JPH09302401A - Treatment of hydrogen storage alloy powder - Google Patents
Treatment of hydrogen storage alloy powderInfo
- Publication number
- JPH09302401A JPH09302401A JP8116766A JP11676696A JPH09302401A JP H09302401 A JPH09302401 A JP H09302401A JP 8116766 A JP8116766 A JP 8116766A JP 11676696 A JP11676696 A JP 11676696A JP H09302401 A JPH09302401 A JP H09302401A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- alloy powder
- storage alloy
- treatment
- oxide film
- 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.)
- Granted
Links
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 163
- 239000000956 alloy Substances 0.000 title claims abstract description 163
- 239000001257 hydrogen Substances 0.000 title claims abstract description 105
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 105
- 239000000843 powder Substances 0.000 title claims abstract description 104
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 88
- 238000003860 storage Methods 0.000 title claims abstract description 88
- 238000000034 method Methods 0.000 claims abstract description 76
- 238000010438 heat treatment Methods 0.000 claims abstract description 31
- 230000002378 acidificating effect Effects 0.000 claims abstract description 25
- 239000007864 aqueous solution Substances 0.000 claims description 36
- 238000007711 solidification Methods 0.000 claims description 17
- 230000008023 solidification Effects 0.000 claims description 17
- 230000001590 oxidative effect Effects 0.000 claims description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 22
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 abstract description 21
- 239000002253 acid Substances 0.000 abstract description 21
- 238000010306 acid treatment Methods 0.000 abstract description 14
- 230000004913 activation Effects 0.000 abstract description 13
- 230000008569 process Effects 0.000 abstract description 9
- 150000002431 hydrogen Chemical class 0.000 abstract description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract 1
- 230000003213 activating effect Effects 0.000 abstract 1
- 239000000460 chlorine Substances 0.000 abstract 1
- 229910052801 chlorine Inorganic materials 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 34
- 230000000694 effects Effects 0.000 description 20
- 230000000977 initiatory effect Effects 0.000 description 19
- 238000007712 rapid solidification Methods 0.000 description 19
- 238000001994 activation Methods 0.000 description 15
- 238000010298 pulverizing process Methods 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 11
- 238000004381 surface treatment Methods 0.000 description 10
- 238000001816 cooling Methods 0.000 description 9
- 239000013078 crystal Substances 0.000 description 9
- 239000007788 liquid Substances 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 238000009210 therapy by ultrasound Methods 0.000 description 9
- 238000009689 gas atomisation Methods 0.000 description 7
- 238000007654 immersion Methods 0.000 description 7
- 238000010791 quenching Methods 0.000 description 7
- 230000000171 quenching effect Effects 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000011260 aqueous acid Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 238000005554 pickling Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 3
- 229910001122 Mischmetal Inorganic materials 0.000 description 3
- 229910018007 MmNi Inorganic materials 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- QPJSUIGXIBEQAC-UHFFFAOYSA-N n-(2,4-dichloro-5-propan-2-yloxyphenyl)acetamide Chemical compound CC(C)OC1=CC(NC(C)=O)=C(Cl)C=C1Cl QPJSUIGXIBEQAC-UHFFFAOYSA-N 0.000 description 3
- 229910052720 vanadium Inorganic materials 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910052684 Cerium Inorganic materials 0.000 description 2
- 229910052779 Neodymium Inorganic materials 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 229910052777 Praseodymium Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 229910052790 beryllium Inorganic materials 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 229910052761 rare earth metal Inorganic materials 0.000 description 2
- 150000002910 rare earth metals Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- 229910003307 Ni-Cd Inorganic materials 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910008340 ZrNi Inorganic materials 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000006182 cathode active material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hcl hcl Chemical compound Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910000765 intermetallic Inorganic materials 0.000 description 1
- 229910001068 laves phase Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000007773 negative electrode material Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000009700 powder processing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000004506 ultrasonic cleaning Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- 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
- Battery Electrode And Active Subsutance (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、AB5 型、AB2
型などの二次電池用 (特にNi−水素二次電池用)水素吸
蔵合金粉末の処理方法に関する。本発明の処理方法によ
り、初期活性化が容易で、高温での自己放電が少なく、
電極寿命の長い電池用の水素吸蔵合金粉末が得られる。The present invention relates is, AB 5 type, AB 2
The present invention relates to a method for treating a hydrogen storage alloy powder for secondary batteries such as molds (especially for Ni-hydrogen secondary batteries). The treatment method of the present invention facilitates initial activation, reduces self-discharge at high temperatures,
A hydrogen storage alloy powder for a battery having a long electrode life can be obtained.
【0002】[0002]
【従来の技術】AV機器やノート型パソコンのメモリー
・バックアップ用に用いる二次電池として、従来は主に
Ni−Cd電池が使用されてきた。しかし、Cdの公害問題、
Cdが亜鉛精練の副産物という資源量制約の問題、より高
電気容量の二次電池開発といった観点から、Cdに替えて
水素吸蔵合金を陰極活物質に用いたNi−水素電池と呼ば
れる二次電池が開発され、利用されるようになってき
た。Ni−水素電池は容量が高いため、電気自動車用の二
次電池としての利用も検討されており、既に量産が始ま
っている。2. Description of the Related Art As a secondary battery used for memory backup of AV equipment and notebook type personal computers, conventionally
Ni-Cd batteries have been used. But the Cd pollution problem,
From the viewpoint of the resource limitation problem that Cd is a by-product of zinc refining and the development of secondary batteries with higher electric capacity, a secondary battery called Ni-hydrogen battery that uses a hydrogen storage alloy as the cathode active material instead of Cd has been developed. It has been developed and used. Since the Ni-hydrogen battery has a high capacity, its use as a secondary battery for electric vehicles is also being considered, and mass production has already started.
【0003】Ni−水素電池用の水素吸蔵合金として検討
されてきた主な合金系は、LaNi5 やMmNi5(Mmは希土類金
属混合物であるミッシュメタル) で代表されるAB5 型
結晶構造をとる金属間化合物と、ZnV0.4Ni1.6 で代表さ
れるAB2 型のラーベス相構造をとる金属間化合物であ
る。実用化に関してはAB5 型の水素吸蔵合金の方が進
んでいるが、AB2 型構造の水素吸蔵合金も高容量を示
すので有望である。The main alloy system that has been studied as a hydrogen storage alloy for Ni-hydrogen batteries has an AB 5 type crystal structure represented by LaNi 5 and MmNi 5 (Mm is a misch metal which is a rare earth metal mixture). It is an intermetallic compound having an AB 2 type Laves phase structure represented by ZnV 0.4 Ni 1.6 . AB 5 type hydrogen storage alloys are more advanced in practical use, but AB 2 type hydrogen storage alloys are also promising because they show high capacity.
【0004】しかし、Ni−水素電池の量産においていく
つかの問題点が浮かび上がってきた。その1つは、Ni−
水素電池を構成した後の初期活性化処理 (電池の放電容
量を所定の定常値まで増大させる処理) に非常に時間が
かかり、生産性が著しく阻害されることである。However, some problems have emerged in the mass production of Ni-hydrogen batteries. One of them is Ni-
This means that the initial activation process (the process of increasing the discharge capacity of the battery to a predetermined steady value) after the hydrogen battery is constructed takes a very long time, and the productivity is significantly impaired.
【0005】現在行われている初期活性化処理は、低電
流で長時間の充電後に放電する処理(15〜20時間の充電
と数時間の放電) を所定の放電容量が得られるようにな
るまで数回繰り返すことにより行われている。このた
め、電池を組み立ててから出荷するまでに、初期活性化
処理として工場内で充電・放電を数日間繰り返す必要が
あった。The initial activation process currently performed is a process of discharging after a long time charging with a low current (charging for 15 to 20 hours and discharging for several hours) until a predetermined discharge capacity is obtained. This is done by repeating several times. For this reason, it was necessary to repeat charging and discharging in the factory for several days as an initial activation process from the time the battery was assembled to the time it was shipped.
【0006】この問題点を解決するために、特開平3−
219036号公報には、水素吸蔵合金中にホウ素を添加する
ことで粉化し易いホウ素リッチ相を生成させ、粉化によ
る比表面積の増加により初期の活性化効率を向上させる
ことが提案されている。しかし、この方法では、生成し
たホウ素リッチ相が可逆的に水素吸収・放出する量は少
なく、合金全体としては水素吸蔵量、従って放電容量が
低下する。しかも、粉化が進みすぎて電極としての集電
性が低下し、早期に放電容量が劣化する。In order to solve this problem, Japanese Patent Laid-Open No.
Japanese Patent No. 219036 proposes that boron is added to a hydrogen storage alloy to generate a boron-rich phase that is easily pulverized and the specific surface area is increased by the pulverization to improve the initial activation efficiency. However, in this method, the amount of the generated boron-rich phase that reversibly absorbs and releases hydrogen is small, and the hydrogen storage amount and therefore the discharge capacity of the entire alloy decreases. Moreover, pulverization progresses too much to reduce the current collecting ability as an electrode, and the discharge capacity deteriorates at an early stage.
【0007】特開平4−179055号公報には、水素吸蔵合
金粉末を所定濃度範囲の酸性水溶液中に所定時間浸漬し
た後、水洗すると、酸化物層や水酸化物層を除去するこ
とができ、その水素吸蔵合金粉末で電極を作製すると、
電極の活性化サイクルの短縮が図れ、電極利用率とサイ
クル寿命が向上することが報告されている。[0007] In Japanese Patent Laid-Open No. 4-179055, an oxide layer or a hydroxide layer can be removed by immersing the hydrogen-absorbing alloy powder in an acidic aqueous solution having a predetermined concentration range for a predetermined time and then washing with water. When an electrode is made from the hydrogen storage alloy powder,
It has been reported that the activation cycle of the electrode can be shortened and the electrode utilization rate and the cycle life can be improved.
【0008】また、本発明者らは、特開平6−223827号
公報に、急冷凝固法で微細結晶粒とした水素吸蔵合金粉
末を酸性水溶液中で処理して表面酸化膜を除去すると、
より高活性の水素吸蔵合金粉末が製造されることを報告
した。Further, the inventors of the present invention disclosed in Japanese Unexamined Patent Publication No. 6-223827 that a hydrogen storage alloy powder formed into fine crystal grains by a rapid solidification method is treated in an acidic aqueous solution to remove a surface oxide film.
It was reported that a more active hydrogen storage alloy powder was produced.
【0009】[0009]
【発明が解決しようとする課題】しかし、水素吸蔵合金
粉末の表面酸化膜を強い酸性水溶液を用いて化学的に除
去すると、合金表面により多くのNi(OH)2 が生成する。
表面にNi(OH)2 が付着した水素吸蔵合金粉末を負極の活
物質に用いたNi−水素電池は、高温における自己放電が
大きい。これは、Ni(OH)2 のOH- イオンが負極の放電反
応に関与する物質であり、負極の合金表面にNi(OH)2 が
存在すると、これから高温でOH- イオンが遊離し、負極
放電反応 (MHx + x OH- → M + x H2O + x e- ) が起こ
って、水素を消費しつつ自己放電反応が進行するからで
ある。従って、水素吸蔵合金粉末の表面にNi(OH)2 が生
成しないような処理方法が望ましい。However, when the surface oxide film of the hydrogen storage alloy powder is chemically removed using a strong acidic aqueous solution, more Ni (OH) 2 is produced on the alloy surface.
A Ni-hydrogen battery using a hydrogen storage alloy powder having Ni (OH) 2 adhered on its surface as an active material of a negative electrode has a large self-discharge at high temperature. This is a substance in which the OH − ions of Ni (OH) 2 are involved in the discharge reaction of the negative electrode, and when Ni (OH) 2 is present on the alloy surface of the negative electrode, OH − ions are liberated from this at high temperature and the negative electrode discharge occurs. reaction (MH x + x OH - → M + x H 2 O + xe -) happening, because self-discharge reaction proceeds while consuming hydrogen. Therefore, a treatment method that does not generate Ni (OH) 2 on the surface of the hydrogen storage alloy powder is desirable.
【0010】急冷凝固法では、例えば、ロール急冷法で
得た合金薄片を粉砕する、或いは合金の溶湯から直接ア
トマイズ法により粉末を得る、といった方法により水素
吸蔵合金粉末を得る。溶湯から凝固する際の形態が、薄
片や粉末といった表面積の大きい形態であるため、凝固
中に合金表面に酸化膜が多く生成する。また、得られた
水素吸蔵合金粉末は、急冷歪みを除去または緩和する
(放電容量の増大につながる) ため、製造後に熱処理す
ることが多いが、この熱処理中にも粉末表面に酸化膜が
生成する。In the rapid solidification method, for example, a hydrogen absorbing alloy powder is obtained by a method of crushing alloy flakes obtained by the roll rapid cooling method or directly obtaining a powder from a molten alloy by an atomizing method. Since the form when solidifying from the molten metal is a form with a large surface area such as flakes and powder, many oxide films are formed on the alloy surface during solidification. Further, the obtained hydrogen storage alloy powder removes or alleviates quenching strain.
Since this leads to an increase in discharge capacity, heat treatment is often performed after manufacturing, but an oxide film is formed on the powder surface during this heat treatment.
【0011】急冷凝固法で水素吸蔵合金粉末を製造する
場合、アトマイズ法のように粉砕がほとんど必要ない
か、あるいはロール急冷法でも粉砕はインゴット法に比
べれば非常に少なくてすむ。そのため、粉砕で新たに現
れる合金表面の割合が少なく、凝固中または熱処理中に
生じた酸化膜が合金粉末の表面に残存する割合が、イン
ゴット法で得られた粉末に比べて非常に多くなる。When the hydrogen storage alloy powder is produced by the rapid solidification method, pulverization is hardly required as in the atomizing method, or even by the roll rapid cooling method, the pulverization is much less than that of the ingot method. Therefore, the proportion of the alloy surface newly appearing by pulverization is small, and the proportion of the oxide film generated during solidification or heat treatment remaining on the surface of the alloy powder is much higher than that of the powder obtained by the ingot method.
【0012】従って、急冷凝固法で得られた合金粉末
は、表面に存在する酸化膜の多くが、凝固中または熱処
理中に生じた強固な酸化膜となる。この強固な表面酸化
膜は、特開平6−223827号公報に提案されているよう
に、高濃度の酸性水溶液で処理すると除去できるが、こ
の処理中に粉末表面に多くのNi(OH)2 が生成し、前述し
たように高温での自己放電が顕著になり、電極寿命 (保
存容量) が低下する。Therefore, in the alloy powder obtained by the rapid solidification method, most of the oxide film existing on the surface becomes a strong oxide film generated during solidification or heat treatment. This strong surface oxide film can be removed by treatment with a high-concentration acidic aqueous solution as proposed in Japanese Patent Laid-Open No. 6-223827, but a large amount of Ni (OH) 2 is formed on the powder surface during this treatment. As described above, the self-discharge at a high temperature becomes remarkable and the electrode life (storage capacity) is reduced.
【0013】これに対し、インゴット法では、粉末表面
のほとんどが、粉砕で新たに生じた表面である。粉砕中
にも表面酸化膜は生成するが、生成の程度が小さいた
め、インゴット法で製造した水素吸蔵合金粉末の表面の
酸化膜のほとんどは、粉砕で生成した弱い酸化膜であっ
て、除去が容易である。On the other hand, in the ingot method, most of the powder surface is the surface newly formed by pulverization. Although a surface oxide film is formed even during pulverization, since the degree of formation is small, most of the oxide film on the surface of the hydrogen storage alloy powder produced by the ingot method is a weak oxide film produced by pulverization and cannot be removed. It's easy.
【0014】特開平5−195007号公報には、表面に緻密
な酸化皮膜が生成した場合、アルカリ水溶液中での超音
波処理が合金活性の向上に効果的であることが記載され
ている。しかし、この処理方法は、粉砕時に粉末表面に
生成した酸化膜に対しては有効であっても、急冷凝固法
で得られた粉末のように、溶湯からの凝固時または熱処
理に生じた強固な酸化膜が粉末表面に多く存在する場合
には、十分な効果が得られないことが判明した。JP-A-5-195007 describes that when a dense oxide film is formed on the surface, ultrasonic treatment in an alkaline aqueous solution is effective for improving the alloy activity. However, even though this treatment method is effective for the oxide film formed on the powder surface during pulverization, it does not give a strong solidification that occurs during solidification from the molten metal or during heat treatment like the powder obtained by the rapid solidification method. It was found that a sufficient effect could not be obtained when many oxide films were present on the powder surface.
【0015】本発明の目的は、急冷凝固法で製造された
水素吸蔵合金粉末に見られるような強固な酸化膜を除去
することができ、しかも合金表面のNi(OH)2 の生成 (即
ち、酸素濃度増加) が抑制された、Ni−水素電池の初期
活性と電極寿命の一層の向上を実現することが可能な水
素吸蔵合金粉末の処理方法を提供することである。The object of the present invention is to remove the strong oxide film found in the hydrogen storage alloy powder produced by the rapid solidification method, and to produce Ni (OH) 2 on the alloy surface (that is, It is an object of the present invention to provide a method for treating a hydrogen storage alloy powder, which can suppress the increase in oxygen concentration) and can further improve the initial activity and the electrode life of a Ni-hydrogen battery.
【0016】[0016]
【課題を解決するための手段】本発明者らは、上記目的
を達成すべく検討した結果、酸処理と超音波処理とを併
用することにより、比較的低濃度の酸水溶液で水素吸蔵
合金粉末の表面の強固な酸化膜を除去することができ、
しかも超音波の併用によってNi(OH)2 の生成が著しく抑
制され、高温自己放電の低減により電極寿命が改善され
ることを見出し、本発明に到達した。Means for Solving the Problems As a result of studies to achieve the above object, the inventors of the present invention have found that a combination of acid treatment and ultrasonic treatment can be used to produce a hydrogen storage alloy powder in a relatively low concentration aqueous acid solution. The strong oxide film on the surface of can be removed,
Moreover, the inventors have found that the combined use of ultrasonic waves significantly suppresses the generation of Ni (OH) 2 , and that the high temperature self-discharge is reduced to improve the electrode life.
【0017】ここに、本発明は、粉末表面の20%以上の
面積が合金の凝固中または熱処理中に生成した酸化膜で
ある水素吸蔵合金粉末を、非酸化性の酸性水溶液中に浸
漬し、かつ20〜100 kHz の周波数の超音波を作用させる
ことを特徴とする水素吸蔵合金粉末の処理方法である。According to the present invention, the hydrogen storage alloy powder, which is an oxide film having an area of 20% or more of the powder surface formed during solidification or heat treatment of the alloy, is immersed in a non-oxidizing acidic aqueous solution. In addition, it is a method for treating a hydrogen storage alloy powder, which is characterized in that an ultrasonic wave having a frequency of 20 to 100 kHz is applied.
【0018】本発明により処理する水素吸蔵合金粉末
は、粉末表面の20%以上の面積が合金の凝固中または熱
処理中に高温で生成した強固な酸化膜で覆われているも
のである。このような粉末の例は、前述したように、急
冷凝固法で製造され、場合によりさらに熱処理が施され
た水素吸蔵合金粉末である。The hydrogen storage alloy powder treated according to the present invention is such that 20% or more of the surface of the powder is covered with a strong oxide film formed at high temperature during solidification or heat treatment of the alloy. An example of such a powder is the hydrogen storage alloy powder produced by the rapid solidification method and optionally further heat-treated as described above.
【0019】水素吸蔵合金の初期活性 (即ち、Ni−水素
電池の初期活性化の容易さ) は、合金表面の酸化状況と
水素吸蔵合金のバルク組織の両因子により変化する。具
体的には、初期活性に影響する主要な現象は、合金表
面の酸化膜による電極反応活性度の低下現象、および
充電・放電サイクル初期の水素吸収・放出時の体積変化
によって粒界を起点とした破砕が生じ、比表面積が増加
して初期活性度が向上する現象、の二つである。The initial activity of the hydrogen storage alloy (that is, the ease of initial activation of the Ni-hydrogen battery) depends on both the oxidation state of the alloy surface and the bulk structure of the hydrogen storage alloy. Specifically, the main phenomena that affect the initial activity are the origin of the grain boundary due to the phenomenon of the decrease in the electrode reaction activity due to the oxide film on the alloy surface, and the volume change at the time of hydrogen absorption / desorption at the beginning of the charge / discharge cycle. The crushing occurs, the specific surface area increases, and the initial activity improves.
【0020】特開平4−179055号公報に記載のように、
単に溶製した合金を粉砕して得た水素吸蔵合金粉末を酸
性水溶液に浸漬する場合は、上記により合金表面の酸
化膜が除去できた分だけ初期活性度が向上するが、上記
による合金バルク組織に起因する初期活性度の向上は
期待できない。As described in Japanese Patent Laid-Open No. 4-179055,
When the hydrogen-absorbing alloy powder obtained by simply crushing the melted alloy is immersed in an acidic aqueous solution, the initial activity is improved by the amount by which the oxide film on the alloy surface can be removed by the above, but the alloy bulk structure according to the above It cannot be expected to improve the initial activity due to.
【0021】これに対し、水素吸蔵合金粉末を急冷凝固
法で製造すると、結晶粒が微細 (望ましくは30μm以
下) となり、結晶粒界部分が多い組織であることから、
の面酸化膜除去に加えて、のサイクル初期の粒界起
点の破砕、表面積増加による初期活性化への相乗効果が
得られるため、初期活性度の向上効果が大きくなる。On the other hand, when the hydrogen-absorbing alloy powder is manufactured by the rapid solidification method, the crystal grains become fine (preferably 30 μm or less) and the structure has many crystal grain boundary portions.
In addition to the removal of the surface oxide film of (1), the effect of crushing the grain boundary starting point in the initial cycle of (1) and the synergistic effect on the initial activation by increasing the surface area can be obtained, so that the effect of improving the initial activity becomes large.
【0022】また、通常の凝固冷却速度で得られた合金
(結晶粒径≧80〜100 μm) は、粉砕工程で多くの結晶
粒が破砕されるため、個々の結晶単位が破壊される結
果、電極にした際の寿命が短くなる傾向がある。急冷凝
固法、特にアトマイズ法により結晶粒径が微細な合金を
粉砕せずに製造した後、酸性水溶液中で表面酸化膜を除
去すると、破壊されずに残存している結晶単位の割合が
多くなることと、急冷のために成分偏析が少なく均質な
組織が得られることが相まって、電極寿命が長くなる。Further, an alloy obtained at a normal solidification cooling rate
(Crystal grain size ≧ 80 to 100 μm), many crystal grains are crushed in the crushing process, and as a result, individual crystal units are destroyed, so that the life of the electrode tends to be shortened. If the surface oxide film is removed in an acidic aqueous solution after manufacturing an alloy with a fine grain size without crushing by a rapid solidification method, especially an atomizing method, the proportion of crystal units remaining without being destroyed increases. In addition, because of the rapid cooling, a uniform structure with less component segregation can be obtained, and the life of the electrode is extended.
【0023】しかし、急冷凝固中および熱処理中に生成
した強固な酸化膜を除去するには、強い (高濃度の) 酸
性水溶液で処理することが必要と考えられてきた。強い
酸性水溶液で処理すると、前述したように、合金表面に
多くのNi(OH)2 が生成し、これがNi−水素電池の高温で
の自己放電特性を悪化させる原因となり、電極寿命の延
長を阻んでいた。However, it has been considered necessary to treat with a strong (high-concentration) acidic aqueous solution in order to remove the strong oxide film formed during the rapid solidification and the heat treatment. When treated with a strong acidic aqueous solution, as described above, a large amount of Ni (OH) 2 is produced on the alloy surface, which causes deterioration of the self-discharge characteristics of Ni-hydrogen battery at high temperature and prevents extension of the electrode life. I was there.
【0024】本発明によれば、超音波処理を併用するこ
とで、比較的低濃度の酸水溶液で水素吸蔵合金粉末の表
面の強固な酸化膜を除去することができ、低い酸濃度と
超音波の効果によって合金表面のNi(OH)2 の生成が抑え
られ、高温での自己放電特性が良好に保持され、電極寿
命が延びる。According to the present invention, a strong oxide film on the surface of the hydrogen-absorbing alloy powder can be removed with an aqueous acid solution having a relatively low concentration by using the ultrasonic treatment together. By this effect, generation of Ni (OH) 2 on the alloy surface is suppressed, good self-discharge characteristics at high temperature are maintained, and the electrode life is extended.
【0025】[0025]
【発明の実施の形態】本発明で処理する水素吸蔵合金
は、Niを含有しているものであれば特に制限されない。
代表例は、AB5 型またはAB2 型の水素吸蔵合金であ
るが、AB型またはA2 B型の水素吸蔵合金でもよい。BEST MODE FOR CARRYING OUT THE INVENTION The hydrogen storage alloy treated in the present invention is not particularly limited as long as it contains Ni.
A typical example is an AB 5 type or AB 2 type hydrogen storage alloy, but an AB type or A 2 B type hydrogen storage alloy may be used.
【0026】合金の具体的組成も特に制限されないが、
AB5 型合金の例は、LaNix またはMmNix (xは 4.7〜5.
2)を基本構造とし、Niの一部をCo、Mn、Al、Fe、Cr、C
u、V、Be、Zr、Ti、Mo等の1種または2種以上の元素
で置換したものである。LaNixは高価格である上、寿命
低下が早いので、実用的にはMmNix が好ましい。The specific composition of the alloy is not particularly limited, either.
Examples of AB 5 type alloys are LaNi x or MmNi x, where x is 4.7-5.
2) as a basic structure, with some of Ni as Co, Mn, Al, Fe, Cr, C
It is substituted with one or more elements such as u, V, Be, Zr, Ti and Mo. LaNi x is on a high price, since reduction in life is fast, the practical MmNi x preferred.
【0027】AB2 型合金の例は、ZrNiy (yは 1.9〜2.
25) を基本構造とし、Niの一部をV、Mn、Cr、Co、Fe、
Al、Mo、Cu、Be等の1種または2種以上の元素で置換し
たものである。具体例として Zr1.0V0.4Ni1.6, Zr1.0M
n0.6Cr0.2Ni1.2, Zr1.0Ni1.2Mn0.6V0.2Co0.1, Zr1.0Ni
1.2Mn0.6V0.2Fe0.1, Zr1.0V0.4Ni1.6等がある。An example of an AB 2 type alloy is ZrNi y (y is 1.9 to 2.
25) is a basic structure, and a part of Ni is V, Mn, Cr, Co, Fe,
It is substituted with one or more elements such as Al, Mo, Cu and Be. As a specific example, Zr 1.0 V 0.4 Ni 1.6 , Zr 1.0 M
n 0.6 Cr 0.2 Ni 1.2 , Zr 1.0 Ni 1.2 Mn 0.6 V 0.2 Co 0.1 , Zr 1.0 Ni
1.2 Mn 0.6 V 0.2 Fe 0.1 , Zr 1.0 V 0.4 Ni 1.6 etc.
【0028】本発明で処理する水素吸蔵合金粉末は、粉
末表面の20%以上の面積が合金の凝固中または熱処理中
に生成した酸化膜で覆われているものである。前述した
ように、急冷凝固法で製造した水素吸蔵合金粉末にこの
条件を満たすものが多いが、本発明で処理する水素吸蔵
合金粉末は急冷凝固法で製造されたものに限定されるわ
けではない。The hydrogen storage alloy powder treated in the present invention is such that 20% or more of the surface of the powder is covered with an oxide film formed during solidification or heat treatment of the alloy. As described above, many hydrogen storage alloy powders manufactured by the rapid solidification method satisfy this condition, but the hydrogen storage alloy powders treated in the present invention are not limited to those manufactured by the rapid solidification method. .
【0029】急冷凝固法では、溶融状態から50℃/秒以
上、好ましくは500 ℃/秒以上の速い冷却速度で凝固さ
れるため、得られた水素吸蔵合金粉末は成分偏析が少な
く、耐食性が良好で、繰り返し充電・放電に伴う容量低
下が非常に少なく、電極寿命が長いという特長がある。In the rapid solidification method, since the solidified product is solidified from the molten state at a high cooling rate of 50 ° C./sec or more, preferably 500 ° C./sec or more, the obtained hydrogen storage alloy powder has little component segregation and good corrosion resistance. Therefore, there is a feature that the capacity decrease due to repeated charging and discharging is very small and the electrode life is long.
【0030】急冷凝固法としては、例えば、回転電極
法、回転ドラム上への注湯による急冷、水冷鋼板上に薄
く鋳込む方法、ガスアトマイズ法などを採用することが
できる。このうち、球形の合金粉末を直接得ることがで
きるガスアトマイズ法が好ましい。ガスアトマイズ法に
よれば、電極製作時の合金の粉砕工程が必ずしも必要と
はならず、しかも合金が球形粉末状であるので、電極構
成時に合金粒子が最密充填されて高容量の電極を得るこ
とができるからである。As the rapid solidification method, for example, a rotating electrode method, rapid cooling by pouring on a rotating drum, thin casting on a water-cooled steel sheet, gas atomizing method, etc. can be adopted. Of these, the gas atomization method is preferable because it can directly obtain spherical alloy powder. According to the gas atomizing method, the crushing process of the alloy at the time of manufacturing the electrode is not always necessary, and since the alloy is a spherical powder, it is possible to obtain the high capacity electrode by the closest packing of the alloy particles at the time of forming the electrode. Because you can
【0031】好ましくは、急冷凝固後で、酸性水溶液に
よる処理前に、水素吸蔵合金粉末を550〜950 ℃で2〜
5時間の熱処理を受けさせる。それにより合金が再結晶
し、急冷歪が除去されて、放電容量が向上する。この熱
処理は一般に真空中または不活性雰囲気中で行う。好ま
しい熱処理条件は、 750〜900 ℃で3〜4時間、さらに
好ましくは 750〜800 ℃で4時間である。熱処理雰囲気
は、表面酸化防止の観点から真空より不活性雰囲気
(例、アルゴン、ヘリウム) の方が好ましい。Preferably, the hydrogen storage alloy powder is heated at 550 to 950 ° C. for 2 to 2 after the rapid solidification and before the treatment with the acidic aqueous solution.
Heat treatment for 5 hours. As a result, the alloy is recrystallized, quenching strain is removed, and the discharge capacity is improved. This heat treatment is generally performed in vacuum or in an inert atmosphere. Preferred heat treatment conditions are 750 to 900 ° C. for 3 to 4 hours, and more preferably 750 to 800 ° C. for 4 hours. The heat treatment atmosphere is more inert than vacuum from the viewpoint of preventing surface oxidation.
(Eg argon, helium) is preferred.
【0032】製造された水素吸蔵合金が粉末状でない場
合には、本発明の処理を行う前に合金を粉砕しておく。
粉砕が後になると、粉砕時に合金表面に酸化膜が生成し
て、初期活性化特性が劣化するからである。If the hydrogen storage alloy produced is not in powder form, the alloy is ground before the treatment according to the invention.
This is because when the pulverization is performed later, an oxide film is formed on the alloy surface during the pulverization and the initial activation characteristics are deteriorated.
【0033】こうして製造された水素吸蔵合金粉末は表
面が酸化膜で覆われている。例えば、水素吸蔵合金粉末
をガスアトマイズ法で製造した場合、ガスアトマイズの
過程でガスに含まれる微量の酸素あるいはアトマイズチ
ャンバー内の残留酸素分などの影響による酸化、さらに
は合金製造後の熱処理過程において熱処理炉内不活性ガ
ス中に含まれる微量の酸素による酸化が原因で、表面に
酸化膜が生成する。The surface of the hydrogen storage alloy powder produced in this manner is covered with an oxide film. For example, when hydrogen-absorbing alloy powder is manufactured by the gas atomizing method, oxidation is caused by the influence of a trace amount of oxygen contained in the gas in the gas atomizing process or the residual oxygen content in the atomizing chamber, and further in the heat treatment furnace in the heat treatment process after alloy production. An oxide film is formed on the surface due to the oxidation caused by a trace amount of oxygen contained in the inert gas.
【0034】水素吸蔵合金粉末を他の方法で製造した場
合にも、合金製造過程や熱処理過程(熱処理を行った場
合) 、さらには合金粉砕過程において酸化を完全に避け
ることはできず、やはり表面酸化膜が生成する。Even when the hydrogen-absorbing alloy powder is manufactured by another method, oxidation cannot be completely avoided during the alloy manufacturing process, the heat treatment process (when heat treatment is performed), and further during the alloy crushing process. An oxide film is formed.
【0035】酸化膜のうち高温で生成したもの、すなわ
ち、溶湯からの凝固中または合金の熱処理中に生じた酸
化膜は、特に強固で、表面処理による除去が困難であ
り、酸処理だけで除去しようとすると、高濃度の酸水溶
液が必要となる。本発明では、酸処理と超音波処理とを
併用することで、比較的低濃度の酸水溶液で、このよう
な強固な酸化膜を除去できる。表面処理にアルカリ水溶
液を使用した場合には、超音波を併用しても、高温で生
成した強固な酸化膜は効率的に除去できない。The oxide film formed at a high temperature among the oxide films, that is, the oxide film formed during solidification from the molten metal or during the heat treatment of the alloy is particularly strong and difficult to remove by surface treatment, and is removed only by acid treatment. Attempts to do so require a highly concentrated aqueous acid solution. In the present invention, by using the acid treatment and the ultrasonic treatment together, such a strong oxide film can be removed with an acid aqueous solution having a relatively low concentration. When an alkaline aqueous solution is used for the surface treatment, the strong oxide film formed at high temperature cannot be efficiently removed even if ultrasonic waves are used together.
【0036】本発明で処理するのは、凝固中または熱処
理中に高温で生成した、強固で除去しにくい酸化膜が、
表面の20%以上の面積を占める水素吸蔵合金粉末であ
る。凝固中または熱処理中に生成した酸化膜の割合 (面
積率) は、熱処理後 (熱処理しない場合は凝固後) の合
金の表面積(A) と、粉砕後の合金の表面積(B) とから、
(A)/(B) ×100 により算出することができる。The treatment of the present invention is to remove a strong and hard-to-remove oxide film formed at high temperature during solidification or heat treatment.
It is a hydrogen storage alloy powder that occupies 20% or more of the surface area. The ratio (area ratio) of the oxide film formed during solidification or heat treatment is calculated from the surface area (A) of the alloy after heat treatment (after solidification if not heat treated) and the surface area (B) of the alloy after pulverization.
It can be calculated by (A) / (B) × 100.
【0037】例えば、アトマイズ法で製造した、粉砕し
ていない水素吸蔵合金粉末の場合には、凝固中または熱
処理中に生成した酸化膜の割合は100 %となる。急冷凝
固法で製造しても、粉砕の程度が大きかった場合には、
凝固中または熱処理中に高温で生成した酸化膜の割合が
20%未満となることもある。このように高温で生成した
強固な酸化膜の割合が粉末表面の20%未満である場合に
は、従来の方法でも十分に粉末表面の酸化膜を除去でき
る。For example, in the case of the non-pulverized hydrogen storage alloy powder produced by the atomization method, the ratio of the oxide film formed during solidification or heat treatment is 100%. Even if manufactured by the rapid solidification method, if the degree of crushing is large,
The percentage of oxide film formed at high temperature during solidification or heat treatment is
It may be less than 20%. When the ratio of the strong oxide film formed at a high temperature is less than 20% of the powder surface, the conventional method can sufficiently remove the oxide film on the powder surface.
【0038】本発明の処理に用いる酸は、塩酸および/
またはフッ化水素酸などの非酸化性の酸がよい。これ以
外の酸 (例、硝酸、硫酸等) では、酸の持つ酸化機能に
より酸性水溶液による浸漬処理中に合金表面に新たに酸
化膜が生じやすく、合金の初期活性化特性の改善効果が
充分には得られないからである。The acid used in the treatment of the present invention is hydrochloric acid and / or
Alternatively, a non-oxidizing acid such as hydrofluoric acid is preferable. With other acids (e.g. nitric acid, sulfuric acid, etc.), the oxidation function of the acid makes it easier for a new oxide film to form on the alloy surface during the immersion treatment in an acidic aqueous solution, and the effect of improving the initial activation characteristics of the alloy is not sufficient. Is not available.
【0039】処理に用いる酸性水溶液は、試薬特級もし
くは1級またはそれと同程度の濃度の原液 (塩酸は35〜
36%、フッ化水素酸は44〜46%濃度) を水で希釈するこ
とにより調製できる。酸性水溶液の酸濃度は、この原液
の含有量 (重量%) として、塩酸で0.5 〜5%、フッ化
水素酸で 0.5〜3%、塩酸とフッ化水素酸との混酸で0.
5〜5%の濃度が好ましい。より好ましい酸濃度は、塩
酸で 1.0〜2%、フッ化水素酸で 0.5〜1.0 %、塩酸と
フッ化水素酸の混酸で 0.5〜2.0 %である。The acidic aqueous solution used for the treatment is a special grade reagent or a first grade reagent or a stock solution having a concentration similar to that (35% for hydrochloric acid).
36%, hydrofluoric acid 44-46% concentration) can be prepared by diluting with water. The acid concentration of the acidic aqueous solution is 0.5 to 5% with hydrochloric acid, 0.5 to 3% with hydrofluoric acid, and 0. 0 with a mixed acid of hydrochloric acid and hydrofluoric acid as the content (% by weight) of this stock solution.
A concentration of 5-5% is preferred. More preferable acid concentrations are 1.0 to 2% for hydrochloric acid, 0.5 to 1.0% for hydrofluoric acid, and 0.5 to 2.0% for mixed acid of hydrochloric acid and hydrofluoric acid.
【0040】酸濃度が高すぎると、合金表面にNi(OH)2
が多量に生成し、高温での自己放電特性が悪化し易い。
しかし、酸濃度が高い場合には、処理時間を短くするこ
とでNi(OH)2 の生成を抑制し、本発明の効果を達成する
ことができるので、酸水溶液の濃度は特に制限されな
い。If the acid concentration is too high, the surface of the alloy will have Ni (OH) 2
Are generated in a large amount, and the self-discharge characteristics at high temperature are likely to deteriorate.
However, when the acid concentration is high, generation of Ni (OH) 2 can be suppressed by shortening the treatment time and the effect of the present invention can be achieved, so the concentration of the acid aqueous solution is not particularly limited.
【0041】酸性水溶液による好ましい処理時間を、濃
度別に下記に示す。ここに示した時間より長いと合金の
表面に多くのNi(OH)2 が生成し易くなる。 HCl: 0.5〜2.0 %濃度=10分以下、2.0 〜5.0 %濃度
=5分以下、 HF : 0.5〜1.0 %濃度= 5分以下、1.0 〜3.0 %濃度
=3分以下、 HCl+HF混酸: 0.5〜2.0 %濃度=10分以下、 2.0〜5.0
%濃度=5分以下。The preferable treatment time with the acidic aqueous solution is shown below for each concentration. If it is longer than the time shown here, a large amount of Ni (OH) 2 is likely to be formed on the surface of the alloy. HCl: 0.5 to 2.0% concentration = 10 minutes or less, 2.0 to 5.0% concentration = 5 minutes or less, HF: 0.5 to 1.0% concentration = 5 minutes or less, 1.0 to 3.0% concentration = 3 minutes or less, HCl + HF mixed acid: 0.5 to 2.0 % Concentration = 10 minutes or less, 2.0 to 5.0
% Concentration = 5 minutes or less.
【0042】酸処理の温度は0〜80℃の範囲内が好まし
い。0℃より低温では、酸濃度が低すぎる場合と同様、
酸洗反応の進行が遅く、表面酸化膜の十分な除去が困難
なことが多い。一方、処理温度が80℃を超えると、酸濃
度が高すぎる場合と同様、酸洗反応の進行が速すぎ、合
金表面の酸化膜の除去にとどまらず合金内部にまで酸洗
が進む傾向がある。さらに、80℃より高温では、水素吸
収平衡圧力の関係から、酸洗反応で発生した水素は合金
に吸収されないですべて大気中に放出されてしまい、活
性化の促進が不十分となることがある。The temperature of the acid treatment is preferably in the range of 0 to 80 ° C. At temperatures lower than 0 ° C, the same as when the acid concentration is too low,
The pickling reaction proceeds slowly, and it is often difficult to sufficiently remove the surface oxide film. On the other hand, if the treatment temperature exceeds 80 ° C, as in the case where the acid concentration is too high, the pickling reaction proceeds too fast, and the pickling tends not only to remove the oxide film on the alloy surface but also to the inside of the alloy. . Further, at a temperature higher than 80 ° C, due to the hydrogen absorption equilibrium pressure, the hydrogen generated in the pickling reaction may not be absorbed by the alloy and may be released into the atmosphere, resulting in insufficient promotion of activation. .
【0043】本発明においては、酸処理中に酸水溶液中
の水素吸蔵合金粉末に超音波を作用させる。ただし、超
音波処理は酸処理の後に行うこともできる。使用する超
音波は、通常の超音波洗浄に用いられている20〜100 kH
z の周波数を用いることで十分な効果が得られる。20 k
Hz未満では可聴音波であり表面の酸化膜除去の効果は少
ない。周波数が100 kHz を超える超音波は、表面の付着
物を除去する等の目的には効果が認められるが、合金表
面の酸化膜を除去するためには効果が少ない。好ましい
周波数は28〜80 kHzである。In the present invention, ultrasonic waves are applied to the hydrogen storage alloy powder in the aqueous acid solution during the acid treatment. However, the ultrasonic treatment can also be performed after the acid treatment. The ultrasonic wave used is 20 to 100 kH, which is used for normal ultrasonic cleaning.
A sufficient effect can be obtained by using the frequency of z. 20 k
Below Hz, it is an audible sound wave and the effect of removing the oxide film on the surface is small. Ultrasonic waves with a frequency above 100 kHz are effective for the purpose of removing deposits on the surface, but are less effective for removing the oxide film on the alloy surface. The preferred frequency is 28-80 kHz.
【0044】超音波と酸性水溶液による酸洗効果との相
互作用で、酸水溶液が比較的低濃度であっても、効率的
に水素吸蔵合金粉末の表面の強固な酸化膜を除去するこ
とが可能となる。本発明の方法で処理した水素吸蔵合金
粉末の表面にNi(OH)2 の生成が少ない理由は明確ではな
いが、酸水溶液の濃度の影響以外に、超音波を用いるこ
とで生成したNi(OH)2 が超音波エネルギーにより除去さ
れることも寄与しているのではないかと推定される。By the interaction between the ultrasonic waves and the pickling effect of the acidic aqueous solution, it is possible to efficiently remove the strong oxide film on the surface of the hydrogen storage alloy powder even when the acidic aqueous solution has a relatively low concentration. Becomes The reason why the generation of Ni (OH) 2 on the surface of the hydrogen storage alloy powder treated by the method of the present invention is small is not clear, but in addition to the effect of the concentration of the acid aqueous solution, Ni (OH) generated by using ultrasonic waves is used. It is presumed that the removal of 2 ) by ultrasonic energy also contributes.
【0045】超音波強度については、0.05 W/cm2以上の
超音波強度であることが望ましい。これ以下では表面の
酸化膜除去能力が小さく、表面改質効果が小さくなる。
望ましくは0.35 W/cm2以上の超音波強度であると、水中
でキャビテーションが生じて、より効率的に合金表面の
酸化物除去が可能となり、表面改質効果が大きい。The ultrasonic wave intensity is preferably 0.05 W / cm 2 or more. Below this, the ability to remove the oxide film on the surface is small, and the effect of surface modification is small.
Desirably, when the ultrasonic wave intensity is 0.35 W / cm 2 or more, cavitation occurs in water, and oxides on the alloy surface can be removed more efficiently, and the surface modification effect is large.
【0046】超音波は、酸水溶液中に水素吸蔵合金粉末
を浸漬している間ずっと作用させる必要はなく、浸漬中
の一部の時間だけでもよい。その場合には、浸漬中の後
半に超音波を作用させる方が好ましい。また、酸処理後
の水洗中に超音波をかけることでもいくらかの効果はあ
るが、酸処理中に超音波をかける方が好ましい。The ultrasonic waves do not have to be applied during the immersion of the hydrogen storage alloy powder in the aqueous acid solution, and may be applied only for a part of the immersion time. In that case, it is preferable to apply ultrasonic waves in the latter half of the immersion. Further, although there is some effect by applying ultrasonic waves during washing with water after the acid treatment, it is preferable to apply ultrasonic waves during the acid treatment.
【0047】酸性水溶液により処理した水素吸蔵合金
は、次いで水洗し、通常はその後に乾燥する。水洗は、
合金に付着した酸がほぼ完全に除去されるように実施す
ればよい。例えば、水洗前後液のpHの変化が小数点1
ケタ以下になるまで水洗することができる。The hydrogen storage alloy treated with the acidic aqueous solution is then washed with water and usually dried thereafter. Washing with water
It may be carried out so that the acid attached to the alloy is almost completely removed. For example, the decimal point is the change in pH of the solution before and after washing.
It can be washed with water until it becomes less than the digit.
【0048】上述したように、表面酸化膜は水素透過を
妨げるバリアーであるので、本発明に従って酸処理し、
この酸化膜を除去すると、水素吸蔵合金の活性発現に必
要な水素の吸収・放出が初期より容易に行われる。ま
た、酸処理中に水素が合金表面で発生し、酸化膜が除去
されてガスが透過し易くなった合金の内部に、この発生
した水素が吸収される。これらの作用があいまって、活
性化処理の初期から水素が合金内部に十分に吸収されて
活性化が速まり、初期活性化特性が著しく改善される。As described above, since the surface oxide film is a barrier that prevents hydrogen permeation, it is treated with an acid according to the present invention,
By removing this oxide film, the absorption and release of hydrogen necessary for the activation of the hydrogen storage alloy can be easily performed from the initial stage. Further, hydrogen is generated on the surface of the alloy during the acid treatment, and the generated hydrogen is absorbed inside the alloy from which the oxide film is removed and the gas easily permeates. Combined with these effects, hydrogen is sufficiently absorbed inside the alloy from the initial stage of the activation treatment, the activation is accelerated, and the initial activation characteristics are remarkably improved.
【0049】さらに、超音波処理を併用して酸処理する
ことで、酸処理中に合金表面に生成するNi(OH)2 の量が
著しく少なくなり、この水酸化物に起因する高温での自
己放電が抑制される結果、電極寿命が改善される。Furthermore, by performing the acid treatment together with the ultrasonic treatment, the amount of Ni (OH) 2 formed on the alloy surface during the acid treatment is remarkably reduced, and the self-treatment at high temperature due to the hydroxide is caused. As a result of suppressing the discharge, the electrode life is improved.
【0050】本発明の方法により表面処理した水素吸蔵
合金粉末から当業者に周知の方法で電極を製造し、Ni−
水素電池の負極として使用する。電極は、例えば、水素
吸蔵合金粉末を適当な結着剤 (ポリビニルアルコールな
どの樹脂) および水 (または他の液体) と混合してペー
スト状とし、ニッケル多孔体に充填して乾燥した後、所
望の電極形状に加圧成形することにより製造できる。An electrode was manufactured from the hydrogen-absorbing alloy powder surface-treated by the method of the present invention by a method well known to those skilled in the art.
Used as a negative electrode for hydrogen batteries. The electrode is formed, for example, by mixing hydrogen storage alloy powder with an appropriate binder (resin such as polyvinyl alcohol) and water (or other liquid) to form a paste, filling the nickel porous body and drying it, and then It can be manufactured by pressure forming into the electrode shape.
【0051】[0051]
【実施例】本発明の水素吸蔵合金粉末の処理方法の効果
を次の実施例により実証する。実施例中、%は特に指定
しない限り重量%である。また、処理に用いた酸性水溶
液の酸濃度は、前述した原液 [即ち、試薬特級の35%塩
酸(HCl) または46%フッ化水素酸(HF)] の含有量 (重量
%) である。EXAMPLES The effects of the hydrogen storage alloy powder processing method of the present invention will be demonstrated by the following examples. In Examples,% is% by weight unless otherwise specified. The acid concentration of the acidic aqueous solution used for the treatment is the content (% by weight) of the above-mentioned undiluted solution [that is, reagent grade 35% hydrochloric acid (HCl) or 46% hydrofluoric acid (HF)].
【0052】(製造例1)表1に示す組成のAB5 型ま
たはAB2 型合金の水素吸蔵合金粉末を以下に述べる方
法で製造した。(Production Example 1) Hydrogen storage alloy powder of AB 5 type or AB 2 type alloy having the composition shown in Table 1 was produced by the method described below.
【0053】[0053]
【表1】 [Table 1]
【0054】合金の製造に用いた原料は、純度99.9%の
フレーク状Ni、純度99.8%の電解Co、純度99.9%のショ
ット状Al、純度99.8%の板状電解Mn、Ni−56.9%V母合
金、純度99.5%以上のスポンジ状Zr、希土類金属純度が
99.8%以上のミッシュメタル(Mm) (La=28%、Ce=48
%、Nd=18%、Pr=6%) 、およびLa富化ミッシュメタ
ル(Lm) (La=58%、Ce=15%、Pr=7%、Nd=20%) で
あった。The raw materials used for the production of the alloy are flake Ni having a purity of 99.9%, electrolytic Co having a purity of 99.8%, shot Al having a purity of 99.9%, plate electrolytic Mn having a purity of 99.8%, and Ni-56.9% V mother. Alloy, sponge Zr with a purity of 99.5% or more, rare earth metal purity
99.8% or more of misch metal (Mm) (La = 28%, Ce = 48
%, Nd = 18%, Pr = 6%), and La-rich misch metal (Lm) (La = 58%, Ce = 15%, Pr = 7%, Nd = 20%).
【0055】これらの原料から、急冷凝固法である75 k
g/chのArガスアトマイズ法 (溶湯からの冷却速度1×10
3 〜1×104 ℃/秒) 、または厚み約500 μm(溶湯から
の冷却速度9×103 ℃/秒) もしくは約250 μm(同じく
3×103 ℃/秒) の薄片状に鋳込んだロール急冷法を採
用して、所定組成の水素吸蔵合金を作製した。さらに、
従来法である100 kg/ch のインゴット法 (溶湯からの冷
却速度1.0 ℃/sec) によっても、水素吸蔵合金粉末を作
製した。From these raw materials, a rapid solidification method of 75 k
g / ch Ar gas atomization method (cooling rate from molten metal 1 × 10
3 to 1 × 10 4 ℃ / sec) or about 500 μm in thickness (cooling rate from molten metal 9 × 10 3 ℃ / sec) or about 250 μm (also 3 × 10 3 deg / sec) A hydrogen storage alloy having a predetermined composition was produced by adopting a double roll quenching method. further,
Hydrogen storage alloy powder was also produced by the conventional 100 kg / ch ingot method (cooling rate from molten metal 1.0 ° C / sec).
【0056】得られた各水素吸蔵合金はすべて、純度9
9.99 %のArガスを用いたAr雰囲気中において所定条件
で熱処理した。インゴット法およびロール急冷法で作製
した水素吸蔵合金は、熱処理後にステンレス製のボール
ミルによりAr雰囲気下で機械的に粉砕して粉末にした。
アトマイズ法で得た粉末も含め、各水素吸蔵合金粉末を
−74μmに分級した。Each of the obtained hydrogen storage alloys had a purity of 9
The heat treatment was performed under a predetermined condition in an Ar atmosphere using 9.99% Ar gas. The hydrogen storage alloy produced by the ingot method and the roll quenching method was mechanically crushed into powder by a stainless ball mill in an Ar atmosphere after heat treatment.
Each hydrogen storage alloy powder including the powder obtained by the atomization method was classified to -74 μm.
【0057】得られた水素吸蔵合金粉末の表面酸化膜に
おける、凝固または熱処理中に高温で生成した酸化膜
(以下、高温酸化膜という) の割合を、粉砕前および粉
砕・分級後のBET法により測定した比表面積から求め
た。但し、アトマイズ法で製造した粉末は、粉砕工程を
経由していないため、高温酸化膜の割合は100 %とな
る。こうして求めた高温酸化膜の割合を、次の表2にま
とめて示す。In the surface oxide film of the obtained hydrogen storage alloy powder, an oxide film formed at high temperature during solidification or heat treatment
The ratio (hereinafter referred to as high temperature oxide film) was determined from the specific surface area measured by the BET method before pulverization and after pulverization / classification. However, since the powder produced by the atomization method does not go through the crushing process, the proportion of the high temperature oxide film is 100%. The proportion of the high temperature oxide film thus obtained is summarized in Table 2 below.
【0058】[0058]
【表2】 [Table 2]
【0059】表2からわかるように、急冷凝固法である
ロール急冷法で水素吸蔵合金を製造しても、薄片が500
μmと厚いと、粉砕で現れる表面が多くなって、高温酸
化膜の割合が20%未満となった。As can be seen from Table 2, even when the hydrogen storage alloy is manufactured by the roll quenching method, which is a rapid solidification method, the flakes show 500 pieces.
When the thickness is as thick as μm, the surface exposed by crushing increases and the ratio of the high temperature oxide film becomes less than 20%.
【0060】(実施例1)製造例1に記載したようにし
て、表2の (イ)〜(ニ) の各方法で製造したAB5型の水
素吸蔵合金種の粉末を、次の (A)〜(C) に示す従来技
術および本発明の各種方法で表面処理した。水素吸蔵合
金の製造後の熱処理は、いずれも 850℃×4時間の同一
条件とした。表面処理条件を次に説明する。(Example 1) As described in Production Example 1, the powder of the AB 5 type hydrogen storage alloy species produced by each of the methods (a) to (d) in Table 2 was prepared as follows. )-(C), and the surface treatment was carried out by the various methods of the present invention. The heat treatment after the hydrogen storage alloy was manufactured was the same under the same conditions of 850 ° C. × 4 hours. The surface treatment conditions will be described below.
【0061】(A) アルカリ処理+超音波 (特開平5−19
5007号) 合金粉末1kgに対して1リットルの割合の比重1.30のKO
H 水溶液中に合金粉末を浸漬し、液温を80℃に保ちなが
ら100 rpm で攪拌しつつ、液中に浸漬型超音波振動子を
設置して超音波 (周波数:26 kHz、出力:20 W/処理容
量1m3) を作用させながら、60分間のアルカリ処理を行
った。その後、アルカリ水溶液を除去し、合金粉末を洗
液のpHが9以下になるまで水洗し、真空雰囲気におい
て乾燥した。(A) Alkali treatment + ultrasonic wave (Japanese Patent Laid-Open No. 5-19
No. 5007) KO with a specific gravity of 1.30 at a ratio of 1 liter to 1 kg of alloy powder
Immerse the alloy powder in the H 2 aqueous solution and stir at 100 rpm while maintaining the liquid temperature at 80 ° C, and install an immersion ultrasonic transducer in the liquid to generate ultrasonic waves (frequency: 26 kHz, output: 20 W / Processing volume of 1 m 3 ) was applied and alkali treatment was carried out for 60 minutes. Then, the alkaline aqueous solution was removed, the alloy powder was washed with water until the pH of the washing liquid was 9 or less, and dried in a vacuum atmosphere.
【0062】(B) 高濃度酸性水溶液処理 (特開平6−22
3827号) 合金粉末1kgに対して2リットルの割合の7% HCl 水溶
液中に、液温30℃で合金粉末を8分間浸漬した。浸漬中
に処理液を100 rpm で攪拌したが、超音波は作用させな
かった。その後、酸性水溶液を除去し、重量で合金の20
倍量の水で洗浄し、真空雰囲気において乾燥した。(B) Treatment with high-concentration acidic aqueous solution (JP-A-6-22
(No. 3827) The alloy powder was immersed for 8 minutes at a liquid temperature of 30 ° C. in a 7% HCl aqueous solution in a ratio of 2 liters to 1 kg of the alloy powder. The treatment liquid was stirred at 100 rpm during the immersion, but no ultrasonic wave was applied. After that, the acidic aqueous solution is removed and the weight of the alloy is reduced to 20%.
It was washed with twice the amount of water and dried in a vacuum atmosphere.
【0063】(C) 低濃度酸処理+超音波 (本発明法) 合金粉末1kgに対して2リットルの割合の1% HCl 水溶
液中に、液温30℃で合金粉末を5分間浸漬した。浸漬中
に処理液を60 rpmで攪拌し、方法(A) と同様にして、周
波数48 kHz、強度0.50 W/cm2の超音波をかけた。その
後、酸性水溶液を除去し、重量で合金の20倍量の水で洗
浄し、真空雰囲気にて乾燥した。(C) Low-concentration acid treatment + ultrasonic wave (method of the present invention) The alloy powder was immersed for 5 minutes at a liquid temperature of 30 ° C. in a 1% HCl aqueous solution in a ratio of 2 liters to 1 kg of the alloy powder. The treatment liquid was stirred at 60 rpm during the immersion, and ultrasonic waves having a frequency of 48 kHz and an intensity of 0.50 W / cm 2 were applied in the same manner as in the method (A). After that, the acidic aqueous solution was removed, washed with 20 times the weight of water of the alloy, and dried in a vacuum atmosphere.
【0064】上記の(A) ないし(C) の方法で表面処理し
た水素吸蔵合金粉末、および未処理の水素吸蔵合金粉末
の電極特性を次のようにして試験した。その試験結果
を、表3にまとめて示す。The electrode characteristics of the hydrogen storage alloy powder surface-treated by the above methods (A) to (C) and the untreated hydrogen storage alloy powder were tested as follows. The test results are summarized in Table 3.
【0065】(試験方法)水素吸蔵合金粉末を、結着剤
(ポリビニルアルコール5%水溶液) を添加して混練し
た。得られた合金粉末のペーストをニッケル製発泡状金
属多孔体 (例、住友電工製セルメット) に充填し、乾燥
した後、1.5 ton/cm2 の圧力で加圧して合金粉末をNi多
孔体内に担持させ、電池の負極を構成した。この時の水
素吸蔵合金粉末の担持量は約12gであった。(Test method) Hydrogen storage alloy powder was used as a binder.
(Polyvinyl alcohol 5% aqueous solution) was added and kneaded. The obtained alloy powder paste is filled into a nickel foamed porous metal body (for example, Celmet manufactured by Sumitomo Electric), dried, and then pressed at a pressure of 1.5 ton / cm 2 to hold the alloy powder in the Ni porous body. Thus, a negative electrode of the battery was formed. At this time, the amount of the hydrogen storage alloy powder supported was about 12 g.
【0066】正極には市販の公称2000 mA のNi電極を用
い、正極と負極の間に6N-KOHのアルカリ電解液を含浸さ
せたナイロン不織布をセパレータとして挟み、公称20
00 mAのNi−水素二次電池を構成した。この電池
を単二型のケース内に密閉化し、試験に供する電池を得
た。この電池は負極の容量が大きい正極容量規制型の電
池である。A commercially available Ni electrode with a nominal value of 2000 mA was used as the positive electrode, and a nylon non-woven fabric impregnated with an alkaline electrolyte of 6N-KOH was sandwiched between the positive electrode and the negative electrode as a separator to give a nominal value of 20%.
A Ni-hydrogen secondary battery of 00 mA was constructed. This battery was hermetically sealed in a C / D type case to obtain a battery to be tested. This battery is a positive electrode capacity regulated battery having a large negative electrode capacity.
【0067】(1) 初期活性度 作製した正極容量規制型Ni−水素電池を、25℃、400 mA
で6時間充電した後、400 mAで端子電圧0.9 V まで放電
する繰り返し充電・放電を10回行った。1回目の放電容
量と10回目の放電容量を測定して、その比 (1回目放電
容量/10回目の放電容量×100 %) によって初期活性度
を求めた。初期活性度が95%以上であれば優れた初期活
性度を有すると評価できる。(1) Initial activity The prepared positive electrode capacity regulated Ni-hydrogen battery was tested at 25 ° C, 400 mA.
After charging for 6 hours at 400 mA, the battery was repeatedly charged and discharged 10 times by discharging at 400 mA to a terminal voltage of 0.9 V. The discharge capacity at the first time and the discharge capacity at the 10th time were measured, and the initial activity was determined by the ratio (1st discharge capacity / 10th discharge capacity × 100%). If the initial activity is 95% or more, it can be evaluated as having excellent initial activity.
【0068】(2) 高温自己放電特性 上記のNi−水素電池を25℃で上記と同じ充電・放電電流
量にて充電・放電を繰り返し、20サイクル目の完全充電
状態で一時試験を中断した。この電池を次いで50℃で10
日間保存し、その後25℃に戻して400 mAで放電し、残存
容量を測定した。この時の残存容量と19サイクル目 (25
℃) の放電容量との比 (保存容量または保存後の容量と
いう) を求めることにより、高温自己放電特性を評価し
た。この値が大きい程、高温での自己放電が少ない、自
己放電特性に優れた電池である。この値が85%以上であ
れば、自己放電量の少ない電池と評価できる。(2) High temperature self-discharge characteristics The above Ni-hydrogen battery was repeatedly charged and discharged at 25 ° C. with the same amount of charge and discharge current as described above, and the test was temporarily stopped in the fully charged state of the 20th cycle. This battery is then 10
It was stored for one day, then returned to 25 ° C., discharged at 400 mA, and the remaining capacity was measured. The remaining capacity at this time and the 19th cycle (25
The high-temperature self-discharge characteristics were evaluated by determining the ratio (° C) to the discharge capacity (called storage capacity or capacity after storage). The larger this value, the less self-discharge at high temperature, and the better the self-discharge characteristics of the battery. If this value is 85% or more, it can be evaluated as a battery with a small self-discharge amount.
【0069】[0069]
【表3】 [Table 3]
【0070】表3から、次の結果が判明した。 (i) 表面処理を行わないと、初期活性、保存容量とも目
標性能に達しない。 (ii)特開平5−195007号公報に記載された、アルカリ性
水溶液による処理と超音波処理の併用は、表面の高温酸
化膜の面積率が20%未満の水素吸蔵合金粉末には十分に
有効で、初期活性と保存容量が目標値に到達する。しか
し、高温酸化膜の面積率が20%以上の合金粉末では、酸
化膜を十分に除去できないため、初期活性の改善が不十
分である。From Table 3, the following results were found. (i) Without surface treatment, the initial performance and storage capacity do not reach the target performance. (ii) The combination of the treatment with the alkaline aqueous solution and the ultrasonic treatment described in JP-A-5-195007 is sufficiently effective for the hydrogen storage alloy powder having an area ratio of the high temperature oxide film on the surface of less than 20%. , Initial activity and storage capacity reach the target value. However, with an alloy powder having an area ratio of the high temperature oxide film of 20% or more, the oxide film cannot be sufficiently removed, so that the improvement of the initial activity is insufficient.
【0071】(iii) 特開平6−223827号公報に記載され
た、高濃度の酸性水溶液による表面処理では、表面の高
温酸化膜の面積率が20%以上の水素吸蔵合金粉末でも、
酸化膜を十分に除去でき、初期活性は目標値に達する
が、高温での自己放電が多くなり、保存容量が目標値よ
り低くなる。 (iv)本発明に従って、低濃度の酸性水溶液による処理と
超音波処理とを併用すると、初期活性、保存容量ともに
十分な改善効果が得られる。(Iii) In the surface treatment with the high-concentration acidic aqueous solution described in JP-A-6-223827, even if the hydrogen storage alloy powder has an area ratio of the high temperature oxide film of 20% or more,
Although the oxide film can be removed sufficiently and the initial activity reaches the target value, the self-discharge at high temperature increases and the storage capacity becomes lower than the target value. (iv) According to the present invention, when the treatment with the low-concentration acidic aqueous solution and the ultrasonic treatment are used together, sufficient improvement effects can be obtained in both initial activity and storage capacity.
【0072】(実施例2)製造例1に記載したようにし
て、表2の(イ)(インゴット法) 、(ハ)(250 μm厚のロー
ル急冷法) 、および(ニ)(ガスアトマイズ法) の各方法で
製造したAB5 型の水素吸蔵合金種またはAB2 型の
水素吸蔵合金種の合金粉末を表面処理に使用した。Example 2 As described in Production Example 1, (a) (ingot method), (c) (250 μm thick roll quenching method), and (d) (gas atomizing method) in Table 2 were performed. The alloy powder of the AB 5 type hydrogen storage alloy species or the AB 2 type hydrogen storage alloy species produced by each of the above methods was used for the surface treatment.
【0073】この水素吸蔵合金の合金作製後の熱処理条
件は表4に示す通りであった。表2にも示したように、
インゴット法 (ITと略記) で製造された合金粉末は表面
の高温酸化膜の面積率が20%未満であり、ロール急冷法
(RLと略記) およびガスアトマイズ法 (ATと略記) で製
造された合金粉末は表面の高温酸化膜の面積率が20%以
上であった。The heat treatment conditions of the hydrogen storage alloy after preparation were as shown in Table 4. As shown in Table 2,
The alloy powder manufactured by the ingot method (abbreviated as IT) has a high-temperature oxide film area ratio of less than 20% on the surface.
(Abbreviated as RL) and gas atomized method (abbreviated as AT) produced the alloy powder, and the area ratio of the high temperature oxide film on the surface was 20% or more.
【0074】各合金粉末を実施例1の表面処理方法(C)
と同様にして、酸処理と超音波処理とを併用して表面処
理した。試験No.1, 2 のインゴット材の粉末は、全く処
理を行わずに試験に供した。処理条件 (酸水溶液の原液
濃度、処理時間および温度、超音波の周波数と強度) を
表4にまとめて示す。処理中の液の攪拌速度は60 rpmで
あった。表面処理後、重量比で合金粉末の20倍量の水を
用いて水洗し、真空雰囲気にて乾燥した。表面処理した
水素吸蔵合金粉末の電極特性を実施例1と同様にして試
験した結果を、表4に併せて示す。Surface treatment method (C) of Example 1 for each alloy powder
In the same manner as above, the surface treatment was performed by using both acid treatment and ultrasonic treatment in combination. The powders of the ingot materials of Test Nos. 1 and 2 were subjected to the test without any treatment. Table 4 summarizes the treatment conditions (concentration of the acid aqueous solution, treatment time and temperature, ultrasonic frequency and intensity). The stirring speed of the liquid during the treatment was 60 rpm. After the surface treatment, the alloy powder was washed with water in an amount 20 times the weight of the alloy powder, and dried in a vacuum atmosphere. Table 4 also shows the results of testing the electrode characteristics of the surface-treated hydrogen storage alloy powder in the same manner as in Example 1.
【0075】[0075]
【表4−1】 [Table 4-1]
【0076】[0076]
【表4−2】 [Table 4-2]
【0077】熱処理条件や水素吸蔵合金種が変化して
も、本発明の処理方法により高温酸化膜を除去して初期
活性を十分に高めることができ、しかもその際にNi(OH)
2 の生成が少ないため、高温保存後の自己放電が抑制さ
れ、保存容量も十分に高い電池が得られることがわか
る。しかし、超音波の周波数が20 kHz未満または100 kH
z超では、表面改質効果が不十分で、初期活性が不芳と
なる。Even if the heat treatment conditions and the hydrogen storage alloy species change, the high temperature oxide film can be removed by the treatment method of the present invention to sufficiently enhance the initial activity, and at that time, Ni (OH) 2
It can be seen that since the amount of 2 generated is small, self-discharge after storage at high temperature is suppressed, and a battery having a sufficiently high storage capacity can be obtained. However, the ultrasonic frequency is less than 20 kHz or 100 kH
Above z, the surface modification effect is insufficient and the initial activity becomes poor.
【0078】[0078]
【発明の効果】本発明によれば、結晶粒が微細で初期活
性の改善が可能なアトマイズ法、ロール急冷法といった
急冷凝固法で製造された水素吸蔵合金粉末に見られるよ
うな、高温で生成した酸化膜が表面の20%以上を覆って
いる水素吸蔵合金粉末を表面処理して、Ni(OH)2 の生成
を抑制しながら、酸化膜を除去することができる。その
結果、本発明の方法により表面処理した水素吸蔵合金粉
末を負極活物質としてNi−水素電池を作製すると、初期
活性が高く、高温での保存容量、従って電極寿命も良好
なNi−水素電池が得られる。EFFECTS OF THE INVENTION According to the present invention, it is produced at a high temperature as seen in the hydrogen storage alloy powder produced by the rapid solidification method such as the atomizing method and the roll quenching method, which have fine crystal grains and can improve the initial activity. It is possible to remove the oxide film while suppressing the generation of Ni (OH) 2 by surface-treating the hydrogen-absorbing alloy powder whose oxide film covers 20% or more of the surface. As a result, when a Ni-hydrogen battery is produced by using the hydrogen storage alloy powder surface-treated by the method of the present invention as a negative electrode active material, the initial activity is high, the storage capacity at high temperature, and thus the electrode life is also good Ni-hydrogen battery. can get.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 竹下 幸輝 大阪市中央区北浜4丁目5番33号 住友金 属工業株式会社内 (72)発明者 神代 光一 大阪市中央区北浜4丁目5番33号 住友金 属工業株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Koki Takeshita 4-5-33 Kitahama, Chuo-ku, Osaka City Within Sumitomo Metal Industries, Ltd. (72) Inventor Koichi Jinshiro 4-5-33 Kitahama, Chuo-ku, Osaka City Sumitomo Metal Industries Co., Ltd.
Claims (1)
中または熱処理中に生成した酸化膜で覆われている水素
吸蔵合金粉末を、非酸化性の酸性水溶液中に浸漬し、か
つ20〜100 kHz の周波数の超音波を作用させることを特
徴とする水素吸蔵合金粉末の処理方法。1. A hydrogen storage alloy powder having an area of 20% or more of the surface of the powder covered with an oxide film formed during solidification or heat treatment of the alloy is immersed in a non-oxidizing acidic aqueous solution, and 20 A method for treating hydrogen-absorbing alloy powder, which comprises applying ultrasonic waves having a frequency of up to 100 kHz.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007308797A (en) * | 2006-05-18 | 2007-11-29 | Ranco Co Ltd | Method for regenerating metal powder |
KR20170115374A (en) * | 2016-04-07 | 2017-10-17 | 재단법인 포항산업과학연구원 | Method for manufacturing iron-based powders |
KR20170118302A (en) * | 2016-04-14 | 2017-10-25 | 재단법인 포항산업과학연구원 | Method for manufacturing high purity spherical titanium powder |
-
1996
- 1996-05-10 JP JP11676696A patent/JP3149783B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007308797A (en) * | 2006-05-18 | 2007-11-29 | Ranco Co Ltd | Method for regenerating metal powder |
JP4523617B2 (en) * | 2006-05-18 | 2010-08-11 | ランコ カンパニー リミテッド | Recycling method of metallic powder |
KR20170115374A (en) * | 2016-04-07 | 2017-10-17 | 재단법인 포항산업과학연구원 | Method for manufacturing iron-based powders |
KR20170118302A (en) * | 2016-04-14 | 2017-10-25 | 재단법인 포항산업과학연구원 | Method for manufacturing high purity spherical titanium powder |
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