JP3185151B2 - Hydrogen storage alloy for hydrogen storage electrode and method for producing hydrogen storage electrode - Google Patents
Hydrogen storage alloy for hydrogen storage electrode and method for producing hydrogen storage electrodeInfo
- Publication number
- JP3185151B2 JP3185151B2 JP08078591A JP8078591A JP3185151B2 JP 3185151 B2 JP3185151 B2 JP 3185151B2 JP 08078591 A JP08078591 A JP 08078591A JP 8078591 A JP8078591 A JP 8078591A JP 3185151 B2 JP3185151 B2 JP 3185151B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- alloy
- electrode
- reaction
- storage alloy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000956 alloy Substances 0.000 title claims description 81
- 239000001257 hydrogen Substances 0.000 title claims description 80
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 80
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 79
- 238000003860 storage Methods 0.000 title claims description 78
- 229910045601 alloy Inorganic materials 0.000 title claims description 77
- 238000004519 manufacturing process Methods 0.000 title claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 43
- 239000000843 powder Substances 0.000 claims description 26
- 238000005245 sintering Methods 0.000 claims description 19
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
- 230000002194 synthesizing effect Effects 0.000 claims description 5
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 22
- 238000000034 method Methods 0.000 description 21
- 238000002844 melting Methods 0.000 description 16
- 230000008018 melting Effects 0.000 description 16
- 239000000203 mixture Substances 0.000 description 15
- 239000000463 material Substances 0.000 description 14
- 229910052759 nickel Inorganic materials 0.000 description 11
- 238000003786 synthesis reaction Methods 0.000 description 10
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 6
- 229910010380 TiNi Inorganic materials 0.000 description 5
- 238000011109 contamination Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 239000003792 electrolyte Substances 0.000 description 5
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 5
- 229910001120 nichrome Inorganic materials 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 230000010287 polarization Effects 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 239000000470 constituent Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 229910000765 intermetallic Inorganic materials 0.000 description 4
- 238000010298 pulverizing process Methods 0.000 description 4
- 239000010936 titanium Substances 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 150000004678 hydrides Chemical class 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 2
- 229910008340 ZrNi Inorganic materials 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052746 lanthanum Inorganic materials 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 229940101209 mercuric oxide Drugs 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 description 1
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 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
- 230000004913 activation Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- ASKVAEGIVYSGNY-UHFFFAOYSA-L cobalt(ii) hydroxide Chemical compound [OH-].[OH-].[Co+2] ASKVAEGIVYSGNY-UHFFFAOYSA-L 0.000 description 1
- 238000005049 combustion synthesis Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000002482 conductive additive Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000006232 furnace black Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910001068 laves phase Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 150000004681 metal hydrides Chemical class 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 229910001285 shape-memory alloy Inorganic materials 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000006467 substitution reaction Methods 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)
Description
【0001】[0001]
【産業上の利用分野】本発明は、アルカリ蓄電池などの
負極に用いる水素吸蔵合金からなる電極の製造方法に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an electrode made of a hydrogen storage alloy used for a negative electrode of an alkaline storage battery or the like.
【0002】[0002]
【従来の技術】水素吸蔵電極は、水素の可逆的な吸蔵お
よび放出が可能な水素吸蔵合金を電極に用いるものであ
り、その水素の電気化学的な酸化還元反応をアルカリ蓄
電池の負極の起電反応に利用する。水素吸蔵電極に用い
られる水素吸蔵合金には、LaNi5 ,Laves 相のZrNi2 あ
るいはTiNiなどの金属間化合物の構成元素を、そのほか
の金属で置換して水素吸蔵電極としての性能を改良した
ものなどがある。2. Description of the Related Art A hydrogen storage electrode uses a hydrogen storage alloy capable of reversibly storing and releasing hydrogen as an electrode. The electrochemical oxidation-reduction reaction of hydrogen is carried out by the electromotive force of a negative electrode of an alkaline storage battery. Use for reaction. Hydrogen storage alloys used for hydrogen storage electrodes include those in which the constituent elements of intermetallic compounds such as LaNi 5 or Laves phase ZrNi 2 or TiNi are replaced with other metals to improve the performance as hydrogen storage electrodes. There is.
【0003】そして、これらの水素吸蔵合金を用いる従
来の水素吸蔵電極の製造方法には、次のようなものがあ
った。[0003] Conventional methods of manufacturing a hydrogen storage electrode using these hydrogen storage alloys include the following.
【0004】1つは、水素吸蔵合金の粉末をフッ素樹脂
などの結着剤によってパンチングメタルや発泡ニッケル
などの耐アルカリ性導電性支持体に保持させる方法であ
る。この方法で製造した電極をプラスチックボンデッド
タイプの電極と呼ぶ。もう1つは、水素吸蔵合金の粉末
を焼結する方法である。この方法によって製造した電極
を焼結式の電極と呼ぶ。[0004] One is a method in which a powder of a hydrogen storage alloy is held on an alkali-resistant conductive support such as punched metal or foamed nickel by a binder such as a fluororesin. The electrode manufactured by this method is called a plastic bonded type electrode. The other is a method of sintering a powder of a hydrogen storage alloy. The electrode manufactured by this method is called a sintered electrode.
【0005】プラスチックボンデッド電極は、水素吸蔵
合金の粉末をペースト状にして、このペーストを導電性
支持体に塗着したり充填してから、乾燥し、プレスする
方法で製造することができるので、簡単な製造装置によ
って電極を高速に製造できる点で優れている。[0005] The plastic bonded electrode can be produced by a method in which a powder of a hydrogen storage alloy is made into a paste, and the paste is applied or filled on a conductive support, and then dried and pressed. It is excellent in that electrodes can be manufactured at high speed by a simple manufacturing apparatus.
【0006】一方、焼結式電極は、水素吸蔵合金が焼結
されて結合しているので、機械的な強度が高く、また水
素吸蔵合金間の電子伝導性が高いので電極の分極が小さ
い点で優れている。On the other hand, the sintered electrode has a high mechanical strength because the hydrogen storage alloy is sintered and bonded thereto, and has a small electrode polarization because the electron conductivity between the hydrogen storage alloys is high. Is excellent.
【0007】[0007]
【発明が解決しようとする課題】しかし、これらの電極
ではいずれも粉末状の水素吸蔵合金を用いるので、まず
真空中や不活性雰囲気中で水素吸蔵合金の成分金属を溶
解してから、これを鋳造して機械的に粉砕するか、ある
いはその溶解物を噴霧して粉末を製造する必要があっ
た。そして、この溶解工程や粉砕工程において、大規模
な装置や熱源としての大量のエネルギ消費が必要であ
り、さらに溶解工程での炉材からの不純物の混入,溶解
工程での揮発性成分元素の蒸発による合金組成の偏移,
粉砕工程でのミルの材料による合金粉末の汚染等の問題
点があった。However, since all of these electrodes use a powdered hydrogen storage alloy, the component metals of the hydrogen storage alloy are first dissolved in a vacuum or in an inert atmosphere, and then dissolved. It was necessary to cast and mechanically grind or spray the melt to produce a powder. In the melting step and the pulverizing step, a large-scale equipment and a large amount of energy consumption as a heat source are required. Furthermore, impurities are mixed in from the furnace material in the melting step, and the volatile component elements are evaporated in the melting step. Of alloy composition due to
There were problems such as contamination of the alloy powder by the material of the mill in the pulverizing step.
【0008】このような溶解工程を用いない水素吸蔵電
極の製造方法としては、特開昭49-15933号に開示された
チタンの水素化物およびニッケルの粉末混合物の圧粉体
を高温で長時間焼結し、この焼結体を粉砕したものを銅
粉末と混合してホットプレスする方法がある。しかしこ
の方法は、大規模な溶解装置を必要としないものの、チ
タンの水素化物とニッケルとの粉末混合物の圧粉体の焼
結に1日程度の長時間を必要とするので、量産性に劣る
という欠点がある。また合金の材料として用いるチタン
の水素化物が著しく高価である点においても、この方法
は工業的な利用価値が低い。As a method of manufacturing a hydrogen storage electrode without using such a melting step, a green compact of a powder mixture of a hydride of titanium and nickel disclosed in Japanese Patent Application Laid-Open No. 49-15933 is sintered for a long time at a high temperature. There is a method in which the sintered body is pulverized, mixed with copper powder and hot-pressed. However, although this method does not require a large-scale melting apparatus, it requires a long time of about one day for sintering a green compact of a powder mixture of hydride and nickel of titanium, and is inferior in mass productivity. There is a disadvantage that. Also, this method has low industrial utility in that the hydride of titanium used as a material for the alloy is extremely expensive.
【0009】従って、安価な合金材料をそのまま用いる
ことができて、しかも、エネルギ消費が多く不純物の混
入や合金組成の偏移が起こりやすい合金の溶解工程や粉
砕工程を必要とせず、さらに電極の分極が小さい水素吸
蔵合金の焼結体からなる水素吸蔵電極の製造方法が望ま
れていた。Therefore, an inexpensive alloy material can be used as it is, and furthermore, there is no need for a melting step or a pulverizing step of an alloy which consumes a lot of energy and is liable to mix impurities and shift the alloy composition. There has been a demand for a method of manufacturing a hydrogen storage electrode made of a sintered body of a hydrogen storage alloy having a small polarization.
【0010】[0010]
【課題を解決するための手段】本発明は、上述の問題点
を解決するために、水素吸蔵合金を合成する反応の際に
発熱する材料金属粉末を混合した圧粉体に、真空中もし
くは非酸化性雰囲気中で着火して、自己伝播反応焼結す
る水素吸蔵電極の製造方法を提供する。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a method for producing a hydrogen storage alloy, which comprises mixing a metal powder which generates heat during a reaction for synthesizing a hydrogen storage alloy with a green compact or a non-vacuum compact. A method for producing a hydrogen storage electrode that ignites in an oxidizing atmosphere and performs self-propagating reaction sintering.
【0011】[0011]
【作用】自己伝播反応焼結(Self-Propagating Reaction
Sintering) は、燃焼合成(Combustion Synthesis)とも
呼ばれる現象もしくはプロセスであり、その内容は次の
ようなものである。[Action] Self-Propagating Reaction
Sintering is a phenomenon or process also called combustion synthesis, and its contents are as follows.
【0012】すなわち、無機物質の合成反応にかかる原
料粉末の混合圧粉体の一部に着火して、反応の開始に必
要な活性化エネルギよりも高いエネルギを与えると、そ
の部分で無機物質の合成反応が始まる。その際に、その
反応が自発的な発熱をともなう種類のものである場合、
すなわちその無機化合物の生成エンタルピが負の場合に
は、その反応が起こった部分では着火によって投入され
た熱量よりも多くの熱が発生する。そして、この発熱に
よって、着火部に隣接する部分の圧粉体が加熱され、こ
の隣接部分に反応が伝播する。この隣接部分でも反応に
よる発熱がおこるので、合成反応が次々と伝播して進行
する。この発熱反応が起こっている部分では、多くの場
合に強い発光が観察されるほど高温になる。That is, when a part of the mixed green compact of the raw material powders involved in the synthesis reaction of the inorganic substance is ignited and an energy higher than the activation energy required for starting the reaction is given, the part of the inorganic substance is decomposed at that part. The synthesis reaction starts. If the reaction is of a type with spontaneous exotherm,
That is, when the enthalpy of formation of the inorganic compound is negative, more heat is generated in the portion where the reaction has occurred than the heat input by ignition. Then, the heat generation heats the green compact in a portion adjacent to the ignition portion, and the reaction propagates to the adjacent portion. Since heat is generated by the reaction also in this adjacent portion, the synthesis reaction propagates and proceeds one after another. In many cases, the temperature at which the exothermic reaction occurs becomes so high that strong light emission is observed.
【0013】そして、自己伝播反応焼結では、反応ゾー
ンが高温になって、この部分で固相反応が起こったり、
一部が融解状態になっていて、このゾーンはその後方に
低温で固相の既反応部分を形成しながら、その前方の低
温で固相の未反応部分へと順次移動していく。In the self-propagating reaction sintering, the reaction zone is heated to a high temperature, and a solid phase reaction occurs in this part,
A part of the zone is in a molten state, and this zone sequentially moves to an unreacted portion of the solid phase at a low temperature in front thereof while forming a reacted portion of the solid phase at a low temperature behind the zone.
【0014】従って、この自己伝播反応焼結の特徴とし
ては、通常の焼結プロセスと同様の特徴のほかに、反応
の生成熱を利用して加熱するので、外部の熱源によって
加熱する必要がないこと、および、反応が自発的に伝播
して行くので、焼結が短時間で終わることがあげられ
る。Therefore, the self-propagating reaction sintering has the same characteristics as those of the ordinary sintering process, and furthermore, since it uses the heat generated by the reaction, it does not need to be heated by an external heat source. And sintering is completed in a short time because the reaction spontaneously propagates.
【0015】この現象は、金属間化合物にもみられるも
ので、たとえば、形状記憶合金であるTiNi合金の製造に
も応用する試みがある。This phenomenon is also observed in intermetallic compounds. For example, there is an attempt to apply it to the production of a TiNi alloy which is a shape memory alloy.
【0016】本発明は、このプロセスを水素吸蔵電極の
製造に応用しようとするものである。The present invention intends to apply this process to the production of a hydrogen storage electrode.
【0017】たとえば、水素吸蔵電極に用いられる金属
間化合物LaNi5およびTiNiの生成エンタルピΔH は、そ
れぞれ-40kcal/mol および-16kcal/mol であり、ΔH が
負の値であるから、これらの金属間化合物をその成分金
属から合成する反応は、発熱反応である。従って、Laお
よびNiの粉末を原子比で1:5 の比率で混合した圧粉体
や、TiおよびNiの粉末を原子比で等モルの比率で混合し
た圧粉体に、真空中やアルゴンなどの不活性雰囲気中で
着火すると、その反応熱によって反応が自発的に伝播し
て、それぞれ金属間化合物LaNi5 およびTiNiを主体とす
る焼結体が得られる。For example, the enthalpies of formation ΔH of the intermetallic compounds LaNi 5 and TiNi used for the hydrogen storage electrode are -40 kcal / mol and -16 kcal / mol, respectively, and ΔH is a negative value. The reaction for synthesizing a compound from its component metals is an exothermic reaction. Therefore, a green compact in which La and Ni powders are mixed in an atomic ratio of 1: 5, and a green compact in which Ti and Ni powders are mixed in an equimolar ratio by atomic ratio, in vacuum, argon, etc. When ignited in an inert atmosphere, the reaction spontaneously propagates due to the reaction heat, and a sintered body mainly containing the intermetallic compounds LaNi 5 and TiNi is obtained.
【0018】なお、水素吸蔵電極に用いる水素吸蔵合金
は、たとえばLaNi5 の組成のままでは、そのPCT特性
(平衡水素圧−水素吸蔵量−等温線特性)におけるプラ
トー部の平衡圧がやや高く、また充放電サイクル寿命が
短いので、これらの問題を解決するために、Laの一部を
そのほかの稀土類元素や少量のZrで置換したり、Niの一
部をCoやAlで置換することが行われる。そして、このよ
うな場合にも、たとえば、ZrNi5 およびLaCo5 の生成エ
ンタルピが、それぞれ-57kcal/mol および-17.5kcal/mo
l であるように、これらの置換元素を用いてもこれらの
成分元素から水素吸蔵合金を合成する反応は多くの場合
に発熱反応となる。従って、実用的な多成分系の電池用
水素吸蔵合金の場合にも、本発明の方法が適用できる。The hydrogen storage alloy used for the hydrogen storage electrode has, for example, the composition of LaNi 5 having a slightly higher equilibrium pressure at the plateau portion in its PCT characteristics (equilibrium hydrogen pressure-hydrogen storage amount-isothermal characteristic). In addition, since the charge-discharge cycle life is short, in order to solve these problems, it is necessary to replace part of La with other rare earth elements or a small amount of Zr, and replace part of Ni with Co or Al. Done. And even in such a case, for example, the enthalpy of formation of ZrNi 5 and LaCo 5 are -57 kcal / mol and -17.5 kcal / mo, respectively.
As in l, the reaction for synthesizing a hydrogen storage alloy from these constituent elements is an exothermic reaction in many cases even if these substitution elements are used. Therefore, the method of the present invention can be applied to a practical multi-component hydrogen storage alloy for batteries.
【0019】また、本発明では、水素吸蔵合金の合成反
応における発熱を利用するのであるから、自己伝播反応
焼結を起こす圧粉体の材料粉末は必ずしも単体金属であ
る必要はなく、合金材料であってもよい。要するに、圧
粉体の材料金属に関しては、その材料金属が単体金属で
あるか合金であるかという点は、本発明における必須構
成要件ではなく、水素吸蔵合金を合成する反応が発熱反
応になる材料金属を用いることが本発明の必須構成要件
である。Further, in the present invention, since the heat generated in the synthesis reaction of the hydrogen storage alloy is used, the material powder of the green compact which causes self-propagation reaction sintering is not necessarily a single metal, but is made of an alloy material. There may be. In short, regarding the material metal of the green compact, whether the material metal is a simple metal or an alloy is not an essential constituent requirement in the present invention, but a material that causes a reaction for synthesizing a hydrogen storage alloy to be an exothermic reaction. The use of a metal is an essential component of the present invention.
【0020】また、本発明の自己伝播反応焼結では、水
素吸蔵合金の合成が起こっている反応ゾーンが高温にな
っているので、合金の酸化反応を防止して所望の水素吸
蔵合金を得るためには、真空中またはアルゴンや水素な
どの非酸化性の雰囲気で反応焼結をおこなう必要があ
る。In the self-propagating reaction sintering of the present invention, since the reaction zone in which the synthesis of the hydrogen storage alloy is occurring is at a high temperature, the oxidation reaction of the alloy is prevented to obtain the desired hydrogen storage alloy. It is necessary to perform reaction sintering in vacuum or in a non-oxidizing atmosphere such as argon or hydrogen.
【0021】この方法によれば、次の点が従来の水素吸
蔵電極の製造方法と比較して有利である。 (1)安価な金属の粉末材料を成型した圧粉体を反応焼
結したものが、そのままで水素吸蔵電極になるので、大
規模な合金溶解炉や、粉末製造装置を用いる工程が不要
になる。 (2)金属の圧粉体の一部を支持した状態で水素吸蔵合
金の合成反応が短時間に進行し、そのまま水素吸蔵電極
が得られるので、合金の溶解工程における炉材からの合
金の汚染,溶解工程における低融点成分元素の蒸発によ
る組成の偏移および粉砕工程におけるミルの材料による
汚染が起こらない。従って、不純物の量が少なく、しか
も組成の偏移が少ない水素吸蔵合金からなる電極が得ら
れる。 (3)合金材料を加熱して溶解する工程を経ることな
く、反応熱のみによって水素吸蔵合金の合成が起こるの
で、電極の製造に要するエネルギが著しく少なくて済
む。 (4)得られる電極は水素吸蔵合金の焼結体であるか
ら、電極の電気抵抗が小さくなり、電池の内部抵抗が小
さくなって、電池を大電流で放電する際の分極が小さく
なる。According to this method, the following points are advantageous as compared with the conventional method for manufacturing a hydrogen storage electrode. (1) Since a compact obtained by molding a compact made of an inexpensive metal powder material by reaction sintering becomes a hydrogen storage electrode as it is, a large-scale alloy melting furnace and a process using a powder manufacturing apparatus are not required. . (2) The synthesis reaction of the hydrogen storage alloy proceeds in a short time while supporting a part of the metal compact, and the hydrogen storage electrode can be obtained as it is. Therefore, the contamination of the alloy from the furnace material in the melting process of the alloy. In addition, the composition shift due to the evaporation of the low melting point element in the melting step and the contamination of the mill material in the pulverizing step do not occur. Accordingly, an electrode made of a hydrogen storage alloy having a small amount of impurities and a small composition shift can be obtained. (3) Since the synthesis of the hydrogen storage alloy occurs only by the reaction heat without the step of heating and melting the alloy material, the energy required for manufacturing the electrode can be significantly reduced. (4) Since the obtained electrode is a sintered body of a hydrogen storage alloy, the electric resistance of the electrode is reduced, the internal resistance of the battery is reduced, and the polarization when discharging the battery with a large current is reduced.
【0022】[0022]
【実施例】本発明を好適な実施例によって説明する。 [実施例]モル比でLa0.8 Ce0.2 Ni3.8 Co0.7 Al0.3 Mn
0.2 の組成になるように、粒径が100 μm以下のLa、C
e、Ni、Co、AlおよびMnの粉末を乾式で混合し、この混
合粉末を、1ton/cm2 の圧力でプレスして、厚さ約0.4m
m 、巾約16mm、高さ約57mmの圧粉体を成型した。この原
料粉末には可塑性に富むニッケル粉末が多量に含まれて
いるので、圧粉体の密度を高くすることができた。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described by way of preferred embodiments. [Example] La 0.8 Ce 0.2 Ni 3.8 Co 0.7 Al 0.3 Mn in molar ratio
La, C with a particle size of 100 μm or less so that the composition becomes 0.2
e, Ni, Co, Al and Mn powders are dry-mixed, and this mixed powder is pressed under a pressure of 1 ton / cm 2 to a thickness of about 0.4 m.
m, a compact having a width of about 16 mm and a height of about 57 mm were molded. Since the raw material powder contained a large amount of nickel powder having high plasticity, the density of the green compact could be increased.
【0023】次に、圧粉体との接触面積が小さくなるよ
うに表面に多数の凹凸を有するカルシア製の台上にこの
圧粉体を置き、その圧粉体の一端にニクロム線を巻き付
け、これを真空容器に入れて、真空容器の内部を約10-5
気圧の真空にした。そして、このニクロム線に通電して
赤熱させると、圧粉体はニクロム線に接している部分か
ら着火して激しく発光しはじめた。そして、発光してい
る反応部は、未反応の圧粉体へと順次伝播していった。
発光をともなう反応は数分間で終了したので、焼結体を
放冷してから真空容器に乾燥空気を導入した。Next, the compact is placed on a calcia table having a large number of irregularities on the surface so that the contact area with the compact is reduced, and a nichrome wire is wound around one end of the compact. Put this in a vacuum vessel and evacuate the inside of the vacuum vessel to about 10 -5
Atmospheric pressure was applied. When the nichrome wire was energized and glowed red, the green compact ignited from the portion in contact with the nichrome wire and began to emit light intensely. Then, the reaction part emitting light sequentially propagated to the unreacted green compact.
Since the reaction involving light emission was completed within a few minutes, the sintered body was allowed to cool and then dry air was introduced into the vacuum vessel.
【0024】自己伝播反応焼結が進行して水素吸蔵電極
が製造されている途中の圧粉体の斜視図を図1に示す。
図1において、1は未反応の圧粉体、2は反応が終わっ
た水素吸蔵合金の焼結体、3は水素吸蔵合金の合成反応
が起こっていて、未反応の圧粉体に向かって伝播しつつ
ある反応焼結ゾーン、4は着火のために取り付けたニク
ロム線である。FIG. 1 is a perspective view of a green compact in the process of producing a hydrogen storage electrode by the progress of self-propagating reaction sintering.
In FIG. 1, reference numeral 1 denotes an unreacted green compact, 2 denotes a sintered body of a hydrogen storage alloy after the reaction, and 3 denotes a synthesis reaction of the hydrogen storage alloy, which propagates toward the unreacted green compact. The reacting sintering zone 4 is a nichrome wire attached for ignition.
【0025】得られた焼結体は、板状の圧粉体の形状を
保っており、その寸法はやや収縮して、厚さ約0.4mm 、
巾約15mm、長さ約55mmであった。この焼結体は1枚の重
量が約1.5 gの多孔体であり、この焼結体を瑪瑙の乳鉢
で粉砕して、その結晶構造についてX線回折分析をおこ
なった結果、LaNi5 形の結晶構造のものが主体であっ
た。そして、合金の組成は、投入した原料金属の成分に
ほぼ等しかった。そして粒径が45μm以下に分級したこ
の合金粉末100mg と電解銅粉末400mg とを混合し、加圧
成型して、合金の容量評価用の電極を製作し、7M KOH電
解液中で、15mAの電流で2.5 時間充電し、酸化第2水銀
電極電位を基準として0.7Vまで放電するという充放電を
繰り返して放電容量を求めた結果、合金1g当たりの放電
容量は約0.32Ahであった。The obtained sintered body retains the shape of a plate-like compact, and its dimensions shrink slightly to a thickness of about 0.4 mm.
It was about 15mm wide and 55mm long. The sintered body is the weight of one sheet porous material about 1.5 g, the sintered body was ground in an agate mortar, the results was carried out X-ray diffraction analysis of the crystal structure, LaNi 5 in crystalline form The main thing was the structure. And the composition of the alloy was almost equal to the component of the input raw material metal. Then, 100 mg of the alloy powder classified to have a particle size of 45 μm or less and 400 mg of electrolytic copper powder were mixed, pressed and molded to produce an electrode for evaluating the capacity of the alloy, and a current of 15 mA was applied in a 7 M KOH electrolyte. The battery was charged for 2.5 hours and then discharged to 0.7 V with reference to the mercury oxide electrode potential. The discharge capacity was determined as a result. As a result, the discharge capacity per 1 g of the alloy was about 0.32 Ah.
【0026】また、この焼結体1枚にニッケル網を当接
して集電し、7M KOH電解液中で、0.24A の電流で2.5 時
間充電し、酸化第2水銀電極電位を基準として0.7Vまで
放電するという充放電を繰り返した場合の放電容量は、
約0.48Ahであった。The sintered body was brought into contact with a nickel net to collect electricity, charged in a 7M KOH electrolyte at a current of 0.24 A for 2.5 hours, and 0.7 V based on the potential of the mercuric oxide electrode. The discharge capacity in the case of repeating charge and discharge of discharging up to
It was about 0.48 Ah.
【0027】次に、この焼結体を負極とするニッケル・
金属水素化物蓄電池を製作した。Next, a nickel alloy using this sintered body as a negative electrode
A metal hydride storage battery was manufactured.
【0028】この電池の負極には、この焼結体4枚を用
い、集電のためにニッケル網をその表面に当接した。正
極には、公知の焼結式水酸化ニッケル電極3枚を用い
た。この焼結式ニッケル電極1枚の大きさは、厚さが約
0.84mm、巾が約14mm、長さが約54mmであり、3枚の正極
板に含まれる水酸化ニッケル及び添加物の水酸化コバル
トの量の合計は、約3.5gであり、反応が1電子過程に従
うことを仮定した場合の理論容量は、約1.01Ahである。
セパレータには、ナイロン製の不織布を用いた。そし
て、セパレータを介して正極板と負極板とを交互に積層
した極板群を角形密閉容器に収納し、外形寸法が、高さ
66.7mm、巾16.4mm、厚さ5.6mm の密閉電池を構成した。
電解液は、7M KOHに20g/l のLiOHを添加したものを用い
た。この電池を電池Aと呼ぶ。 [比較例]比較のために、上記の実施例と同じ合金組成
で、次のような従来の製造方法を用いてプラスチックボ
ンデッドタイプの水素吸蔵電極を製造した。As the negative electrode of this battery, four sintered bodies were used, and a nickel net was in contact with the surface for current collection. As the positive electrode, three known sintered nickel hydroxide electrodes were used. The size of one sintered nickel electrode is approximately
0.84 mm, width about 14 mm, length about 54 mm, the total amount of nickel hydroxide and the additive cobalt hydroxide contained in the three positive plates is about 3.5 g, and the reaction is one electron. The theoretical capacity, assuming to follow the process, is about 1.01 Ah.
Nylon nonwoven fabric was used for the separator. Then, the electrode plate group in which the positive electrode plate and the negative electrode plate are alternately laminated via the separator is housed in a rectangular sealed container, and the outer dimensions are height.
A sealed battery of 66.7 mm, width of 16.4 mm and thickness of 5.6 mm was constructed.
The electrolyte used was 7 M KOH to which 20 g / l of LiOH had been added. This battery is called battery A. [Comparative Example] For comparison, a plastic bonded type hydrogen storage electrode was manufactured with the same alloy composition as that of the above-mentioned embodiment by using the following conventional manufacturing method.
【0029】まず、モル比でLa0.8 Ce0.2 Ni3.8 Co0.7
Al0.3 Mn0.2 の組成になるように、La,Ce,Ni,Co,Al
およびMnをカルシアで内張りした高周波溶解炉に投入
し、2時間をかけて溶解した。次に、この溶解物を水冷
した銅製のモールドに注入して凝固させ、この鋳塊をジ
ョークラッシャーで粗粉砕してから、アルミナ製のボー
ルミルで微粉砕した。そして、分級し、粒径が45μm以
下の水素吸蔵合金粉末を得た。First, in terms of molar ratio, La 0.8 Ce 0.2 Ni 3.8 Co 0.7
Al 0.3 so that the composition of the Mn 0.2, La, Ce, Ni , Co, Al
And Mn were charged into a high-frequency melting furnace lined with calcia and melted for 2 hours. Next, this melt was poured into a water-cooled copper mold and solidified. The ingot was roughly pulverized with a jaw crusher and then finely pulverized with an alumina ball mill. Then, classification was performed to obtain a hydrogen storage alloy powder having a particle size of 45 μm or less.
【0030】この合金粉末は、結晶構造はLaNi5 形のも
のが主体であったが、揮発成分のMnが合金の溶解中に揮
発して、その化学量論数が投入時の0.2 から0.12へ低下
していた。また、ボールミルで粉砕した際のミルの材料
であるアルミナの微粉末が、約0.1 重量%混入してい
た。The crystal structure of this alloy powder was mainly of LaNi 5 type , but the volatile component Mn volatilized during melting of the alloy, and the stoichiometric number of the alloy powder changed from 0.2 at the time of injection to 0.12. Had declined. Further, about 0.1% by weight of a fine powder of alumina as a material of the mill when pulverized by a ball mill was mixed.
【0031】この水素吸蔵合金粉末100mg と電解銅粉末
400mgとを混合し、加圧成型して、合金の容量評価用の
電極を製作し、7M KOH電解液中で、15mAの電流で2.5 時
間充電し、酸化第2水銀電極電位を基準として0.7Vまで
放電するという充放電を繰り返して放電容量を求めた結
果、合金1g当たりの放電容量は約0.32Ahであった。The hydrogen storage alloy powder 100 mg and the electrolytic copper powder
400 mg, and press-molded to produce an electrode for evaluating the capacity of the alloy, charged in a 7 M KOH electrolyte at a current of 15 mA for 2.5 hours, and 0.7 V based on the potential of the mercuric oxide electrode. The discharge capacity was determined by repeating charge / discharge of discharging to about 0.32 Ah per 1 g of the alloy.
【0032】次に、この水素吸蔵合金粉末100 重量部に
導電助剤たるファーネスブラック1.5 重量部を混合し、
結着剤たる1.5 重量部相当のポリビニルアルコールを溶
解した水溶液を加えて混練し、ペースト状混合物を製作
した。そして、このペースト状混合物を、厚さが0.8mm
で開孔率が約50% のニッケルメッキした鉄製のパンチン
グメタルの両面に塗着し、乾燥してから、約1ton/cm2
の圧力でプレスし、切断して従来の製造方法による水素
吸蔵電極を製作した。この電極1枚の大きさは、厚さ約
0.4mm 、巾約15mm、長さ約55mmであった。この水素吸蔵
電極1枚に含まれる水素吸蔵合金の重量は約1.2 gであ
った。従って、この水素吸蔵合金電極1枚には、約0.38
Ahの放電容量を有する水素吸蔵合金が含まれている。Next, 1.5 parts by weight of furnace black as a conductive additive was mixed with 100 parts by weight of the hydrogen storage alloy powder.
An aqueous solution in which 1.5 parts by weight of polyvinyl alcohol as a binder was dissolved was added and kneaded to produce a paste-like mixture. Then, this paste-like mixture is 0.8 mm thick
In and coated on both sides of the open porosity is about 50% nickel plated iron punched metal, after drying, about 1 ton / cm 2
Pressing and cutting at a pressure of 1. The hydrogen absorbing electrode was manufactured by a conventional manufacturing method. The size of this electrode is approximately
It was 0.4 mm, about 15 mm wide and about 55 mm long. The weight of the hydrogen storage alloy contained in one hydrogen storage electrode was about 1.2 g. Therefore, this one hydrogen storage alloy electrode has about 0.38
A hydrogen storage alloy having a discharge capacity of Ah is included.
【0033】このように、従来のプラスチックボンデッ
ドの電極が本発明の方法による電極よりも水素吸蔵合金
の坦持量が少ない原因は、プラスチックボンデッド電極
では、実用的に適用できる程度の機械的なプレスでは、
可塑性が小さい水素吸蔵合金粉末からなる圧粉体の多孔
度をある程度以上小さくできないことにある。As described above, the reason that the conventional plastic-bonded electrode has a smaller amount of the hydrogen-absorbing alloy than the electrode according to the method of the present invention is that the plastic-bonded electrode has a mechanically practically applicable degree. In the press,
This is because the porosity of the compact made of the hydrogen storage alloy powder having low plasticity cannot be reduced to a certain degree or more.
【0034】次に、自己伝播反応焼結によって製作した
水素吸蔵電極の代わりに、このプラスチックボンデッド
タイプの水素吸蔵電極を4枚用いるほかは、電池Aと同
じにして、電池Bを製作した。Next, a battery B was manufactured in the same manner as the battery A except that four plastic bonded type hydrogen storage electrodes were used instead of the hydrogen storage electrode manufactured by self-propagating reaction sintering.
【0035】以上に述べた電池Aおよび電池Bを、25℃
において、1Aの電流で1.2 時間充電し、1Aの電流で端子
電圧が1.0Vになるまで放電するという充放電サイクルを
繰り返した。そして、放電容量が10サイクル目の放電容
量の60% に減少するまでの充放電サイクル数(充放電サ
イクル寿命)を調べた。その結果を表1に示す。また、
1Aの電流で1.2 時間充電した後に3Aの電流で放電した場
合に、端子電圧が0.8Vに到達するまでの放電時間の1/2
の放電時間における端子電圧(放電中間電圧)を調べ
た。その結果も表1に併せて示す。The batteries A and B described above were heated at 25 ° C.
, A charge / discharge cycle was repeated in which the battery was charged at a current of 1 A for 1.2 hours and discharged at a current of 1 A until the terminal voltage reached 1.0 V. Then, the number of charge / discharge cycles (charge / discharge cycle life) until the discharge capacity was reduced to 60% of the discharge capacity at the 10th cycle was examined. Table 1 shows the results. Also,
When charging with 1A current for 1.2 hours and then discharging with 3A current, 1/2 of the discharge time until the terminal voltage reaches 0.8V
The terminal voltage (discharge intermediate voltage) during the discharge time was examined. The results are also shown in Table 1.
【0036】[0036]
【表1】 表1から、本発明の方法で製造した水素吸蔵電極を用い
る電池Aは、従来の方法で製造した水素吸蔵電極を用い
る電池Bと比較して、充放電サイクル寿命が長いことが
わかる。[Table 1] Table 1 shows that the battery A using the hydrogen storage electrode manufactured by the method of the present invention has a longer charge / discharge cycle life than the battery B using the hydrogen storage electrode manufactured by the conventional method.
【0037】この理由は、次のことにあるものと推察さ
れる。The reason is presumed to be as follows.
【0038】すなわち、従来の方法で製造した水素吸蔵
合金は、Mnが揮発して、水素吸蔵合金の化学量論数が偏
移した結果、充放電サイクルの進行にともなう合金の劣
化速度が増加し、さらに、プラスチックボンデッド電極
では、合金の量が少ないので、この合金の劣化の影響が
顕著にあらわれた。さらに、従来の方法で製造した水素
吸蔵合金にはアルミナが混入していたので、これがアル
カリ電解液に溶解し、正極に到達して、その放電容量が
低下した。That is, in the hydrogen storage alloy manufactured by the conventional method, Mn volatilizes and the stoichiometric number of the hydrogen storage alloy shifts, so that the deterioration rate of the alloy with the progress of the charge / discharge cycle increases. Further, in the case of the plastic bonded electrode, since the amount of the alloy was small, the influence of the deterioration of the alloy was remarkable. Furthermore, since alumina was mixed in the hydrogen storage alloy produced by the conventional method, the alumina was dissolved in the alkaline electrolyte, reached the positive electrode, and its discharge capacity was reduced.
【0039】また、表1から、本発明の方法で製造した
水素吸蔵電極を用いる電池Aは、従来の方法で製造した
水素吸蔵電極を用いる電池Bと比較して、大きい電流で
放電した場合の放電中間電圧が高いことがわかる。Further, from Table 1, it can be seen that the battery A using the hydrogen storage electrode manufactured by the method of the present invention has a larger discharge current than the battery B using the hydrogen storage electrode manufactured by the conventional method. It can be seen that the discharge intermediate voltage is high.
【0040】この原因は次のように推察される。The cause is presumed as follows.
【0041】すなわち、本発明の方法で製造した水素吸
蔵電極は、水素吸蔵合金が強固に焼結されているので、
電極内の電気伝導性に優れている結果、大電流で放電す
る場合の電池の分極が小さくなる。That is, in the hydrogen storage electrode manufactured by the method of the present invention, since the hydrogen storage alloy is firmly sintered,
As a result of the excellent electrical conductivity in the electrodes, the polarization of the battery when discharging with a large current is reduced.
【0042】なお、上述の実施例では、LaNi5 合金の成
分元素の一部を特定の他の元素で置換した水素吸蔵合金
の場合について説明したが、本発明の効果は、TiNi合金
や、Laves 相合金についても、またそれらの成分元素の
一部を他の元素で置換した合金の場合にも、水素吸蔵合
金の合成反応が発熱反応であれば、同様に得られるもの
である。In the above embodiment, the description has been given of the case of the hydrogen storage alloy in which a part of the component elements of the LaNi 5 alloy is replaced with another specific element. However, the effects of the present invention are not limited to the TiNi alloy and the Laves alloy. In the case of a phase alloy and an alloy in which some of the constituent elements are replaced with other elements, the same can be obtained if the synthesis reaction of the hydrogen storage alloy is an exothermic reaction.
【0043】[0043]
【発明の効果】本発明によれば、安価な金属の粉末材料
を成型した圧粉体を反応焼結したものが、そのままで水
素吸蔵電極になるので、大規模な合金溶解炉や、粉末製
造装置を用いる工程が不要になる。According to the present invention, a compact obtained by molding an inexpensive metal powder material by reaction sintering is used as it is as a hydrogen storage electrode. The step of using the device becomes unnecessary.
【0044】それゆえ、合金の溶解工程における炉材か
らの合金の汚染、溶解工程における低融点成分元素の蒸
発による組成の偏移、および粉砕工程におけるミルの材
料による汚染が起こらない。従って、不純物の量が少な
く、しかも組成の偏移が少ない水素吸蔵合金からなる電
極が得られる。さらに、合金材料を加熱して溶解する工
程を経ることなく、反応熱のみによって水素吸蔵合金の
合成が起こるので、電極の製造に要するエネルギが著し
く少なくて済む。そして、得られる電極は水素吸蔵合金
の焼結体であるから、電極の電気抵抗が小さくなり、電
池の内部抵抗が小さくなって、電池を大電流で放電する
際の分極が小さくなる。Therefore, the contamination of the alloy from the furnace material in the melting step of the alloy, the shift of the composition due to the evaporation of the low melting point component element in the melting step, and the contamination of the mill material in the grinding step do not occur. Accordingly, an electrode made of a hydrogen storage alloy having a small amount of impurities and a small composition shift can be obtained. Furthermore, since the synthesis of the hydrogen storage alloy occurs only by the reaction heat without the step of heating and melting the alloy material, the energy required for manufacturing the electrode can be significantly reduced. Since the obtained electrode is a sintered body of a hydrogen storage alloy, the electric resistance of the electrode is reduced, the internal resistance of the battery is reduced, and the polarization when the battery is discharged with a large current is reduced.
【図1】自己伝播反応焼結が進行して水素吸蔵電極が製
造されている途中の圧粉体の状態を示した図。FIG. 1 is a view showing a state of a green compact during the production of a hydrogen storage electrode by progress of self-propagating reaction sintering.
1 未反応の圧粉体 2 反応が終わった水素吸蔵合金の焼結体 3 反応焼結ゾーン 4 ニクロム線 1 Unreacted green compact 2 Sintered body of hydrogen storage alloy after reaction 3 Reaction sintering zone 4 Nichrome wire
Claims (1)
る材料金属粉末を混合した圧粉体を作成し、次いで真空
中もしくは非酸化性雰囲気中で該圧粉体に着火して自己
伝播反応焼結させることを特徴とする水素吸蔵電極の製
造方法。1. A green compact is prepared by mixing a metal powder which generates heat during a reaction for synthesizing a hydrogen storage alloy, and then ignites the green compact in a vacuum or a non-oxidizing atmosphere to cause self-propagation. A method for producing a hydrogen storage electrode, comprising performing reaction sintering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP08078591A JP3185151B2 (en) | 1991-03-18 | 1991-03-18 | Hydrogen storage alloy for hydrogen storage electrode and method for producing hydrogen storage electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP08078591A JP3185151B2 (en) | 1991-03-18 | 1991-03-18 | Hydrogen storage alloy for hydrogen storage electrode and method for producing hydrogen storage electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04289660A JPH04289660A (en) | 1992-10-14 |
| JP3185151B2 true JP3185151B2 (en) | 2001-07-09 |
Family
ID=13728104
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP08078591A Expired - Fee Related JP3185151B2 (en) | 1991-03-18 | 1991-03-18 | Hydrogen storage alloy for hydrogen storage electrode and method for producing hydrogen storage electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3185151B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4895414B2 (en) * | 1998-07-03 | 2012-03-14 | 東洋アルミニウム株式会社 | Combustion synthesizer |
-
1991
- 1991-03-18 JP JP08078591A patent/JP3185151B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04289660A (en) | 1992-10-14 |
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