JPH04110403A - Manufacture of hydrogen storage alloy electrode - Google Patents
Manufacture of hydrogen storage alloy electrodeInfo
- Publication number
- JPH04110403A JPH04110403A JP2229060A JP22906090A JPH04110403A JP H04110403 A JPH04110403 A JP H04110403A JP 2229060 A JP2229060 A JP 2229060A JP 22906090 A JP22906090 A JP 22906090A JP H04110403 A JPH04110403 A JP H04110403A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- storage alloy
- battery
- hydrogen
- water
- 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
- 239000000956 alloy Substances 0.000 title claims abstract description 100
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 99
- 239000001257 hydrogen Substances 0.000 title claims abstract description 92
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 92
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 87
- 238000003860 storage Methods 0.000 title claims abstract description 83
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 229910052751 metal Inorganic materials 0.000 claims abstract description 20
- 239000002184 metal Substances 0.000 claims abstract description 20
- 239000000843 powder Substances 0.000 claims abstract description 17
- 238000010298 pulverizing process Methods 0.000 claims abstract description 13
- 239000007853 buffer solution Substances 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims abstract description 9
- 229910000000 metal hydroxide Inorganic materials 0.000 claims abstract description 6
- 150000004692 metal hydroxides Chemical class 0.000 claims abstract description 6
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 4
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 4
- 150000004679 hydroxides Chemical class 0.000 claims description 6
- 150000002739 metals Chemical class 0.000 claims description 4
- 238000006722 reduction reaction Methods 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 8
- 230000033116 oxidation-reduction process Effects 0.000 abstract description 3
- -1 beforehand Substances 0.000 abstract description 2
- 238000006479 redox reaction Methods 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 239000011259 mixed solution Substances 0.000 description 5
- 229910052759 nickel Inorganic materials 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 3
- 235000019796 monopotassium phosphate Nutrition 0.000 description 3
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 3
- RQALKBLYTUKBFV-UHFFFAOYSA-N 1,4-dioxa-7-thiaspiro[4.4]nonane Chemical compound O1CCOC11CSCC1 RQALKBLYTUKBFV-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- KRFJLUBVMFXRPN-UHFFFAOYSA-N cuprous oxide Chemical compound [O-2].[Cu+].[Cu+] KRFJLUBVMFXRPN-UHFFFAOYSA-N 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052987 metal hydride Inorganic materials 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- SFKTYEXKZXBQRQ-UHFFFAOYSA-J thorium(4+);tetrahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[Th+4] SFKTYEXKZXBQRQ-UHFFFAOYSA-J 0.000 description 2
- XDVOLDOITVSJGL-UHFFFAOYSA-N 3,7-dihydroxy-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical compound O1B(O)OB2OB(O)OB1O2 XDVOLDOITVSJGL-UHFFFAOYSA-N 0.000 description 1
- GDTSJMKGXGJFGQ-UHFFFAOYSA-N 3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical compound O1B([O-])OB2OB([O-])OB1O2 GDTSJMKGXGJFGQ-UHFFFAOYSA-N 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-M dihydrogenphosphate Chemical compound OP(O)([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-M 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910021508 nickel(II) hydroxide Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- IWZKICVEHNUQTL-UHFFFAOYSA-M potassium hydrogen phthalate Chemical compound [K+].OC(=O)C1=CC=CC=C1C([O-])=O IWZKICVEHNUQTL-UHFFFAOYSA-M 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 238000005303 weighing 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
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
言i花」二の」牛用づと堅
本発明は、金属−水素アルカリ蓄電池の偵極乙;二用い
られる水素吸蔵合金電極の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a hydrogen storage alloy electrode used in a metal-hydrogen alkaline storage battery.
j岨支Ji
近年、二・シヶルーカトミウム電池に代わる新型アルカ
リ蓄電池として、ニノヶルー力1′ミウム電池より高エ
ネルギー密度化が可能な金属−水素アルカリ蓄電池が注
目されている。そして、この電池の負極としては水素吸
蔵合金か用いられている。In recent years, metal-hydrogen alkaline storage batteries have been attracting attention as a new type of alkaline storage battery to replace the Ni-Sigal 1'mium battery, which can have a higher energy density than the Ni-Sigal 1'mium battery. A hydrogen storage alloy is used as the negative electrode of this battery.
ところで、上記水素吸蔵合金の製造方法としては、一般
に、水素吸蔵合金材料を溶解、ン名却し“ζ水素吸蔵合
金鋳塊を作製する二[程と、この水素吸蔵合金鋳塊を水
中で粉砕して水素吸蔵合金粉末を1乍製する二[不呈と
を有している。By the way, the method for producing the above-mentioned hydrogen storage alloy generally involves two steps: melting the hydrogen storage alloy material, producing a hydrogen storage alloy ingot, and pulverizing the hydrogen storage alloy ingot in water. The hydrogen-absorbing alloy powder is prepared by the following steps:
が′″゛ しようとずろ
しかしながら、上記従来の製造方法の如く水素吸蔵合金
鋳塊を水中で粉砕すると、水素吸蔵合金の成分が若干水
中に溶出し、水溶液が弱アルカリ性(p l−18〜1
0)となる。このようなアルカリ性の溶液中では、水素
吸蔵合金を構成する金属の殆どが水酸化物どなる<Iη
域であるため、水素吸蔵合金の酸化還元電位と等しい電
位、又はより貴な電位に保たれている部分か活性点とな
って、水素吸蔵合金の表面に水酸化物の皮膜が形成され
ることになる。この結果、初期特性や急速充電特性が低
下するという課題を有していた。However, when the hydrogen storage alloy ingot is crushed in water as in the conventional manufacturing method described above, some of the hydrogen storage alloy components are eluted into the water, and the aqueous solution becomes weakly alkaline (p l-18 to 1).
0). In such an alkaline solution, most of the metals constituting the hydrogen storage alloy become hydroxides <Iη
Since the hydrogen storage alloy is in the oxidation-reduction potential, the parts that are kept at a potential equal to or more noble can become active sites and form a hydroxide film on the surface of the hydrogen storage alloy. become. As a result, there was a problem in that initial characteristics and rapid charging characteristics deteriorated.
本発明はかかる現状に鑑みてなされたものであり、初7
11特性や急速充電特性を向上させ」士ることかてきる
水素吸蔵合金電極の製造方法を提供することを目的とす
る。The present invention was made in view of the current situation, and is the first 7
The object of the present invention is to provide a method for manufacturing a hydrogen storage alloy electrode that can improve 11 characteristics and rapid charging characteristics.
、BL彫布邂訣t、2い覧Δ−9手段
本発明は上記目的を達成するために、水素吸蔵合金鋳塊
を水素発生電位に保持しつつ、水中で粉砕、または粉砕
、保存して水素吸蔵合金粉末を作製するステップを有す
ることを特徴とする。In order to achieve the above object, the present invention crushes or crushes and stores a hydrogen storage alloy ingot in water while maintaining it at a hydrogen generation potential. The method is characterized by comprising a step of producing a hydrogen storage alloy powder.
尚、水素吸蔵合金鋳塊を水素発生電位に保持する具体的
な方法としては、以下に来場−3つの方法がある。There are three specific methods for maintaining the hydrogen storage alloy ingot at a hydrogen generation potential:
■水素吸蔵合金鋳塊を水中粉砕する前に、合金鋳塊に水
素を吸蔵さ艮る。■Before crushing the hydrogen-absorbing alloy ingot in water, the alloy ingot is made to absorb hydrogen.
■水素吸蔵合金鋳塊を水中粉砕する前に、合金υf塊を
充電状態にしておく。■Before crushing the hydrogen storage alloy ingot in water, keep the alloy υf ingot in a charged state.
■水素吸蔵合金鋳塊を充電状態に保J=6しつつ、合金
鋳塊を粉砕する。■While maintaining the hydrogen storage alloy ingot in a charged state at J=6, crush the alloy ingot.
また、水素吸蔵合金鋳塊を水中で粉砕、または粉砕、保
存するステップを有する水素吸蔵合金電極の製造方法に
おいて、前記水には、予め、前記水素吸蔵合金を構成ず
ろ金属、又は1での金属の酸化物、水酸化物が協力■]
されていることを特徴とする。In addition, in the method for manufacturing a hydrogen storage alloy electrode, which includes the step of crushing or crushing and storing a hydrogen storage alloy ingot in water, the water contains in advance a hydrogen storage alloy constituting the hydrogen storage alloy, or the metal in step 1. The oxides and hydroxides cooperate ■]
It is characterized by being
尚、具体的には、水素吸蔵合金として
L a N i 、を用いる場合は、Niを水に添加ず
れば良い。Specifically, when L a N i is used as the hydrogen storage alloy, Ni may be added to water.
また、水素吸蔵合金鋳塊を水中で粉砕、または粉砕、保
存するステップを有する水素吸蔵合金電極の製造方法に
おいて、前記水には、予め、前記水素吸蔵合金を構成す
る金属の水酸化物の酸化還元電位より貴な電位で酸化、
還元反応を生しる金属、金属酸化物、或いは金属水酸化
物が添加されていることを特徴とする。Further, in the method for manufacturing a hydrogen storage alloy electrode, which includes the step of crushing or crushing and storing a hydrogen storage alloy ingot in water, the water contains oxidized hydroxides of metals constituting the hydrogen storage alloy in advance. oxidation at a potential more noble than the reduction potential,
It is characterized by the addition of a metal, metal oxide, or metal hydroxide that causes a reduction reaction.
尚、具体的には、水素吸蔵合金として
り、、 a N + 5を用いる場合は、Cu2O等を
水に添(川1れば良い。Specifically, when using aN + 5 as a hydrogen storage alloy, Cu2O or the like is added to water (just 1 liter is sufficient).
更に、水素吸蔵合金鋳塊を、p Hを一定に保つ緩衝溶
液中で粉砕、または粉砕、保存して水素吸蔵合金粉末を
作製するステップを有することを特徴とする。Furthermore, the present invention is characterized by having a step of producing a hydrogen-absorbing alloy powder by pulverizing or pulverizing and storing the hydrogen-absorbing alloy ingot in a buffer solution that keeps the pH constant.
一制−−用
上記第1発明の製造方法の如く、水素吸蔵合金鋳塊を水
素発生電位b=保持しつつ、水中で粉砕すれは、水素吸
1代合金の主成分であるNiやCOの電(r、iか水酸
化物になる釘1域に入ることがない。したがって、Ni
等が金属状態に保たれた状態で水素吸蔵合金粉末となる
。したがって、合金表面には、NiやCoの活性点が十
分に存在するごとになる。As in the manufacturing method of the first invention, the hydrogen absorbing alloy ingot is crushed in water while maintaining the hydrogen generation potential b = Ni and CO, which are the main components of the hydrogen absorbing alloy, are Ni (r, i) does not enter the nail region 1 where it becomes hydroxide.
etc. remain in a metallic state and become a hydrogen-absorbing alloy powder. Therefore, there are sufficient active sites of Ni and Co on the alloy surface.
上記第2発明及び第3発明の如く1、水中粉砕或いは水
中保存時に、水素吸蔵合金を構成する金属の水酸化物の
酸化還元電位と同等若しくは貴な電位で酸化、還元反応
を生じる金属、金属酸化物、或いは金属水酸化物を予め
水中に投入しておりば、水素吸蔵合金表面以外に活性点
となる部位が存在することになる。これにより、合金成
分の水酸化物が投入金属等の表面に析出することになる
ので、水素吸蔵合金粉末表面に水酸化物かへ(構成する
のを抑制することが可能となる。したがって、合金表面
には、活性点が十分に存在することになる。As in the above-mentioned second and third inventions, 1. A metal or metal that undergoes an oxidation or reduction reaction at a potential equal to or nobler than the oxidation-reduction potential of the metal hydroxide constituting the hydrogen storage alloy when crushed or stored in water; If the oxide or metal hydroxide is added to the water in advance, there will be sites other than the surface of the hydrogen storage alloy that will become active sites. As a result, the hydroxide of the alloy component will precipitate on the surface of the input metal, etc., so it is possible to suppress the formation of hydroxide on the surface of the hydrogen storage alloy powder. There will be sufficient active sites on the surface.
上記第4発明の如く、水溶液の91丁を一定に保つ緩衝
溶液中で水素吸蔵合金鋳塊を粉砕ずれは、水素吸蔵合金
の主成分であるNiやCOが水酸化物とならす、金属状
態に保たれ]こ状態て水素吸蔵合金粉末となる。したが
って1、合金表面には、活地点が十分に存在するごとに
なる。As in the fourth invention, when the hydrogen storage alloy ingot is crushed in a buffer solution in which the aqueous solution is kept constant, Ni and CO, which are the main components of the hydrogen storage alloy, become hydroxides and become metallic. In this state, it becomes a hydrogen-absorbing alloy powder. Therefore, 1. There are enough active points on the alloy surface.
)(↓j辷助1列−
本発明の第1実施例を、第1図及び第2図に暴ついて、
以下に説明する。) (↓J 1 line - The first embodiment of the present invention is revealed in FIGS. 1 and 2,
This will be explained below.
第1図は本発明により作製した水素吸蔵合金電極を用い
た円筒型ニッケルー水素アルカリ蓄電池の断面図であり
、焼結式ニッケルから成る正極1と、水素吸蔵合金を含
む負極2と、これら正負両極12間に介挿されたセパレ
ータ3とから成る電極J!Y 4は渦巻状に巻回されて
いる。この電極群4は負極端子兼用の外装j耀6内に配
置されており、この外装端6と」正妃負極2どは負極用
導電タブ5により接続されている。」−記外装罐6の上
部開口にはバッキング7を介して封口体8が装着されて
おり、この封口体8の内部にはコイルスプリング9が設
iJられている。このコイルスプリング9は電池内部の
内圧が異常上昇したときに矢印入方向に押圧されて内部
のガスが大気中に放出されるよ・うに構成されている。FIG. 1 is a cross-sectional view of a cylindrical nickel-hydrogen alkaline storage battery using hydrogen storage alloy electrodes produced according to the present invention, showing a positive electrode 1 made of sintered nickel, a negative electrode 2 containing a hydrogen storage alloy, and both positive and negative electrodes. 12 and a separator 3 inserted between the electrodes J! Y4 is spirally wound. This electrode group 4 is arranged in an exterior casing 6 which also serves as a negative electrode terminal, and the exterior end 6 and the positive and negative electrodes 2 are connected by a conductive tab 5 for the negative electrode. A sealing body 8 is attached to the upper opening of the exterior can 6 via a backing 7, and a coil spring 9 is installed inside the sealing body 8. This coil spring 9 is configured so that when the internal pressure inside the battery rises abnormally, it is pressed in the direction of the arrow and the internal gas is released into the atmosphere.
また、」正妃封ロ体8と前記正極1とは正極用導電タブ
10にて接続されている。Furthermore, the positive electrode 1 is connected to the positive electrode 1 by a conductive tab 10 for the positive electrode.
ここで、」正妃構造の円筒型ニッケルー水素アルカリ蓄
電池を、以下のようにして作製した。Here, a cylindrical nickel-metal hydride alkaline storage battery with a ``Fuji'' structure was fabricated as follows.
先ず、市販の1.aとNiとを元素比で1:5の割合と
なるよ・うに秤量した後、高周波溶解炉内で溶解して溶
湯を作成し、更にごの溶湯を冷却することにより、L
a N i 、で示される水素吸蔵合金鋳塊を作成した
。次に、この水素吸蔵合金鋳塊に、合金1g6に対して
10ccだけ水素を吸蔵させた。First, commercially available 1. After weighing a and Ni so that the elemental ratio is 1:5, melting is performed in a high frequency melting furnace to create a molten metal, and by further cooling the molten metal, L
A hydrogen storage alloy ingot represented by a N i was prepared. Next, this hydrogen storage alloy ingot was allowed to store 10 cc of hydrogen per 1g6 of the alloy.
しかる後、」正妃水素吸蔵合金鋳塊の粒径が50μm以
下となるよ・う、水中で4時間粉砕を行った。Thereafter, the ingot of the hydrogen storage alloy was crushed in water for 4 hours so that the particle size of the ingot was 50 μm or less.
この際、水素吸蔵合金鋳塊11くgに対して、水が5℃
となるように設定している。At this time, water was added at 5℃ for 11g of hydrogen storage alloy ingot.
It is set so that
この後、上記水素吸蔵合金粉末に、結着剤としてのPT
FE(ポリテトラフルオロエチレン)粉末を5w45%
加えて混練し、ベースI・を作成する。After this, PT as a binder is added to the hydrogen storage alloy powder.
FE (polytetrafluoroethylene) powder 5w45%
Add and knead to create Base I.
更に、このペーストをパンチングメタルから成る集電体
の両面に圧着して負極2を作製した。Furthermore, this paste was pressed onto both sides of a current collector made of punched metal to produce a negative electrode 2.
次いで、上記負極2と、この負極2よりも十分容量が大
きな焼結式二・ンケル正極1とを、不織布からなるセパ
レータ3を介して巻回し、電極群4を作製した。しかる
後、この電極群4を外装端6内に挿入し、更に30重量
%のK OH水溶液を上記外装端6内に汁液した後、外
装端6を密閉することにより円筒型ニンケルー水素蓄電
池を作製した。尚、このようにして作製した電池の1′
!I!論容量は、1.000mA、hである。Next, the negative electrode 2 and the sintered two-layer positive electrode 1 having a sufficiently larger capacity than the negative electrode 2 were wound together with a separator 3 made of nonwoven fabric interposed therebetween, to produce an electrode group 4. Thereafter, this electrode group 4 was inserted into the exterior end 6, and after a 30% by weight KOH aqueous solution was poured into the exterior end 6, the exterior end 6 was sealed to produce a cylindrical Ninkeru hydrogen storage battery. did. In addition, 1' of the battery thus produced
! I! The theoretical capacity is 1.000 mA, h.
とのよ・うにして作製した電池を、以下(A1)電池と
称する。The battery prepared in the above manner is hereinafter referred to as (A1) battery.
〔実施例■]
水素吸蔵合金鋳塊の粉砕前の処理として、水素を吸蔵さ
1士という処理ではなく、水素吸蔵合金鋳塊を予備充電
するという処理を施す他は、−に記実施例Iと同様ルに
して電池を作製した。尚、予備充電量は、水素吸蔵合金
1gに対して20mAである。[Example ■] Example I described in - except that the treatment before crushing the hydrogen storage alloy ingot was not to absorb hydrogen but to pre-charge the hydrogen storage alloy ingot. A battery was fabricated in the same manner as above. Note that the preliminary charge amount is 20 mA per 1 g of hydrogen storage alloy.
このようにして作製した電池を、以下(A、〕電池と称
する。The battery thus produced is hereinafter referred to as (A) battery.
(実施例■[〕
水素吸蔵合金鋳塊の粉砕前の処理を施さず、水素吸蔵合
金1gに対し−で5 rn△の電流を流しつつ粉砕する
他は、上記実施例■と同様にして電池をイ乍製 し ノ
こ。(Example ■[] A battery was produced in the same manner as in Example ■ above, except that the hydrogen storage alloy ingot was not subjected to any pre-pulverization treatment and was crushed while applying a current of -5 rn△ to 1 g of hydrogen storage alloy. I made the saw.
このよ・うにして作製した電池を、以下(All)電池
と称する。The battery thus produced is hereinafter referred to as an (All) battery.
水素吸蔵合金鋳塊の粉砕前の処理を施すことな(粉砕す
る他は、上記実施例■と同様にして電池を作製した。A battery was produced in the same manner as in Example 2 above, except that the hydrogen storage alloy ingot was not subjected to any pre-pulverization treatment (other than pulverization).
このようにして作製した電池を、以下(X)電池と称す
る。The battery thus produced is hereinafter referred to as the (X) battery.
」正妃本発明の製造方法による(A1)電池〜(△、)
電池、及び比較例の製造方法による(X)電池の酸素濃
度と初期容量と電池内圧とを測定したので、その結果を
下記第1表に示ず。尚、初)υ1容量ば、充電電流0.
3Cで4時間充電し、放電型:/A0.3Cで放電終市
電圧10■まで放電するというサイクルを5回繰り返し
た後の容量である。また、電池内圧は、ICで1
電した際の圧力である。” (A1) Battery by the manufacturing method of the present invention ~ (△,)
The oxygen concentration, initial capacity, and battery internal pressure of the battery and the battery (X) manufactured by the manufacturing method of Comparative Example were measured, and the results are not shown in Table 1 below. In addition, if the capacity is υ1, the charging current is 0.
This is the capacity after repeating the cycle of charging at 3C for 4 hours and discharging at /A 0.3C to a final discharge voltage of 10cm five times. In addition, the battery internal pressure is the pressure when one electric current is applied to the IC.
第1表
2時間光
・合金酸素濃度について
上記第1表に示すように、本発明の製造方法による(A
1)電池〜(A、)電池では0132〜0.35%であ
って非常に低くなっているのに対して、比較例の製造方
法による(X)電池では]50%と高くなっていること
が認められる。Table 1 Regarding 2-hour light and alloy oxygen concentration As shown in Table 1 above, (A
1) Battery - (A,) battery has a very low value of 0.132 to 0.35%, whereas the comparative example (X) battery manufactured using the manufacturing method has a high value of 50%. is recognized.
初1u1容量について
」正妃第1表に示すように、(A1)電池〜(A、)電
池でば略]、 (] 20 mAhであって非常に大き
くなっているのに対して、(X)電池では950m^h
と小さくなっていることがa忍められる。As shown in Table 1 of ``Regarding the initial 1u1 capacity'', (A1) battery to (A,) battery is very large, 20 mAh, while (X ) 950 m^h with batteries
The fact that it is so small is tolerable.
・電池内圧について
」正妃第1表に示すように、(/\1)電池〜(△、l
)電池ては5.1〜5.3al、mてあ、って非常に低
くなっているのに対して、(X)電池では]5]、at
、mと高くなっていることが認められる。・About battery internal pressure" As shown in Table 1, (/\1) battery ~ (△, l
) battery has a very low value of 5.1 to 5.3al, mtea, while (X) battery has ]5], at
, m.
このよ・うに本発明の(A1)電池〜(A、i)電池が
、合金酸素濃度、初期容量及び電池内圧の点で優れてい
るのは、第2図に示すよ・うに、p I(8〜IOの範
囲においては、水素発生電位(図中りで示す)でばN】
は水酸化物とはならず金属Nの状態となっている。した
がって、上記の如く水素吸蔵合金鋳塊を水素発生電位に
保ちつつ粉砕すれば、水素吸蔵合金粉末の表面には
Ni(○■1)2が生成することがないとい・う理由に
よるものと考えられる。As shown in FIG. 2, the (A1) to (A,i) batteries of the present invention are superior in terms of alloy oxygen concentration, initial capacity, and battery internal pressure. In the range of 8 to IO, the hydrogen generation potential (shown in the figure) is N]
does not become a hydroxide but is in the state of metal N. Therefore, it is thought that the reason is that if the hydrogen-absorbing alloy ingot is crushed while maintaining the hydrogen-generating potential as described above, Ni(○■1)2 will not be generated on the surface of the hydrogen-absorbing alloy powder. It will be done.
第1演1貫
〔実施例■]
水素吸蔵合金鋳塊の粉砕前にごの鋳塊の処理を施すので
はなく、粉砕する水内に予め
] 1
Ni(OH)2を100g投入するような処理を施す他
は、前記第1実施例の実施例Iと同様にして電池を作製
した。Part 1 [Example ■] Instead of treating the hydrogen storage alloy ingot before crushing it, we added 100g of Ni(OH)2 to the water to be crushed in advance. A battery was produced in the same manner as in Example I of the first example except for the treatment.
このようにして作製した電池を、以下(B1)電池と称
する。The battery thus produced is hereinafter referred to as (B1) battery.
[実力面倒■]
N ] (01() 2の代わりに、Cu、0を10
0g投入する他は、上記の実施例■と同様にして電池を
作製した。[Troublesome ability ■] N ] (01 () Instead of 2, Cu, 0 to 10
A battery was produced in the same manner as in Example 2 above, except that 0 g was added.
このようにして作製した電池を、以下(B2)電池と称
する。The battery thus produced is hereinafter referred to as a (B2) battery.
[比較例]
比較例としては、上記第1実施例の(X)電池を用いて
いる。[Comparative Example] As a comparative example, the battery (X) of the first example is used.
[実験]
一ヒ記木発明の製造方法による(B、)電池(B2)電
池、及び比較例の製造方法による(χ)電池の酸素濃度
と初311容量と電池内圧とを測定したので、その結果
を下記第2表に示す。尚、実験条件は、上記第1実施例
の実験と同一条件である。[Experiment] The oxygen concentration, initial capacity, and battery internal pressure of the (B) battery (B2) battery manufactured by the manufacturing method of Ichihiki's invention and the (χ) battery manufactured by the manufacturing method of the comparative example were measured. The results are shown in Table 2 below. The experimental conditions were the same as those of the first embodiment.
第2表
・合金酸素濃度について
上記第2表に示すように、本発明の製造方法による(B
1)電池、(B2)電池では、それぞれ0.77.0.
65%であって低くなっているのに対して、比較例の製
造方法による(X)電池では1.5%と高くなっている
ことが認められる。Table 2 - Alloy Oxygen Concentration As shown in Table 2 above, (B
1) battery and (B2) battery, each has a value of 0.77.0.
It is recognized that the ratio is low at 65%, whereas it is high at 1.5% in the battery (X) produced by the manufacturing method of the comparative example.
初jUl容量について
上記第2表に示すように、(B1)電池、 (B、)
電池では、それぞれ990,10(17mAhであって
大きくなっているのに対して、(X)電池では950m
Ahと小さくなっていることが認められる。As shown in Table 2 above regarding the initial jUl capacity, (B1) battery, (B,)
The batteries are 990 and 10 (17mAh), which are larger, while the (X) batteries are 950mA.
It is recognized that the value is smaller than Ah.
電池内圧について
」正妃第2表に示すように、(B1)電池、 (B、
)電池では、それぞれ7.7.6.3almであって低
くなっているのに対して、(X)電池では]、5.1a
l、mと高くなっていることが許忍められる。As shown in Table 2 of "About battery internal pressure", (B1) battery, (B,
) battery, the values are 7.7, 6.3 alm, respectively, which are lower, whereas for the (X) battery], 5.1a
It is acceptable that the values are as high as l and m.
このように本発明の(B1)電池、(B2)電池が、合
金酸素a度、期間容量及び電池内圧の点で優れているの
は、第3図に示すように、p I(8〜10の範囲(図
中ではp H9としている)においては、CIi *
C: u 20となるE/VはNi(○l−1)2の領
域となる。したがって、上記の如(Cu20等を予め粉
砕する水中に投入しておけば、生成したNi(○J1)
2がCuz Oの表面に析出するため、水素吸蔵合金粉
末表面におけるN i (OH) 2の生成が抑制さ
れるという理由によるものと考えられる。As shown in FIG. 3, the (B1) battery and (B2) battery of the present invention are excellent in terms of alloy oxygen a degree, period capacity, and battery internal pressure. In the range of (pH 9 in the figure), CIi *
C: E/V of u 20 is in the area of Ni(○l-1)2. Therefore, if Cu20 etc. are placed in the water to be crushed in advance as described above, the generated Ni(○J1)
This is thought to be due to the fact that the formation of N i (OH) 2 on the surface of the hydrogen storage alloy powder is suppressed because 2 precipitates on the surface of Cuz O.
第3」ΩU−
(実施例I]
水素吸蔵合金鋳塊の粉砕前にこの鋳塊の処理を施すこと
なく、且つ粉砕溶液として水ではなく緩衝溶液(0,I
N酢酸: 0.1 moff / 12酢酸すトリウム
−4:1であってp I−T−4)を用いる他は、前記
第1実施例の実施例Iと同様にして電池を作製した。3rd ΩU- (Example I) The hydrogen storage alloy ingot was not treated before being crushed, and the crushing solution was a buffer solution (0, I) instead of water.
A battery was produced in the same manner as in Example I of the first example, except that N acetic acid: 0.1 moff/12 sodium acetate (4:1, p I-T-4) was used.
このようにして作製した電池を、以下(C4)電池と称
する。The battery thus produced is hereinafter referred to as a (C4) battery.
(実施例■〕
緩衝溶液として、0.1N酢酸+O,imoρ/℃酢酸
すトリウム−1: 2 (pH−5)を用いる他は、」
正妃の実施例Iと同様にして電池を作製(〜た。(Example ■) Except for using 0.1N acetic acid + O, imoρ/℃ strium acetate-1:2 (pH-5) as the buffer solution.
A battery was prepared in the same manner as in Example I of Seihi.
ごのよ・うにして作製した電池を、以下(C2)電池と
称する。The battery produced in this manner is hereinafter referred to as a (C2) battery.
〔実施例■]
緩衝溶液として、0.〕N酢M : 0.1. mo℃
/!酢酸ナトリウム−1:16(pト■−6)を用いる
他は、上記の実施例Iと同様にして電池を作製した。[Example ■] As a buffer solution, 0. ]N vinegar M: 0.1. mo℃
/! A battery was prepared in the same manner as in Example I above, except that sodium acetate-1:16 (pt-6) was used.
このようにして作製した電池を、以下(C3)電池と称
する。The battery thus produced is hereinafter referred to as a (C3) battery.
〔実施例■]
緩衝溶液として、0.03mo r!、/ f!、 ’
Jン酸二水素カG
ノウム: 0.03mo 、+2 / 1水酸化ナトリ
ウム−1:2(p l(= 7 )を用いる他は、−上
記の実施例Iと同様にして電池を作製した。[Example ■] As a buffer solution, 0.03 molar! ,/f! ,'
A battery was prepared in the same manner as in Example I above, except that 0.03 mo of potassium dihydrogen phosphate, +2/1 sodium hydroxide, 1:2 (p l (=7)) was used.
このようにして作製した電池を、以下(C4)電池と称
する。The battery thus produced is hereinafter referred to as a (C4) battery.
[実施例IV)
緩衝溶液として、0 、03mo℃/!リン酸二水素カ
リウム二0.03mo、e/ffi水酸化ナトリウム−
1:16(pH−8)を用いる他は、上記の実施例Iと
同様にして電池を作製した。[Example IV] As a buffer solution, 0,03mo°C/! Potassium dihydrogen phosphate di0.03mo, e/ffi Sodium hydroxide-
A battery was prepared in the same manner as in Example I above, except that 1:16 (pH-8) was used.
このよ・うにして作製した電池を、以下(C1)電池と
称する。The battery thus produced is hereinafter referred to as a (C1) battery.
比較例としては、上記第1実施例の(X)電池を用いて
いる。As a comparative example, the battery (X) of the first embodiment is used.
」正妃木発明の製造方法による(CI )電池〜(C5
)電池、及び比較例の製造方法による(X)電池の酸素
濃度と切刃1容量と電池内圧とを測定したので、その結
果を下記第3表に示す。尚、実験条件は、上記第1実施
例の実験と同一条件である。” (CI) battery by the manufacturing method invented by Shohiki ~ (C5
The oxygen concentration, capacity per cutting edge, and internal pressure of the battery were measured for the battery (X) manufactured by the manufacturing method of Comparative Example, and the results are shown in Table 3 below. The experimental conditions were the same as those of the first embodiment.
第3表
・合金酸素濃度について
」正妃第3表に示すように、本発明の製造方法による(
C1)電池〜(C5)電池では、0.35〜0.39%
であって非常に低くなっているのに対して、比較例の製
造方法による(χ)電池では1.50%と高くなってい
ることが認められる。Table 3: Alloy Oxygen Concentration As shown in Table 3, the manufacturing method of the present invention (
For C1) batteries to (C5) batteries, 0.35 to 0.39%
, which is extremely low, whereas it is recognized that the (χ) battery produced by the manufacturing method of the comparative example has a high value of 1.50%.
・初期容量について
上記第3表に示すよ・うに、(C,)電池〜(C、)電
池では、1012〜1020mAhであって非常に大き
くなっているのに対して、(X)電池ては950mAh
と小さ(なっていることが認められる。- Regarding the initial capacity, as shown in Table 3 above, the (C,) to (C,) batteries have a very large initial capacity of 1012 to 1020 mAh, while the (X) battery has a very large initial capacity. 950mAh
It is recognized that it is small.
・電池内圧について
上記第3表に示すように、(C+ )電池〜(C6)電
池では、5.1〜5.5al:mであって非常に低くな
っているのに対して、(X)電池では15、 ]、a
imと高くなっていることが田忍められる。- Regarding battery internal pressure, as shown in Table 3 above, for (C+) to (C6) batteries, it is 5.1 to 5.5 al:m, which is very low, whereas (X) For batteries, 15, ], a
I can't help but notice that I'm getting taller.
このように本発明の(C,)電池〜(C6)電池が、合
金酸素濃度、初)u1容量及び電池内圧の点で(憂れて
いるのは、本発明に用いる緩fffii溶液はpi−1
を一定に保つことができるので、水素吸蔵合金の主成分
であるNiやCoが粉砕時に水酸化物とならず、金属状
態を維持したままで水素吸蔵合金粉末となるとい・う理
由によるものと考えられる。As described above, the (C,) battery to (C6) battery of the present invention has problems in terms of alloy oxygen concentration, initial) u1 capacity, and battery internal pressure. 1
This is because Ni and Co, which are the main components of the hydrogen storage alloy, do not turn into hydroxides during crushing, but instead maintain their metallic state and become hydrogen storage alloy powder. Conceivable.
■」−記3つの実施例では水素吸蔵合金鋳塊の粉砕時を
例にとって説明したが、保存時でも同様の効果を有する
ことをTuft L?l!、している。■''-Note: In the three examples, explanations were given using the crushing of a hydrogen-absorbing alloy ingot, but Tuft L.? l! ,are doing.
■上記第2実施例では、水中に投入する金属として、N
1(OF+)2やCu2Oを用いたが、これに限定する
ものではなく、水素吸蔵合金の種類に応じて各種の金属
、金属酸化物、金属水酸化物を用いることが可能である
。■In the second embodiment above, N is used as the metal to be thrown into the water.
Although 1(OF+)2 and Cu2O are used, the present invention is not limited thereto, and various metals, metal oxides, and metal hydroxides can be used depending on the type of hydrogen storage alloy.
■−上記第3実施例に用いる緩衝溶液としては」二連し
たものに限定するものではなく、例えば、フタル酸水素
カリウムと水酸化すトリウムとの混合溶液(p H4〜
6に設定可能)、クエン酸二水素カリウムと水酸化すト
リウムとの混合溶液(p I−14〜6に設定可能)、
クエン酸二水素カリウムと四ホウ酸すI・すγシムどの
混合溶液(pH4〜6に設定可能)、リン酸二水素カリ
ウムと四ホラ酸すI〜ゾリウムの混合溶液(pH6〜8
に設定可能)、リン酸水素二す[・リウムとクエン酸と
の混合溶液(p I(4〜Bに設定可能)、1Jン酸二
水素カリウムと水酸化ナトリウムとの混合溶液(p J
(Ei〜8に設定可能)等であっても良い。(2) The buffer solution used in the third embodiment is not limited to two series, but for example, a mixed solution of potassium hydrogen phthalate and thorium hydroxide (pH 4~
6), a mixed solution of potassium dihydrogen citrate and thorium hydroxide (p I-14 to 6),
A mixed solution of potassium dihydrogen citrate and sulfuric acid and zolium tetraborate (pH can be set to 4 to 6), a mixed solution of potassium dihydrogen phosphate and sulfuric acid to zolium tetraboric acid (pH 6 to 8)
), a mixed solution of dihydrogen phosphate and citric acid (p
(Can be set to Ei to 8).
■上記3つの実施例Qこおいては円筒型の蓄電池を用い
ているが、本発明は偏平型の蓄電池にも適応] 9
しうろことは勿論である。■Although a cylindrical storage battery is used in the above three embodiments Q, the present invention is also applicable to a flat storage battery.
光ユ夏熟来
以」二説明したように本発明によれば、水素吸蔵合金粉
末表面に生成する水酸化物層の生成を抑制することがで
きるので、初期特性や急速充電特性を飛躍的に向上させ
せることかできるという効果を奏する。As explained above, according to the present invention, it is possible to suppress the formation of a hydroxide layer on the surface of the hydrogen-absorbing alloy powder, thereby dramatically improving the initial characteristics and rapid charging characteristics. It has the effect of being able to improve things.
第1図は本発明の電極を用いた円筒型ニッケル水素アル
カリ蓄電池の断面図、第2図はNi −1−1,0系(
25°C)におりるpHとE/Vとの関係を示すグラフ
、第3図はN ] 1−120系(25”c >とC
u−+−120系(25°C)とにおけるpHとE/V
との関係を示すグラフである。
1・・・正極、2・・・電極、3・・・セパレータ。
特許出願人:三洋電機 株式会社Figure 1 is a cross-sectional view of a cylindrical nickel-metal hydride alkaline storage battery using the electrode of the present invention, and Figure 2 is a sectional view of a Ni-1-1,0 series (
Figure 3 is a graph showing the relationship between pH and E/V at 25°C).
pH and E/V in u-+-120 system (25°C)
It is a graph showing the relationship between 1...Positive electrode, 2...Electrode, 3...Separator. Patent applicant: Sanyo Electric Co., Ltd.
Claims (4)
水中で粉砕、または粉砕、保存して水素吸蔵合金粉末を
作製するステップを有することを特徴とする水素吸蔵合
金電極の製造方法。(1) While maintaining the hydrogen storage alloy ingot at a hydrogen generation potential,
A method for producing a hydrogen storage alloy electrode, comprising the step of producing a hydrogen storage alloy powder by crushing or crushing and storing in water.
存するステップを有する水素吸蔵合金電極の製造方法に
おいて、 前記水には、予め、前記水素吸蔵合金を構成する金属、
又はこの金属の酸化物、水酸化物が添加されていること
を特徴とする水素吸蔵合金電極の製造方法。(2) A method for producing a hydrogen storage alloy electrode comprising the step of crushing or crushing and storing a hydrogen storage alloy ingot in water, wherein the water contains in advance a metal constituting the hydrogen storage alloy,
Or a method for producing a hydrogen storage alloy electrode, characterized in that an oxide or hydroxide of this metal is added.
存するステップを有する水素吸蔵合金電極の製造方法に
おいて、 前記水には、予め、前記水素吸蔵合金を構成する金属の
水酸化物の酸化還元電位より貴な電位で酸化、還元反応
を生じる金属、金属酸化物、或いは金属水酸化物が添加
されていることを特徴とする水素吸蔵合金電極の製造方
法。(3) A method for producing a hydrogen storage alloy electrode comprising the step of pulverizing or pulverizing and storing a hydrogen storage alloy ingot in water, in which the water is preliminarily treated with hydroxides of metals constituting the hydrogen storage alloy. A method for producing a hydrogen storage alloy electrode, characterized in that a metal, metal oxide, or metal hydroxide that causes an oxidation or reduction reaction at a potential higher than the redox potential is added.
中で粉砕、または粉砕、保存して水素吸蔵合金粉末を作
製するステップを有することを特徴とする水素吸蔵合金
電極の製造方法。(4) A method for producing a hydrogen storage alloy electrode, which comprises the step of producing a hydrogen storage alloy powder by pulverizing or pulverizing and storing a hydrogen storage alloy ingot in a buffer solution that maintains a constant pH.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2229060A JP2854109B2 (en) | 1990-08-29 | 1990-08-29 | Manufacturing method of hydrogen storage alloy electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2229060A JP2854109B2 (en) | 1990-08-29 | 1990-08-29 | Manufacturing method of hydrogen storage alloy electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04110403A true JPH04110403A (en) | 1992-04-10 |
| JP2854109B2 JP2854109B2 (en) | 1999-02-03 |
Family
ID=16886112
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2229060A Expired - Fee Related JP2854109B2 (en) | 1990-08-29 | 1990-08-29 | Manufacturing method of hydrogen storage alloy electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2854109B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0696823A4 (en) * | 1994-02-25 | 1996-04-24 | Yuasa Battery Co Ltd | Hydrogen absorbing electrode and production method thereof |
-
1990
- 1990-08-29 JP JP2229060A patent/JP2854109B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0696823A4 (en) * | 1994-02-25 | 1996-04-24 | Yuasa Battery Co Ltd | Hydrogen absorbing electrode and production method thereof |
| US5935732A (en) * | 1994-02-25 | 1999-08-10 | Yuasa Corporation | Hydrogen absorbing electrode and its manufacturing method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2854109B2 (en) | 1999-02-03 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |