JP3352479B2 - Hydrogen storage alloy electrode and method for producing the same - Google Patents
Hydrogen storage alloy electrode and method for producing the sameInfo
- Publication number
- JP3352479B2 JP3352479B2 JP29421692A JP29421692A JP3352479B2 JP 3352479 B2 JP3352479 B2 JP 3352479B2 JP 29421692 A JP29421692 A JP 29421692A JP 29421692 A JP29421692 A JP 29421692A JP 3352479 B2 JP3352479 B2 JP 3352479B2
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- Japan
- Prior art keywords
- alloy
- hydrogen storage
- electrode
- hydrogen
- storage alloy
- Prior art date
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- 239000000956 alloy Substances 0.000 title claims description 90
- 229910045601 alloy Inorganic materials 0.000 title claims description 89
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 80
- 239000001257 hydrogen Substances 0.000 title claims description 80
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 77
- 238000003860 storage Methods 0.000 title claims description 65
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000000203 mixture Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 10
- 229910001068 laves phase Inorganic materials 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- 229910052720 vanadium Inorganic materials 0.000 claims description 7
- 229910000905 alloy phase Inorganic materials 0.000 claims description 6
- 239000013078 crystal Substances 0.000 claims description 6
- 229910052750 molybdenum Inorganic materials 0.000 claims description 6
- 150000004678 hydrides Chemical class 0.000 claims description 5
- OWXLRKWPEIAGAT-UHFFFAOYSA-N [Mg].[Cu] Chemical compound [Mg].[Cu] OWXLRKWPEIAGAT-UHFFFAOYSA-N 0.000 claims description 4
- 239000012298 atmosphere Substances 0.000 claims description 4
- 229910052804 chromium Inorganic materials 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 3
- 238000013329 compounding Methods 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical group [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 37
- 238000007600 charging Methods 0.000 description 18
- 239000007789 gas Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 229910052793 cadmium Inorganic materials 0.000 description 3
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- -1 r and Ti Chemical class 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052987 metal hydride Inorganic materials 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229910000846 In alloy Inorganic materials 0.000 description 1
- 229910017706 MgZn Inorganic materials 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000018199 S phase Effects 0.000 description 1
- 229910004337 Ti-Ni Inorganic materials 0.000 description 1
- 229910011209 Ti—Ni Inorganic materials 0.000 description 1
- RZJQYRCNDBMIAG-UHFFFAOYSA-N [Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Zn].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn] Chemical class [Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Cu].[Zn].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Ag].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn].[Sn] RZJQYRCNDBMIAG-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000012300 argon atmosphere Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000006258 conductive agent Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 210000001787 dendrite Anatomy 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010325 electrochemical charging Methods 0.000 description 1
- 238000010326 electrochemical discharging Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- KHYBPSFKEHXSLX-UHFFFAOYSA-N iminotitanium Chemical compound [Ti]=N KHYBPSFKEHXSLX-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000004681 metal hydrides Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/383—Hydrogen absorbing alloys
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、電気化学的な水素の吸
蔵・放出を可逆的に行える水素吸蔵合金電極に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogen storage alloy electrode capable of electrochemically storing and releasing hydrogen.
【0002】[0002]
【従来の技術】各種の電源として広く使われている蓄電
池として鉛電池とアルカリ電池がある。このうちアルカ
リ蓄電池は高信頼性が期待でき、小形軽量化も可能など
の理由で小型電池は各種ポータブル機器用に、大型は産
業用として使われてきた。2. Description of the Related Art Lead-acid batteries and alkaline batteries have been widely used as various power supplies. Among them, the alkaline storage battery is expected to have high reliability, and the small battery has been used for various portable devices and the large battery has been used for industrial use for any reason that the size and weight can be reduced.
【0003】このアルカリ蓄電池において、正極として
は一部空気極や酸化銀極なども取り上げられているが、
ほとんどの場合ニッケル極である。ポケット式から焼結
式に代わって特性が向上し、さらに密閉化が可能になる
とともに用途も広がった。In this alkaline storage battery, an air electrode, a silver oxide electrode, and the like are partly taken up as a positive electrode.
In most cases it is a nickel electrode. The characteristics have been improved from the pocket type to the sintering type, and the sealing has been made possible and the use has expanded.
【0004】一方、負極としてはカドミウムの他に亜
鉛、鉄、水素などが対象となっているが、現在のところ
カドミウム極が主体である。ところが、一層の高エネル
ギー密度を達成するために金属水素化物つまり水素吸蔵
合金極を使ったニッケル−水素蓄電池が注目され、製法
などに多くの提案がされている。On the other hand, in addition to cadmium, zinc, iron, hydrogen and the like are targeted for the negative electrode. At present, cadmium electrodes are mainly used. However, a nickel-hydrogen storage battery using a metal hydride, that is, a hydrogen storage alloy electrode, has been attracting attention in order to achieve a higher energy density, and many proposals have been made for a manufacturing method and the like.
【0005】水素を可逆的に吸収・放出しうる水素吸蔵
合金を負極に使用するアルカリ蓄電池の水素吸蔵合金電
極は、理論容量密度がカドミウム極より大きく、亜鉛極
のような変形やデンドライトの形成などもないことか
ら、長寿命・無公害であり、しかも高エネルギー密度を
有するアルカリ蓄電池用負極として期待されている。[0005] A hydrogen storage alloy electrode of an alkaline storage battery using a hydrogen storage alloy capable of reversibly absorbing and releasing hydrogen as a negative electrode has a theoretical capacity density larger than that of a cadmium electrode, and causes deformation such as a zinc electrode and dendrite formation. Therefore, it is expected as a negative electrode for an alkaline storage battery having a long life, no pollution, and a high energy density.
【0006】このような水素吸蔵合金電極に用いられる
合金は、通常アーク溶解法や高周波誘導加熱溶解法など
で作製され、一般的にはTi−Ni系およびLa(また
はMm)−Ni系の多元系合金がよく知られている。T
i−Ni系の多元系合金は、ABタイプ(A:La,Z
r,Tiなどの水素との親和性の大きい元素、B:N
i,Mn,Crなどの遷移元素)として分類できるが、
この特徴として充放電サイクルの初期には比較的大きな
放電容量を示すが、充放電を繰り返すと、その容量を長
く維持することが困難であるという問題がある。また、
AB5 タイプのLa(またはMm)−Ni系の多元系合
金は、近年電極材料として多くの開発が進められ、特に
Mm−Ni系の多元系合金はすでに実用化されている
が、この合金系も比較的放電容量が小さいこと、電池電
極としての寿命性能が不十分であること、材料コストが
高いなどの問題を有している。したがって、さらに放電
容量が大きく長寿命である新規水素吸蔵合金材料が望ま
れている。[0006] The alloy used for such a hydrogen storage alloy electrode is usually produced by an arc melting method or a high-frequency induction heating melting method, and is generally a Ti-Ni-based or La (or Mm) -Ni-based multiple element. Series alloys are well known. T
i-Ni-based multi-component alloys are AB type (A: La, Z
elements having high affinity for hydrogen, such as r and Ti, B: N
i, Mn, Cr, etc.)
As a feature, although a relatively large discharge capacity is exhibited at the beginning of the charge / discharge cycle, there is a problem that it is difficult to maintain the capacity for a long time when charge / discharge is repeated. Also,
AB 5 type La (or Mm) -Ni system multi-alloy has recently extensively developed advanced as an electrode material, in particular Mm-Ni system multi-component alloys are already in practical use, this alloy system However, there are also problems such as a relatively small discharge capacity, insufficient life performance as a battery electrode, and a high material cost. Therefore, a new hydrogen storage alloy material having a larger discharge capacity and a longer life is desired.
【0007】これに対して、AB2 タイプのLaves
相合金は水素吸蔵能が比較的高く、高容量かつ長寿命の
電極として有望である。すでにこの合金系については、
例えばZrMoαNiβ系合金(特開昭64−4837
0号公報)やAxByNiz系合金(特開平1−102
855号公報)、ZrαMnβMoγCrδNiε(特
願平2−174741)などを提案している。[0007] On the other hand, AB 2 type Loves
Phase alloys have a relatively high hydrogen storage capacity and are promising as high capacity and long life electrodes. Already for this alloy system
For example, a ZrMoαNiβ-based alloy (JP-A-64-4837)
No. 0) and AxByNiz-based alloys (JP-A-1-102)
855), ZrαMnβMoγCrδNiε (Japanese Patent Application No. 2-174741).
【0008】[0008]
【発明が解決しようとする課題】しかしながら、AB2
タイプのLaves相合金を電極に用いた場合、Ti−
Ni系やLa(またはMm)−Ni系の多元系合金に比
べて放電容量が大きく、長寿命化が可能なものの、さら
に一層の性能の向上が望まれている。そして、合金系を
Zr−Mn−Mo−Cr−Ni系に限定し組成を調整す
ることにより、0.35Ah/g前後の放電容量を持つ
水素吸蔵合金電極が得られた(特願平2−174741
号)。また、Mn量をさらに増やしCr量を制限するこ
とにより合金の均質性が向上し、Moの一部をVで置換
することにより水素吸蔵−放出過程のヒステリシスが減
少し、放電容量がさらに増大した。However, AB 2
When a Laves phase alloy of the type is used for the electrode, Ti-
Although the discharge capacity is large and the life can be extended as compared with a Ni-based or La (or Mm) -Ni-based multi-component alloy, it is desired to further improve the performance. Then, by restricting the alloy system to the Zr-Mn-Mo-Cr-Ni system and adjusting the composition, a hydrogen storage alloy electrode having a discharge capacity of about 0.35 Ah / g was obtained (Japanese Patent Application No. Hei. 174741
issue). Further, the homogeneity of the alloy was improved by further increasing the amount of Mn and limiting the amount of Cr, and by substituting a part of Mo with V, the hysteresis in the hydrogen absorption-desorption process was reduced, and the discharge capacity was further increased. .
【0009】しかし、このような水素吸蔵合金電極を用
いてニッケル−水素蓄電池を構成した場合、急速充電時
の負極水素吸蔵合金の水素化熱等により蓄電池の温度が
高くなる。このため負極水素吸蔵合金の水素平衡圧力が
上昇し、電池内ガス圧が高くなり、液漏れや水素吸蔵量
が大きく低下するという問題があった。However, when a nickel-hydrogen storage battery is constructed using such a hydrogen storage alloy electrode, the temperature of the storage battery increases due to the heat of hydrogenation of the negative electrode hydrogen storage alloy during rapid charging. For this reason, there has been a problem that the hydrogen equilibrium pressure of the negative electrode hydrogen storage alloy increases, the gas pressure in the battery increases, and the liquid leakage and the hydrogen storage amount decrease significantly.
【0010】本発明は、上記従来の課題を解決するもの
であり、水素吸蔵合金を改善することにより、急速充電
時の高温状態(例えば80℃程度)においても電池内ガ
ス圧を低圧に保ち、液漏れを防止するとともに高容量の
水素吸蔵量を維持させることを目的とする。The present invention solves the above-mentioned conventional problems. By improving the hydrogen storage alloy, the gas pressure in the battery can be kept low even in a high temperature state (for example, about 80 ° C.) during rapid charging. An object of the present invention is to prevent liquid leakage and maintain a high capacity of hydrogen storage.
【0011】[0011]
【課題を解決するための手段】前記目的を達成するた
め、本発明の水素吸蔵合金電極は、一般式が、ZrMn
w Vb Mox Cry Niz (ただし、0.5<w≦0.
8,0<b<0.3,0<x<0.3,0<y≦0.
2,0.8≦z<1.2であり、かつ0.1≦b+x≦
0.3,2.0≦w+b+x+y+z≦2.4)で示さ
れ、合金相の主成分がC15(MgCu2 )型Lave
s相であり、かつその結晶格子定数(a)が、7.05
オングストローム≦a≦7.13オングストロームであ
る水素吸蔵合金またはその水素化物を用いるという構成
を備えたものである。In order to achieve the above object,
Therefore, the hydrogen storage alloy electrode of the present invention has a general formula: ZrMn
wVbMoxCryNiz(However, 0.5 <w ≦ 0.
8, 0 <b <0.3, 0 <x <0.3, 0 <y ≦ 0.
2, 0.8 ≦ z <1.2, and 0.1 ≦ b + x ≦
0.3, 2.0 ≦ w + b + x + y + z ≦ 2.4)
The main component of the alloy phase is C15 (MgCuTwo) Type Love
the s phase, and its crystal lattice constant (a) is 7.05
Angstrom ≦ a ≦ 7.13 angstroms
Using hydrogen storage alloy or its hydride
It is provided with.
【0012】前記構成においては、Cr、VおよびMo
の配合比率がy≦b+xであり、かつNi、VおよびM
oの配合比率がz−b−x≦1.2であることが好まし
い。次に本発明の水素吸蔵合金電極の製造方法は、一般
式が、ZrMnw Vb Mo x Cry Niz (ただし、
0.5<w≦0.8,0<b<0.3,0<x<0.
3,0<y≦0.2,0.8≦z<1.2であり、かつ
0.1≦b+x≦0.3,2.0≦w+b+x+y+z
≦2.4)で示され、合金相の主成分がC15(MgC
u2 )型Laves相であり、かつその結晶格子定数
(a)が、7.05オングストローム≦a≦7.13オ
ングストロームである水素吸蔵合金またはその水素化物
を、温度1000〜1300℃の範囲で、かつ真空中ま
たは不活性ガス雰囲気中で均質化熱処理を行なうという
構成を備えたものである。In the above structure, Cr, V and Mo
Is y ≦ b + x, and Ni, V and M
It is preferable that the compounding ratio of o is zbx ≦ 1.2.
No. Next, the method for producing a hydrogen storage alloy electrode of the present invention is generally
The formula is ZrMnwVbMo xCryNiz(However,
0.5 <w ≦ 0.8, 0 <b <0.3, 0 <x <0.
3,0 <y ≦ 0.2, 0.8 ≦ z <1.2, and
0.1 ≦ b + x ≦ 0.3, 2.0 ≦ w + b + x + y + z
≦ 2.4), and the main component of the alloy phase is C15 (MgC
uTwo) Type Laves phase and its crystal lattice constant
(A) is 7.05 angstroms ≦ a ≦ 7.13
Hydrogen storage alloy or its hydride
At a temperature in the range of 1000 to 1300 ° C. and in a vacuum.
Or homogenizing heat treatment in an inert gas atmosphere.
It has a configuration.
【0013】[0013]
【作用】前記本発明の構成によれば、一般式が、ZrM
nw Vb Mox Cry Niz (ただし、0.5<w≦
0.8,0<b<0.3,0<x<0.3,0<y≦
0.2,0.8≦z<1.2であり、かつ0.1≦b+
x≦0.3,2.0≦w+b+x+y+z≦2.4)で
示され、合金相の主成分がC15(MgCu2 )型La
ves相であり、かつその結晶格子定数(a)が、7.
05オングストローム≦a≦7.13オングストローム
である水素吸蔵合金またはその水素化物を用いることに
より、急速充電時の高温状態(例えば80℃程度)にお
いても電池内ガス圧を低圧に保ち、液漏れを防止すると
ともに高容量の水素吸蔵量を維持することができる。す
なわち、本発明の水素吸蔵合金電極は、従来のZr−M
n−V−Mo−Cr−Ni系水素吸蔵合金を改善したも
のであり、従来合金組成のNi量を減少することによ
り、急速充電時の高温状態(例えば80℃程度)におけ
る水素平衡圧力を低下させたものである。合金中のNi
は合金が電気化学的に水素の吸蔵・放出を行うためには
必要不可欠のものである。Ni量を減少すれば電気化学
的な活性は低下するが水素吸蔵量が増大するために、従
来の水素吸蔵合金電極の放電容量をほぼ維持できる。According to the structure of the present invention, the general formula is ZrM
n w V b Mo x Cr y Ni z ( however, 0.5 <w ≦
0.8, 0 <b <0.3, 0 <x <0.3, 0 <y ≦
0.2, 0.8 ≦ z <1.2, and 0.1 ≦ b +
x ≦ 0.3, 2.0 ≦ w + b + x + y + z ≦ 2.4), and the main component of the alloy phase is C15 (MgCu 2 ) type La
ves phase and its crystal lattice constant (a) is 7.
By using a hydrogen storage alloy or its hydride satisfying 05 angstroms ≦ a ≦ 7.13 angstroms, the gas pressure in the battery is maintained at a low pressure even in a high temperature state (for example, about 80 ° C.) at the time of rapid charging, and liquid leakage is prevented. At the same time, a high capacity hydrogen storage amount can be maintained. That is, the hydrogen-absorbing alloy electrode of the present invention uses the conventional Zr-M
An improved nV-Mo-Cr-Ni-based hydrogen storage alloy, in which the hydrogen equilibrium pressure in a high temperature state (eg, about 80 ° C.) during rapid charging is reduced by reducing the amount of Ni in the conventional alloy composition. It was made. Ni in alloy
Is essential for the alloy to electrochemically store and release hydrogen. When the amount of Ni decreases, the electrochemical activity decreases, but the amount of hydrogen storage increases, so that the discharge capacity of the conventional hydrogen storage alloy electrode can be substantially maintained.
【0014】したがって、本発明の電極を用いて構成し
たアルカリ蓄電池、例えばニッケル−水素蓄電池は、従
来のこの電池に比べて急速充電時の高温状態においても
電池内のガス圧が低圧で維持できるために液漏れがな
く、高容量を有することが可能になる。Therefore, an alkaline storage battery, such as a nickel-metal hydride storage battery, formed by using the electrode of the present invention can maintain the gas pressure in the battery at a low pressure even in a high-temperature state at the time of rapid charging as compared with a conventional battery. , And has a high capacity.
【0015】次に本発明の製造方法の構成によれば、前
記水素吸蔵合金電極を効率良く合理的に製造することが
できる。なお、熱処理温度を1000〜1300℃の範
囲にした理由は、1000℃より温度が低いと熱処理の
効果が低く、1300℃を越えると合金のMnが蒸発し
て合金組成がくずれるためである。また、真空中または
不活性ガス雰囲気中で均質化処理を行なうのは、合金表
面の酸化を防ぐためである。Next, according to the structure of the manufacturing method of the present invention, the hydrogen storage alloy electrode can be efficiently and rationally manufactured. The reason for setting the heat treatment temperature in the range of 1000 to 1300 ° C. is that if the temperature is lower than 1000 ° C., the effect of the heat treatment is low, and if it exceeds 1300 ° C., Mn of the alloy is evaporated and the alloy composition is destroyed. The reason why the homogenization treatment is performed in a vacuum or in an inert gas atmosphere is to prevent oxidation of the alloy surface.
【0016】[0016]
【実施例】以下に本発明の一実施例について図面ととも
に説明する。市販のZr,Mn,V,Mo,Cr,Ni
金属を原料として、アルゴン雰囲気中、アーク溶解炉で
加熱溶解することにより、(表1)に示したような組成
の合金を作製した。ただし、Mn量が0.8以上のもの
はアーク炉で作製すると多量のMnが蒸発し、目的合金
を得ることが困難であるため、誘導加熱炉で作製した。
次いで、真空中、1100℃で12時間熱処理し、合金
試料とした。An embodiment of the present invention will be described below with reference to the drawings. Commercially available Zr, Mn, V, Mo, Cr, Ni
An alloy having a composition as shown in (Table 1) was prepared by heating and melting a metal as a raw material in an arc melting furnace in an argon atmosphere. However, when the Mn content was 0.8 or more, when produced in an arc furnace, a large amount of Mn was evaporated, and it was difficult to obtain a target alloy.
Next, heat treatment was performed in vacuum at 1100 ° C. for 12 hours to obtain an alloy sample.
【0017】[0017]
【表1】 [Table 1]
【0018】この合金試料の一部はX線回折などの合金
分析および水素ガス雰囲気における水素吸収−放出量測
定(通常のP(水素圧力)−C(組成)−T(温度)測
定)に使用し、残りは電極特性評価に用いた。A part of this alloy sample is used for alloy analysis such as X-ray diffraction and measurement of hydrogen absorption / desorption amount in hydrogen gas atmosphere (normal P (hydrogen pressure) -C (composition) -T (temperature) measurement). The rest was used for electrode characteristics evaluation.
【0019】試料No.1〜5は本発明と構成元素また
は組成比が異なる比較例であり、試料No.6〜15は
本発明の水素吸蔵合金のいくつかの実施例である。ま
ず、各合金試料について、X線回折測定を行った。その
結果、いずれの合金試料についても合金相の主成分はC
15型Laves相(MgCu2 型fcc構造)である
ことを確認した。また、真空熱処理後のものは熱処理前
と比べるとfccのピークがより大きく鋭くなったの
で、熱処理することによりC15型Laves相の割合
が増大し、合金の均質性および結晶性も向上したことが
わかった。特にMn量が0.8以上のものについても均
一組成の目的合金が得られたことを確認した。結晶格子
定数については、いずれも7.05〜7.13オングス
トロームであった。Sample No. Sample Nos. 1 to 5 are comparative examples having different constituent elements or composition ratios from the present invention. Nos. 6 to 15 are some examples of the hydrogen storage alloy of the present invention. First, X-ray diffraction measurement was performed on each alloy sample. As a result, the main component of the alloy phase was C
It was confirmed to be a 15 type Laves phase (MgCu 2 type fcc structure). Also, after heat treatment in vacuum, the peak of fcc became larger and sharper than before heat treatment, so that heat treatment increased the proportion of C15-type Laves phase and improved the homogeneity and crystallinity of the alloy. all right. In particular, it was confirmed that a target alloy having a uniform composition was obtained even when the Mn content was 0.8 or more. The crystal lattice constant was 7.05 to 7.13 angstroms in each case.
【0020】次に、各合金試料について、70℃におい
てPCT測定を行った。試料No.1以外の合金試料で
は水素吸蔵−放出過程のヒステリシスが小さく、試料N
o.1に比べて1/5〜1/10であることがわかっ
た。また、図1に水素ガス圧5kg/cm2 までの水素
吸蔵量と水素平衡圧力との関係を示した。水素吸蔵量は
合金の電気化学的な充放電反応による放電容量と比較す
るため、電気量(mAh/g)に換算して示した。図1
の結果より、合金ZrMnw Vb Mox Cry Niz の
Ni量zが少なくなるとともに水素平衡圧力が低下し、
水素吸蔵量が増大することがわかった。Next, a PCT measurement was performed at 70 ° C. for each alloy sample. Sample No. In alloy samples other than Sample No. 1, the hysteresis of the hydrogen absorption-desorption process was small,
o. It was found that the ratio was 1/5 to 1/10 as compared with 1. FIG. 1 shows the relationship between the hydrogen storage amount up to a hydrogen gas pressure of 5 kg / cm 2 and the hydrogen equilibrium pressure. The amount of hydrogen occlusion was shown in terms of an amount of electricity (mAh / g) for comparison with the discharge capacity of the alloy due to electrochemical charging and discharging reactions. FIG.
The results, reduced the hydrogen equilibrium pressure with the alloy ZrMn w V b Mo x Cr y Ni z of Ni amount z is reduced,
It was found that the hydrogen storage amount increased.
【0021】以上のような合金試料について、電気化学
的な充放電反応によるアルカリ蓄電池用負極としての電
極特性を評価するために単電池試験を行った。試料N
o.1〜15の合金を400メッシュ以下の粒径になる
ように粉砕し、30重量%の水酸化カリウム水溶液に8
0℃で1時間浸漬した後、水洗乾燥した。この合金粉末
1gと導電剤としてのカーボニルニッケル粉末3gおよ
び結着剤としてのポリエチレン微粉末0.12gを十分
混合撹伴し、プレス加工により直径24.5mm、厚さ
2.5mmの円板状に成形した。これを真空中、130
℃で1時間加熱し、結着剤を溶融させて水素吸蔵合金電
極とした。With respect to the alloy samples as described above, a single cell test was performed to evaluate the electrode characteristics as a negative electrode for an alkaline storage battery by an electrochemical charge / discharge reaction. Sample N
o. The alloys Nos. 1 to 15 were pulverized so as to have a particle size of 400 mesh or less, and 8 wt.
After immersion at 0 ° C. for 1 hour, it was washed with water and dried. 1 g of this alloy powder, 3 g of carbonyl nickel powder as a conductive agent, and 0.12 g of polyethylene fine powder as a binder were sufficiently mixed and stirred, and pressed to form a disk having a diameter of 24.5 mm and a thickness of 2.5 mm. Molded. This is placed in a vacuum at 130
C. for 1 hour to melt the binder to form a hydrogen storage alloy electrode.
【0022】この水素吸蔵合金電極にニッケル線のリー
ドを取り付けて負極とし、正極として過剰の容量を有す
る焼結式ニッケル極を、セパレータとしてポリアミド不
織布を用い、比重1.30の水酸化カリウム水溶液を電
解液として、25℃において、一定電流で充電と放電を
繰り返し、各サイクルでの放電容量を測定した。なお、
充電条件は水素吸蔵合金1gあたり100mA×5.5
時間であり、放電条件は同様に1gあたり50mAで行
い、0.8Vでカットした。その結果を図2に示した。
図2はいずれも横軸に充放電サイクル数を、縦軸に合金
1gあたりの放電容量を示したものであり、図中の番号
は(表1)の試料No.と一致している。図2の結果よ
り、試料No.3ではMn量が非常に多いので、アルカ
リ溶液に浸漬するとMnの溶出量が非常に多く合金組成
が大きくずれたため放電容量が小さくなったものと考え
る。また、試料No.4および5では電気化学的な活性
に劣るため放電容量が小さくなった。これら以外の合金
試料では放電容量は340mAh/g以上であり、特に
ZrMnw Vb Mox Cry Niz のNi量zが1.0
〜1.1の時に優れた値を示すことがわかった。A nickel wire lead is attached to the hydrogen storage alloy electrode to form a negative electrode, a sintered nickel electrode having an excessive capacity as a positive electrode, a polyamide nonwoven fabric as a separator, and a potassium hydroxide aqueous solution having a specific gravity of 1.30. As an electrolyte, charging and discharging were repeated at a constant current at 25 ° C., and the discharge capacity in each cycle was measured. In addition,
The charging condition was 100 mA × 5.5 g of hydrogen storage alloy.
The discharge was performed at 50 mA / g, and the voltage was cut at 0.8 V. The result is shown in FIG.
2 shows the number of charge / discharge cycles on the horizontal axis and the discharge capacity per 1 g of the alloy on the vertical axis. In FIG. Matches. From the results in FIG. In No. 3, since the amount of Mn was very large, it was considered that when immersed in an alkaline solution, the amount of Mn eluted was so large that the alloy composition was greatly shifted, and the discharge capacity was reduced. In addition, the sample No. In Nos. 4 and 5, the discharge capacity was small due to poor electrochemical activity. Discharge capacity alloy samples other than these are the 340 mAh / g or more, particularly ZrMn w V b Mo x Cr y Ni z of Ni amount z is 1.0
It was found that an excellent value was exhibited when the value was ~ 1.1.
【0023】さらに、これらの水素吸蔵合金電極を用い
て以下に示したような方法で密閉型ニッケル−水素蓄電
池を作製した。(表1)に示した試料合金を400メッ
シュ以下の粉末にした後、上記と同様の方法でアルカリ
溶液処理し水洗乾燥した。そのような各合金粉末をカル
ボキシメチルセルローズ(CMC)の希水溶液と混合撹
拌してペースト状にし、電極支持体として平均ポアサイ
ズ150ミクロン、多孔度95%、厚さ1.0mmの発
泡状ニッケルシートに充填した。これを120℃で乾燥
してローラープレスで加圧し、さらにその表面にフッ素
樹脂粉末をコーティングして水素吸蔵合金電極とした。Further, using these hydrogen storage alloy electrodes, a sealed nickel-hydrogen storage battery was produced in the following manner. The sample alloys shown in Table 1 were powdered to 400 mesh or less, then treated with an alkali solution in the same manner as described above, washed with water and dried. Each of such alloy powders is mixed with a dilute aqueous solution of carboxymethyl cellulose (CMC) and stirred to form a paste, and as an electrode support, a foamed nickel sheet having an average pore size of 150 microns, a porosity of 95%, and a thickness of 1.0 mm is used. Filled. This was dried at 120 ° C., pressed with a roller press, and further coated on its surface with a fluororesin powder to form a hydrogen storage alloy electrode.
【0024】この電極をそれぞれ幅3.3cm、長さ2
1cm、厚さ0.40mmに調整し、リード板を所定の
2カ所に取り付けた。そして、正極(容量3.0Ah)
およびセパレータと組み合わせて円筒状に3層を渦巻き
状にしてSCサイズの電槽に収納した。このときの正極
は公知の発泡式ニッケル極を選び、幅3.3cm、長さ
18cmとして用いた。この場合もリード板を2カ所に
取り付けた。また、セパレータは親水性を付与したポリ
プロピレン不織布を使用し、電解液としては、比重1.
20の水酸化カリウム水溶液に水酸化リチウムを30g
/l溶解したものを用いた。これを封口して密閉型電池
とした。Each of the electrodes was 3.3 cm wide and 2 cm long.
The thickness was adjusted to 1 cm and the thickness to 0.40 mm, and lead plates were attached to two predetermined positions. And the positive electrode (capacity 3.0 Ah)
In addition, the three layers were spirally formed into a cylindrical shape in combination with a separator and stored in an SC-size battery case. As the positive electrode at this time, a known foamed nickel electrode was selected and used with a width of 3.3 cm and a length of 18 cm. Also in this case, two lead plates were attached. The separator used is a polypropylene nonwoven fabric provided with hydrophilicity, and the specific gravity of the electrolyte is 1.
30 g of lithium hydroxide in 20 potassium hydroxide aqueous solution
/ L dissolved. This was sealed to obtain a sealed battery.
【0025】このようにして作製した各々の電池に電池
内のガス圧を測定するための圧力センサを取り付け、急
速充放電時の電池内ガス圧を調べた。また、電池温度の
変化を調べるために電池側部に熱電対を取り付けた。A pressure sensor for measuring the gas pressure in the battery was attached to each of the batteries thus manufactured, and the gas pressure in the battery during rapid charge and discharge was examined. In addition, a thermocouple was attached to the side of the battery to check the change in the battery temperature.
【0026】30℃で充電0.1C(10時間率)12
0%、放電0.2C(5時間率)0.8Vカットの充放
電を20サイクル行い、水素吸蔵合金電極を活性化した
後、充電0.2Cで電池内のガス圧5kg/cm2 まで
充電を行い、放電0.2Cで0.8Vカットまで放電し
た。次に、電池5個ずつプラスチックの容器内に入れて
充電3C(1/3時間率)で電池内のガス圧5kg/c
m2 まで充電を行った。この際、いずれの電池も充電時
に70〜80℃程度に電池温度が上昇した。充電終了
後、電池を30℃まで冷却した後、放電0.2Cで0.
8Vまで放電し、充電0.2Cの時の放電容量との比較
を行った。Charge at 30 ° C. 0.1 C (10 hour rate) 12
20% charging / discharging at 0%, discharge 0.2C (5 hour rate), 0.8V cut, activate the hydrogen storage alloy electrode, then charge at 0.2C to a gas pressure of 5kg / cm 2 in the battery. And discharge was performed at a discharge of 0.2 C up to a 0.8 V cut. Next, 5 batteries are put into a plastic container and charged at 3 C (1/3 hour rate), and the gas pressure in the battery is 5 kg / c.
to m 2 was charged. At this time, the temperature of each of the batteries increased to about 70 to 80 ° C. during charging. After completion of charging, the battery was cooled to 30 ° C., and then discharged at 0.2 C.
The battery was discharged to 8 V and compared with the discharge capacity at the time of charging 0.2 C.
【0027】図3に各試料の水素吸蔵合金電極を用いた
電池の0.2C充電時の放電容量および3C充電時の放
電容量を示した。図3の結果より、試料No.1および
2ではNi量が多いため、3C充電時の電池の温度上昇
のために水素平衡圧が高くなるために放電容量が低下し
たものと考える。また、試料No.3〜5では合金電極
としての容量が小さいため、0.2C,3C充電時の放
電容量が低くなった。これに対して、本発明の水素吸蔵
合金電極を用いると、0.2C充電時の放電容量および
3C充電時の放電容量が最も高いことがわかった。FIG. 3 shows the discharge capacity at the time of 0.2 C charge and the discharge capacity at the time of 3 C charge of the battery using the hydrogen storage alloy electrode of each sample. From the results of FIG. It is considered that in Examples 1 and 2, since the amount of Ni was large, the hydrogen equilibrium pressure was increased due to the temperature rise of the battery during 3C charging, and the discharge capacity was reduced. In addition, the sample No. In Nos. 3 to 5, the capacity as an alloy electrode was small, so that the discharge capacity at the time of charging at 0.2C and 3C was low. In contrast, it was found that when the hydrogen storage alloy electrode of the present invention was used, the discharge capacity at the time of 0.2 C charge and the discharge capacity at the time of 3 C charge were the highest.
【0028】ここで、本発明の合金組成の作用について
説明する。各組成の範囲は主に水素吸蔵−放出量を確保
するとともに急速充電時に電池温度が高くなっても水素
平衡圧力を低く抑えるためのものである。Mnは合金の
均質性を向上させ、水素吸蔵量を増加させる。Vおよび
Moは水素平衡圧力を低下させ、水素吸蔵−放出量増加
に寄与する。特に、Vは水素吸蔵−放出過程のヒステリ
シスを減少させる効果を有する。Niは水素平衡圧を上
昇させ、水素吸蔵−放出量の低下を引き起こすが、電気
化学的な水素の吸蔵−放出に対する活性の向上に寄与す
る。Here, the operation of the alloy composition of the present invention will be described. The range of each composition is intended mainly to secure the amount of hydrogen storage and release, and to keep the hydrogen equilibrium pressure low even when the battery temperature rises during rapid charging. Mn improves the homogeneity of the alloy and increases the hydrogen storage capacity. V and Mo lower the hydrogen equilibrium pressure and contribute to an increase in the amount of hydrogen storage and release. In particular, V has the effect of reducing the hysteresis of the hydrogen storage-release process. Ni raises the hydrogen equilibrium pressure and causes a decrease in the amount of hydrogen storage and release, but contributes to an improvement in the activity for electrochemical storage and release of hydrogen.
【0029】AB2 型合金のBサイト位に配位する各金
属元素は上記のような効果を合金に付与する。ZrMn
w Vb Mox Cry Niz の場合、Mn量wが0.5を
越えるとアルカリ電解液中で合金表面が腐食されやすく
放電容量が低下するが、アルカリ溶液に浸漬して予め合
金表面のMnを溶出させ、合金表面のMn濃度を低下さ
せることにより電解液中での合金表面の腐食を防ぐこと
ができる。したがって、Mn量wが0.5<wの時、合
金の均質性が非常に大きくなり、水素吸蔵−放出量が増
大する。しかし、Mn量が0.8を越えるとアルカリ溶
液処理により多量のMnが溶出し合金組成が大きくずれ
てしまうので放電容量が小さくなる。したがって、Mn
量wは0.5<w≦0.8が適当である。Crの場合、
Crが含まれるとC14型Laves相(MgZn2 型
ヘキサゴナル構造)が混入しやすく、Cr量yが0.2
を越えると、その混入割合が大きくなるため水素吸蔵−
放出量が低下する。Each metal element coordinated at the B site of the AB 2 type alloy provides the above-described effects to the alloy. ZrMn
For w V b Mo x Cr y Ni z, but the amount of Mn w discharge capacity alloy surface tends to be corroded by the alkaline electrolyte exceeds 0.5 is lowered, the prealloyed surface is immersed in an alkaline solution By eluting Mn and reducing the Mn concentration on the alloy surface, corrosion of the alloy surface in the electrolytic solution can be prevented. Therefore, when the Mn content w is 0.5 <w, the homogeneity of the alloy becomes extremely large, and the amount of hydrogen storage and release increases. However, when the Mn content exceeds 0.8, a large amount of Mn is eluted by the alkali solution treatment, and the alloy composition is largely shifted, so that the discharge capacity is reduced. Therefore, Mn
The amount w is suitably 0.5 <w ≦ 0.8. In the case of Cr
When Cr is contained, the C14-type Laves phase (MgZn 2- type hexagonal structure) is easily mixed, and the Cr amount y is 0.2.
Exceeds the hydrogen absorption rate,
Emissions are reduced.
【0030】VおよびMoは原子半径が大きいため、V
量bとMo量xの合計が0.3を越えると、合金の均質
性が悪くなり逆に水素吸蔵−放出量は減少する。また、
Ni量zではzが大きすぎ、V量bおよびMo量xとの
バランスが崩れると、水素吸蔵−放出量は低下する。し
たがって、V量b、Mo量xとNi量zとのバランスを
考えるとz−b−x≦1.2である方がよい。Since V and Mo have a large atomic radius, V
If the sum of the amount b and the Mo amount x exceeds 0.3, the homogeneity of the alloy becomes poor, and conversely, the amount of hydrogen storage and release decreases. Also,
When the Ni amount z is too large and the balance between the V amount b and the Mo amount x is lost, the hydrogen storage-release amount decreases. Therefore, considering the balance between the V amount b, the Mo amount x, and the Ni amount z, zbx ≦ 1.2 is better.
【0031】さらに、急速充電時には電池温度が70〜
80℃に上昇するので、このような温度領域においても
水素平衡圧力の低い、Ni量zが1.2未満の合金が水
素の吸蔵−放出量も多く有利である。しかし、zが0.
8未満の合金ではNi量が少ないために十分な電気化学
的な活性が得られない。Further, at the time of quick charging, the battery temperature is 70 to
Since the temperature rises to 80 ° C., even in such a temperature range, an alloy having a low hydrogen equilibrium pressure and an Ni content z of less than 1.2 is advantageous in that the amount of absorbed and released hydrogen is large. However, if z is 0.
With an alloy less than 8, sufficient electrochemical activity cannot be obtained due to a small amount of Ni.
【0032】以上のことから、急速充電時においても高
容量を有する水素吸蔵合金電極を得るためには、本発明
の合金組成の条件を満たすことが重要である。From the above, it is important to satisfy the conditions of the alloy composition of the present invention in order to obtain a hydrogen storage alloy electrode having a high capacity even during rapid charging.
【0033】[0033]
【発明の効果】本発明の水素吸蔵合金電極は、合金の高
温での水素平衡圧力を低く抑えることにより、急速充電
時においても多量の水素を吸蔵−放出させることができ
るため、これを電極とするアルカリ蓄電池は、従来のこ
の電池に比べて高容量を損なわずに優れた放電特性を有
する。The hydrogen storage alloy electrode of the present invention can store and release a large amount of hydrogen even during rapid charging by suppressing the hydrogen equilibrium pressure at a high temperature of the alloy. The alkaline storage battery has excellent discharge characteristics without impairing high capacity as compared with the conventional battery.
【図1】本発明の実施例および従来例の70℃における
水素吸蔵量と水素平衡圧力との相関図である。FIG. 1 is a correlation diagram between the hydrogen storage amount at 70 ° C. and the hydrogen equilibrium pressure in Examples of the present invention and a conventional example.
【図2】本発明の実施例および従来例の単電池評価結果
を示す充放電サイクル特性図である。FIG. 2 is a charge / discharge cycle characteristic diagram showing evaluation results of a unit cell of an example of the present invention and a conventional example.
【図3】本発明の実施例および従来例の正極容量規制電
池の急速充電時における放電特性図である。FIG. 3 is a discharge characteristic diagram at the time of rapid charging of the positive-electrode capacity-regulated batteries of the example of the present invention and the conventional example.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岩城 勉 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 平6−96762(JP,A) 特開 平4−301045(JP,A) 特開 平3−289041(JP,A) 特開 平1−102855(JP,A) 特開 平1−60961(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 4/38 H01M 4/24 - 4/26 ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tsutomu Iwaki 1006 Kazuma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-6-96762 (JP, A) JP-A-4- 301045 (JP, A) JP-A-3-28941 (JP, A) JP-A-1-102855 (JP, A) JP-A-1-60961 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 4/38 H01M 4/24-4/26
Claims (3)
Niz (ただし、0.5<w≦0.8,0<b<0.
3,0<x<0.3,0<y≦0.2,0.8≦z<
1.2であり、かつ0.1≦b+x≦0.3,2.0≦
w+b+x+y+z≦2.4)で示され、合金相の主成
分がC15(MgCu2 )型Laves相であり、かつ
その結晶格子定数(a)が、7.05オングストローム
≦a≦7.13オングストロームである水素吸蔵合金ま
たはその水素化物を用いる水素吸蔵合金電極。1. A general formula, ZrMn w V b Mo x Cr y
Ni z (where 0.5 <w ≦ 0.8, 0 <b <0.
3, 0 <x <0.3, 0 <y ≦ 0.2, 0.8 ≦ z <
1.2 and 0.1 ≦ b + x ≦ 0.3, 2.0 ≦
w + b + x + y + z ≦ 2.4), the main component of the alloy phase is a C15 (MgCu 2 ) type Laves phase, and its crystal lattice constant (a) is 7.05 Å ≦ a ≦ 7.13 Å. A hydrogen storage alloy electrode using a hydrogen storage alloy or a hydride thereof.
+xであり、かつNi、VおよびMoの配合比率がz−
b−x≦1.2である請求項1に記載の水素吸蔵合金電
極。2. The composition ratio of Cr, V and Mo is y ≦ b.
+ X and the compounding ratio of Ni, V and Mo is z-
The hydrogen storage alloy electrode according to claim 1, wherein b−x ≦ 1.2.
Niz (ただし、0.5<w≦0.8,0<b<0.
3,0<x<0.3,0<y≦0.2,0.8≦z<
1.2であり、かつ0.1≦b+x≦0.3,2.0≦
w+b+x+y+z≦2.4)で示され、合金相の主成
分がC15(MgCu2 )型Laves相であり、かつ
その結晶格子定数(a)が、7.05オングストローム
≦a≦7.13オングストロームである水素吸蔵合金ま
たはその水素化物を、温度1000〜1300℃の範囲
で、かつ真空中または不活性ガス雰囲気中で均質化熱処
理を行なう水素吸蔵合金電極の製造方法。3. A general formula, ZrMn w V b Mo x Cr y
Ni z (where 0.5 <w ≦ 0.8, 0 <b <0.
3, 0 <x <0.3, 0 <y ≦ 0.2, 0.8 ≦ z <
1.2 and 0.1 ≦ b + x ≦ 0.3, 2.0 ≦
w + b + x + y + z ≦ 2.4), the main component of the alloy phase is a C15 (MgCu 2 ) type Laves phase, and its crystal lattice constant (a) is 7.05 Å ≦ a ≦ 7.13 Å. A method for producing a hydrogen storage alloy electrode in which a hydrogen storage alloy or a hydride thereof is subjected to a homogenizing heat treatment in a temperature range of 1000 to 1300 ° C. in a vacuum or an inert gas atmosphere.
Priority Applications (2)
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JP29421692A JP3352479B2 (en) | 1992-11-02 | 1992-11-02 | Hydrogen storage alloy electrode and method for producing the same |
US08/120,244 US5468309A (en) | 1992-09-14 | 1993-09-13 | Hydrogen storage alloy electrodes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29421692A JP3352479B2 (en) | 1992-11-02 | 1992-11-02 | Hydrogen storage alloy electrode and method for producing the same |
Publications (2)
Publication Number | Publication Date |
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JPH06150917A JPH06150917A (en) | 1994-05-31 |
JP3352479B2 true JP3352479B2 (en) | 2002-12-03 |
Family
ID=17804842
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JP29421692A Expired - Fee Related JP3352479B2 (en) | 1992-09-14 | 1992-11-02 | Hydrogen storage alloy electrode and method for producing the same |
Country Status (1)
Country | Link |
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JP (1) | JP3352479B2 (en) |
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1992
- 1992-11-02 JP JP29421692A patent/JP3352479B2/en not_active Expired - Fee Related
Also Published As
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JPH06150917A (en) | 1994-05-31 |
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