜5に調整されている酸性の処理液による表面処理を
施すことを特徴とする水素吸蔵合金粉末の製造方法。
1. A hydrogen storage alloy powder is produced by crushing a lump of hydrogen storage alloy, and the initial pH of the hydrogen storage alloy powder containing nickel ions and having a buffering action is 4.
A method for producing a hydrogen storage alloy powder, which comprises subjecting a surface treatment with an acidic treatment liquid adjusted to 1 to 5 .
【請求項2】 処理液は、緩衝作用を有する酸性溶液
に、ニッケルを含む添加剤を添加したものであって、添
加剤の濃度は0.001mol/l以上に設定されている
求項1に記載の水素吸蔵合金粉末の製造方法。
2. A treatment liquid, an acidic solution having a buffering action, a liquid obtained by adding an additive containing nickel, the concentration of the additive is set to more than 0.001mol / l
The method for producing a hydrogen storage alloy powder according to claim 1 .
【請求項3】3. 緩衝作用を有する酸性溶液は、リンゴ酸A buffered acidic solution is malic acid.
とリンゴ酸塩とを溶解させたものである請求項2に記載The solution according to claim 2, which is a solution of maltate and malate.
の水素吸蔵合金粉末の製造方法。Method for producing hydrogen storage alloy powder of.
JP32125396A 1996-12-02 1996-12-02 Method for producing hydrogen storage alloy powder Expired - Fee Related JP3462682B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32125396A JP3462682B2 (en) 1996-12-02 1996-12-02 Method for producing hydrogen storage alloy powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32125396A JP3462682B2 (en) 1996-12-02 1996-12-02 Method for producing hydrogen storage alloy powder

Publications (2)

Publication Number Publication Date
JPH10162814A JPH10162814A (en) 1998-06-19
JP3462682B2 true JP3462682B2 (en) 2003-11-05

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Country Link
JP (1) JP3462682B2 (en)

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Publication number Priority date Publication date Assignee Title
JP4128635B2 (en) * 1997-03-14 2008-07-30 株式会社東芝 Manufacturing method of nickel metal hydride storage battery

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