JP3472489B2 - Hydrogen storage electrode and method for producing the same - Google Patents
Hydrogen storage electrode and method for producing the sameInfo
- Publication number
- JP3472489B2 JP3472489B2 JP25930198A JP25930198A JP3472489B2 JP 3472489 B2 JP3472489 B2 JP 3472489B2 JP 25930198 A JP25930198 A JP 25930198A JP 25930198 A JP25930198 A JP 25930198A JP 3472489 B2 JP3472489 B2 JP 3472489B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- resin
- metal
- plating film
- metal plating
- 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 - Lifetime
Links
- 239000001257 hydrogen Substances 0.000 title claims description 56
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 56
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 54
- 238000003860 storage Methods 0.000 title claims description 50
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 229910045601 alloy Inorganic materials 0.000 claims description 80
- 239000000956 alloy Substances 0.000 claims description 80
- 239000002245 particle Substances 0.000 claims description 61
- 238000007747 plating Methods 0.000 claims description 52
- 229910052751 metal Inorganic materials 0.000 claims description 47
- 239000002184 metal Substances 0.000 claims description 47
- 229920005989 resin Polymers 0.000 claims description 22
- 239000011347 resin Substances 0.000 claims description 22
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 17
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 17
- 229910052759 nickel Inorganic materials 0.000 claims description 14
- 229920005992 thermoplastic resin Polymers 0.000 claims description 14
- 239000011248 coating agent Substances 0.000 claims description 13
- 238000000576 coating method Methods 0.000 claims description 13
- 239000010419 fine particle Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- -1 polytetrafluoroethylene Polymers 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 7
- 229910018104 Ni-P Inorganic materials 0.000 claims description 5
- 229910018536 Ni—P Inorganic materials 0.000 claims description 5
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 claims description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 4
- 239000004952 Polyamide Substances 0.000 claims description 4
- 239000004698 Polyethylene Substances 0.000 claims description 4
- 239000004793 Polystyrene Substances 0.000 claims description 4
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 229920002492 poly(sulfone) Polymers 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- 229920001955 polyphenylene ether Polymers 0.000 claims description 4
- 229920002223 polystyrene Polymers 0.000 claims description 4
- 229910020674 Co—B Inorganic materials 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 2
- JMMZCWZIJXAGKW-UHFFFAOYSA-N 2-methylpent-2-ene Chemical compound CCC=C(C)C JMMZCWZIJXAGKW-UHFFFAOYSA-N 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims description 2
- 238000009792 diffusion process Methods 0.000 claims description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical group COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims 2
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 claims 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 25
- 239000000758 substrate Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- 239000000843 powder Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000011230 binding agent Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 230000003213 activating effect Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 238000009530 blood pressure measurement Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 238000005238 degreasing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 238000004080 punching Methods 0.000 description 3
- 239000005871 repellent Substances 0.000 description 3
- 239000002562 thickening agent Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000000635 electron micrograph Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910000652 nickel hydride Inorganic materials 0.000 description 2
- 239000000088 plastic resin Substances 0.000 description 2
- 239000007774 positive electrode material Substances 0.000 description 2
- 229910052761 rare earth metal Inorganic materials 0.000 description 2
- 230000002940 repellent Effects 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 229910000967 As alloy Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910001122 Mischmetal Inorganic materials 0.000 description 1
- 229910018007 MmNi Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000009689 gas atomisation Methods 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000007773 negative electrode material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 150000002910 rare earth metals Chemical group 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- IIACRCGMVDHOTQ-UHFFFAOYSA-M sulfamate Chemical compound NS([O-])(=O)=O IIACRCGMVDHOTQ-UHFFFAOYSA-M 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000005979 thermal decomposition 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
- Powder Metallurgy (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水素吸蔵合金を用
いた水素吸蔵電極及びその製造方法に関するものであ
る。TECHNICAL FIELD The present invention relates to a hydrogen storage electrode using a hydrogen storage alloy and a method for manufacturing the same.
【0002】[0002]
【従来の技術】近年、水素吸蔵合金を負極材料として用
いるニッケル−水素化物電池は、携帯電話やノートパソ
コンなど小型ポータブル機器用から電気自動車用まで多
機種の電源として使用されている。従来、ニッケル−水
素化物電池をはじめアルカリ蓄電池の寿命は、正極の電
極膨潤によるセパレータドライアウトが原因であった
が、正極活物質の改良により電極膨潤は抑制されてきて
いる。一方、負極では、水素吸蔵合金は希土類金属やA
l、Mnなどの溶出による腐食や正極から発生する酸素
による酸化を受け、劣化するという問題がある。その結
果、放電容量が減少して水素ガス発生しやすくなるとと
もに、正極から発生する酸素ガスを効率よく吸収できな
いので電池内圧が上昇し、安全弁作動によりセパレータ
ドライアウトが起こってサイクル寿命に至る。すなわ
ち、正極活物質の改良が進むにつれて寿命劣化の原因は
正極から負極に移ってきている。2. Description of the Related Art In recent years, nickel-hydride batteries using a hydrogen-absorbing alloy as a negative electrode material have been used as a power source for various models from small portable devices such as mobile phones and notebook computers to electric vehicles. Conventionally, the life of alkaline storage batteries including nickel-hydride batteries has been caused by separator dryout due to electrode swelling of the positive electrode, but electrode swelling has been suppressed by the improvement of the positive electrode active material. On the other hand, in the negative electrode, the hydrogen storage alloy is rare earth metal or A
There is a problem that it is deteriorated due to corrosion due to elution of l, Mn, etc. and oxidation due to oxygen generated from the positive electrode. As a result, the discharge capacity is reduced and hydrogen gas is easily generated, and the oxygen gas generated from the positive electrode cannot be efficiently absorbed, so that the internal pressure of the battery rises and the separator dryout occurs due to the operation of the safety valve to reach the cycle life. That is, as the improvement of the positive electrode active material progresses, the cause of the deterioration of life has shifted from the positive electrode to the negative electrode.
【0003】電池の寿命特性を改良するためには、電池
の内圧上昇を抑制することが必要であり、そのためには
ガス吸収性がよく、耐食性が優れる負極用水素吸蔵合金
が望まれている。内圧上昇を抑制するには、電極表面に
撥水剤を塗布し、三相界面を形成してガス吸収を促進す
る方法、耐食性向上には合金の組成や組織の制御などが
行われていた。一方、電極の製造方法は、合金と増粘
剤、結着剤などを混合してペーストを作製し、これをパ
ンチングメタル基盤に塗着後、乾燥、プレスして得る工
程であり、さらに撥水剤塗布工程も加えるとかなり複雑
な製造方法である。In order to improve the life characteristics of a battery, it is necessary to suppress an increase in the internal pressure of the battery, and for that purpose, a hydrogen storage alloy for a negative electrode having good gas absorption and excellent corrosion resistance is desired. In order to suppress the increase in internal pressure, a method of applying a water repellent agent to the surface of the electrode to form a three-phase interface to promote gas absorption, and to improve corrosion resistance, control of the alloy composition and structure has been performed. On the other hand, the electrode manufacturing method is a process in which an alloy, a thickener, a binder, etc. are mixed to prepare a paste, which is applied to a punching metal substrate, dried, and pressed to obtain a paste. This is a rather complicated manufacturing method when the agent coating step is also added.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記問題点
に鑑み、ガス吸収性能が優れ、内圧上昇の小さい水素吸
蔵電極を提供することを目的とする。本発明は、またそ
のような水素吸蔵電極の簡略化された製造方法を提供す
ることを目的とする。SUMMARY OF THE INVENTION In view of the above problems, it is an object of the present invention to provide a hydrogen storage electrode having excellent gas absorption performance and a small increase in internal pressure. The present invention also aims to provide a simplified method of manufacturing such a hydrogen storage electrode.
【0005】[0005]
【課題を解決するための手段】本発明の水素吸蔵電極
は、水素を可逆的に吸蔵放出しうる水素吸蔵合金を用い
る電極であって、主電極構成材が、水素吸蔵合金粒子
と、表面に熱可塑性樹脂の微粒子を包含した金属メッキ
被膜を有する平板状の金属集電体とからなり、前記水素
吸蔵合金粒子の少なくとも一部が、表面に熱可塑性樹脂
の微粒子を包含した金属メッキ被膜を有し、前記水素吸
蔵合金粒子が、乾式で、かつローラープレスによって、
前記金属集電体に圧着して加圧成形されていることを特
徴とする。また、前記水素吸蔵合金粒子のメッキ被膜
は、水素の拡散を許容する多孔質被膜であることが好ま
しい。The hydrogen storage electrode of the present invention is an electrode using a hydrogen storage alloy capable of reversibly storing and releasing hydrogen, wherein the main electrode constituent material is hydrogen storage alloy particles and a surface A flat metal collector having a metal plating coating containing fine particles of a thermoplastic resin, wherein at least a part of the hydrogen storage alloy particles has a metal plating coating containing fine particles of a thermoplastic resin on the surface. The hydrogen absorption
The alloy particles are dry, and by roller press,
Crimp the metal current collector, characterized that you have been pressure-formed. Further, the plating film of the hydrogen storage alloy particles is preferably a porous film which allows diffusion of hydrogen.
【0006】本発明は、表面に熱可塑性樹脂の微粒子を
包含した金属メッキ被膜を有する平板状の金属集電体上
に、少なくとも一部が表面に熱可塑性樹脂の微粒子を包
含した金属メッキ被膜を有する水素吸蔵合金粒子を、乾
式で、かつローラープレスによって、圧着することを特
徴とする水素吸蔵電極の製造方法を提供する。According to the present invention, a metal-plated film having at least a part thereof containing fine particles of a thermoplastic resin is provided on a flat metal current collector having a metal-plated film containing fine particles of a thermoplastic resin on its surface. Dry the hydrogen storage alloy particles
A method for manufacturing a hydrogen storage electrode, characterized in that pressure bonding is performed by a method and by a roller press .
【0007】[0007]
【発明の実施の形態】本発明の水素吸蔵電極は、表面に
熱可塑性樹脂の微粒子を包含した金属メッキ被膜を有す
る金属集電体の片面または両面に水素吸蔵合金粒子を加
圧成形することによって製造することができる。この加
圧成形を前記熱可塑性樹脂のガラス転移温度または融点
以上で、かつ熱分解温度未満の温度下で行うことが好ま
しい。この方法により製造される電極は、金属集電体表
面の金属メッキ被膜の凹凸あるいはさらに合金粒子表面
の金属メッキ被膜の凹凸のアンカー効果により集電体と
合金粒子との密着性あるいはさらに合金粒子同士の密着
性が向上する。また、前記のような特定の温度下で加圧
成形すると、金属メッキ被膜に包含されている樹脂粒子
が流動して広範囲でバインダーとして働くので、集電体
からの合金粒子の脱落をより低減することができる。本
発明によれば、乾式で、かつローラープレスにより連続
的に長尺帯状の金属集電体に水素吸蔵合金粒子を圧着す
ることができる。従って、品質の安定した電極を大量生
産することができる。BEST MODE FOR CARRYING OUT THE INVENTION The hydrogen storage electrode of the present invention is obtained by press-molding hydrogen storage alloy particles on one or both sides of a metal current collector having a metal plating coating containing fine particles of a thermoplastic resin on the surface. It can be manufactured. This pressure molding is preferably performed at a temperature not lower than the glass transition temperature or melting point of the thermoplastic resin and lower than the thermal decomposition temperature. The electrode produced by this method has an adhesion effect between the current collector and the alloy particles or further between the alloy particles due to the anchor effect of the unevenness of the metal plating film on the surface of the metal current collector or the unevenness of the metal plating film on the surface of the alloy particles. Improves the adhesion. Further, when pressure molding is performed under a specific temperature as described above, the resin particles contained in the metal plating film flow and act as a binder in a wide range, so that the drop of alloy particles from the current collector is further reduced. be able to. According to the present invention, the hydrogen-absorbing alloy particles can be pressure-bonded to a long strip-shaped metal current collector continuously by a dry method with a roller press. Therefore, electrodes with stable quality can be mass-produced.
【0008】本発明において、金属集電体は、少なくと
もFe、Ni、Cuのいずれか一つ以上を含み、その形
状が平板であることが好ましい。また、パンチングメタ
ルを使用することもできる。金属集電体の表面に形成す
るメッキ被膜の金属としては、Ni、Cu、Ni−P、
およびNi−Bからなる群より選ばれる素材が好まし
い。メッキ被膜の厚みは、1〜10μmが好ましい。一
方、水素吸蔵合金粒子の表面に形成するメッキ被膜の金
属としては、Ni、Cu、Co、Ni−P、Ni−B、
Co−PおよびCo−Bからなる群より選ばれる素材が
好ましい。合金粒子は、平均粒径10〜100μmであ
り、その表面にメッキされる被膜は、厚みが0.01〜
50μmで、合金の0.1〜4重量%相当が好ましい。
合金粒子にメッキされるニッケルなどの金属は水素の吸
蔵をほとんどしないため、多量の金属メッキをすると、
電極の単位重量当たりのエネルギー密度が低下する。従
って、できる限りメッキ量を低減することが望まれる。
しかしながら、4重量%を越えるメッキを施した水素吸
蔵合金粒子であっても、メッキを施していない水素吸蔵
合金粒子と混合することにより、見かけの単位重量当た
りのエネルギー密度を維持することが可能である。その
条件は、メッキを施していない水素吸蔵合金粒子を混合
しても導電性および結着性が低下しないことが挙げられ
る。導電性および結着性が低下しないメッキ量の上限
が、水素吸蔵合金粒子全体の20重量%相当である。金
属集電体および合金粒子の双方に金属メッキをする場合
は、金属集電体にメッキする同一の素材でメッキ被膜を
形成するのが好ましい。In the present invention, the metal current collector preferably contains at least one of Fe, Ni, and Cu and has a flat plate shape. It is also possible to use punching metal. As the metal of the plating film formed on the surface of the metal current collector, Ni, Cu, Ni-P,
And a material selected from the group consisting of Ni-B is preferable. The thickness of the plating film is preferably 1 to 10 μm. On the other hand, as the metal of the plating film formed on the surface of the hydrogen storage alloy particles, Ni, Cu, Co, Ni-P, Ni-B,
A material selected from the group consisting of Co-P and Co-B is preferable. The alloy particles have an average particle size of 10 to 100 μm, and the coating film plated on the surface has a thickness of 0.01 to 100 μm.
It is preferably 50 μm and corresponds to 0.1 to 4% by weight of the alloy.
Metals such as nickel plated on the alloy particles hardly absorb hydrogen, so if a large amount of metal is plated,
The energy density per unit weight of the electrode is reduced. Therefore, it is desired to reduce the plating amount as much as possible.
However, it is possible to maintain an apparent energy density per unit weight by mixing hydrogen storage alloy particles with plating of more than 4% by weight with hydrogen storage alloy particles without plating. is there. The condition is that the electroconductivity and the binding property are not deteriorated even when the hydrogen storage alloy particles which are not plated are mixed. The upper limit of the plating amount that does not reduce the conductivity and the binding property is equivalent to 20% by weight of the entire hydrogen storage alloy particles. When both the metal current collector and the alloy particles are metal-plated, it is preferable to form the plating film with the same material for plating the metal current collector.
【0009】前記金属集電体のメッキ被膜が包含する可
塑性樹脂としては、ポリテトラフルオロエチレン、ポリ
エチレン、ABS樹脂、ポリアミド、ポリスルフォン、
AS樹脂、ポリスチレン、塩化ビニリデン樹脂、ポリフ
ェニレンエーテル、メチルペンテン樹脂、およびメタク
リル酸樹脂からなる群より選ばれるものが好ましい。ま
た、前記水素吸蔵合金粒子のメッキ被膜が包含する可塑
性樹脂としては、前記と同様のものが用いられる。集電
体および合金粒子の双方にメッキ被膜を形成する場合
は、それらに包含される樹脂粒子は、同一の素材のもの
が好ましい。ここに用いる樹脂粒子の平均粒径は1〜5
μmが好ましい。そして、合金粒子のメッキ被膜に包含
される樹脂粒子の量は、合金の1〜10重量%相当、集
電体のメッキ被膜に包含される樹脂粒子の量は、単位面
積あたり0.1〜5.0g/m2が好ましい。The plastic resin contained in the plating film of the metal current collector is polytetrafluoroethylene, polyethylene, ABS resin, polyamide, polysulfone,
A resin selected from the group consisting of AS resin, polystyrene, vinylidene chloride resin, polyphenylene ether, methylpentene resin, and methacrylic acid resin is preferable. As the plastic resin included in the plating film of the hydrogen storage alloy particles, the same ones as described above are used. When a plating film is formed on both the current collector and the alloy particles, the resin particles contained therein are preferably made of the same material. The average particle size of the resin particles used here is 1 to 5
μm is preferred. The amount of the resin particles contained in the plated coating of the alloy particles corresponds to 1 to 10% by weight of the alloy, and the amount of the resin particles contained in the plated coating of the current collector is 0.1 to 5 per unit area. 0.0 g / m 2 is preferable.
【0010】[0010]
【実施例】以下、実施例により発明を説明する。
実施例1
まず、厚さ0.06mmの鉄板を脱脂、活性化、水洗な
どの前処理をした後、ポリテトラフルオロエチレン(以
下PTFEで表す)(分子量約7500〜10500)
の平均粒径5μmの粒子を含む以下のニッケルメッキ液
中でメッキ処理を行い、水洗乾燥して集電体基盤試料を
得た。これを基盤Aとする。EXAMPLES The present invention will be described below with reference to examples. Example 1 First, an iron plate having a thickness of 0.06 mm is pretreated by degreasing, activating, washing with water, etc., and then polytetrafluoroethylene (hereinafter referred to as PTFE) (molecular weight of about 7500 to 10500).
A plating treatment was performed in the following nickel plating solution containing particles having an average particle diameter of 5 μm, washed with water and dried to obtain a current collector base sample. This is the base A.
【0011】 電解ニッケルめっき(スルファミン酸浴) Ni(NH2SO3)2・4H2O 350(g/l) NiCl2・6H2O 45(g/l) H3BO3 40(g/l) 界面活性剤 1.0(g/l) PTFE粒子 100(g/l) pH 4.0 陰極電流密度 10A/dm2 温度 50℃ 陽極 Ni板 攪拌 循環 めっき時間 15分間 膜厚 5μm[0011] Electroless nickel plating (sulfamate bath) Ni (NH 2 SO 3) 2 · 4H 2 O 350 (g / l) NiCl 2 · 6H 2 O 45 (g / l) H 3 BO 3 40 (g / l ) Surfactant 1.0 (g / l) PTFE particles 100 (g / l) pH 4.0 Cathode current density 10 A / dm 2 Temperature 50 ° C. Anode Ni plate stirring Circulation plating time 15 minutes Film thickness 5 μm
【0012】次に、同じ鉄板材料を用いて、同様の前処
理を行い、PTFE粒子を含まないニッケルメッキ液中
で通常のニッケルメッキを行い水洗乾燥した。これを基
盤Bとする。また、厚さ0.06mmの鉄板に直径1.
5mm、ピッチ2.0mmの孔を規則正しくあけたパン
チングメタルに、基盤Bと同様の方法でメッキを行っ
た。これを基盤Cとする。Next, the same iron plate material was used to carry out the same pretreatment, followed by ordinary nickel plating in a nickel plating solution containing no PTFE particles, followed by washing with water and drying. This is the base B. In addition, a steel plate having a thickness of 0.06 mm has a diameter of 1.
A punching metal in which holes of 5 mm and a pitch of 2.0 mm were regularly formed was plated in the same manner as the substrate B. This is referred to as base C.
【0013】一方、MmNi3.6Co0.75Mn0.35Al
0.3(Mmは希土類元素の混合物であるミッシュメタル
を意味する)の組成になるように各金属を所定量秤量
し、不活性雰囲気下、高周波誘導溶解炉で合金インゴッ
トを作製し、1000℃で熱処理して合金試料を得た。
この合金インゴットを粒径75μm以下に機械的に粉砕
して水素吸蔵合金粉末試料とした。合金粉末試料は、こ
のほかに単ロール法やガスアトマイズ法など急冷法によ
り作製したものでもよい。On the other hand, MmNi 3.6 Co 0.75 Mn 0.35 Al
A predetermined amount of each metal is weighed so as to have a composition of 0.3 (Mm means Misch metal which is a mixture of rare earth elements), an alloy ingot is produced in a high frequency induction melting furnace in an inert atmosphere, and heat treated at 1000 ° C. Then, an alloy sample was obtained.
This alloy ingot was mechanically crushed to have a particle size of 75 μm or less to obtain a hydrogen storage alloy powder sample. Alternatively, the alloy powder sample may be prepared by a quenching method such as a single roll method or a gas atomizing method.
【0014】この合金粉末試料を脱脂、活性化、水洗な
どの前処理をした後、上記と同様のPTFE粒子を含む
ニッケルメッキ液を用いたバレルメッキ装置により、メ
ッキ量が合金の2重量%相当となるように電解メッキを
行い、水洗乾燥した。このバレルメッキ装置は、特開平
9−106817号公報に詳しく説明されている。こう
して得た複合メッキ被膜を有する合金試料を合金Aとす
る。図1に合金Aの粒子表面のSEM像を示す。図1よ
り、合金粒子表面には、メッキされた金属ニッケルの粒
子と、PTFE粒子が存在していたと思われる穴が観察
され、多くの凹凸が形成されていることがわかった。S
EM像を撮影するための試料の処理の際金属メッキ被膜
に包含されていたPTFE粒子の脱落が観察された。前
述の集電体基盤Aの表面についても多くの凹凸を含む同
様の状態が観察された。また、メッキ処理をしない合金
試料を比較合金Bとする。This alloy powder sample was pretreated by degreasing, activating, washing with water, etc., and then the amount of plating was equivalent to 2% by weight of the alloy by a barrel plating apparatus using a nickel plating solution containing PTFE particles similar to the above. Electroplating was performed so that This barrel plating device is described in detail in JP-A-9-106817. The alloy sample having the composite plating film thus obtained is called alloy A. FIG. 1 shows a SEM image of the particle surface of alloy A. From FIG. 1, it was found that on the surface of the alloy particles, plated metal nickel particles and holes in which the PTFE particles were supposed to exist were observed, and many irregularities were formed. S
During processing of the sample for taking an EM image, shedding of the PTFE particles contained in the metal plating coating was observed. A similar state including many irregularities was also observed on the surface of the current collector substrate A. Further, an alloy sample which is not plated is referred to as Comparative Alloy B.
【0015】上記基盤Aの片面上に、合金Aを均等にの
せ、ローラープレスで圧着させ、さらに反対側の面にも
同様の方法で同量の合金を圧着させて、厚さ約0.4m
mの水素吸蔵電極を作製した。このようにして得た電極
を電極Aとする。次に、基盤Bおよび基盤Cを用いて同
様の手法で電極を作製し、比較電極Bおよび比較電極C
とする。さらに、比較合金Bに増粘剤および結着剤を加
えてペースト状にし、基盤A、基盤Bおよび基盤Cにそ
れぞれ塗着し、乾燥後プレスして水素吸蔵電極を作製し
た。このようにして得た電極をそれぞれ比較電極D、比
較電極Eおよび比較電極Fとする。The alloy A is evenly placed on one surface of the base A and pressure-bonded by a roller press, and the same amount of the alloy is pressure-bonded on the other surface in the same manner to a thickness of about 0.4 m.
m hydrogen storage electrode was produced. The electrode thus obtained is called electrode A. Next, electrodes were prepared by the same method using the base B and the base C, and the reference electrode B and the reference electrode C were prepared.
And Further, a thickening agent and a binder were added to Comparative Alloy B to form a paste, which was coated on each of Substrate A, Substrate B and Substrate C, dried and pressed to produce a hydrogen storage electrode. The electrodes thus obtained are referred to as a comparison electrode D, a comparison electrode E, and a comparison electrode F, respectively.
【0016】以上のようにして作製した電極を相手極の
水酸化ニッケル電極とともに6モル/Lの水酸化カリウ
ム水溶液中に浸漬して開放型電池を作製した。そして、
周囲温度20℃において、0.1C(30mA/g)で
150%充電し、0.2C(60mA/g)で酸化水銀
電極基準で−0.6Vまで放電する充放電試験を行っ
た。その結果を図2に示す。図2から明らかなとおり、
本発明による電極Aと比較電極Fのみが安定した放電容
量を示した。これは合金と基盤との密着性に関係があ
る。電極Aは、合金と基盤の双方の表面に多くの凹凸を
持つため、図3の模式図に示すように、プレスするだけ
で両者のアンカー効果により、密着性が増してくる。図
3において、1は水素吸蔵合金粒子を表す。粒子1は、
PTFE粒子3を包含するニッケルメッキ被膜2を有す
る。一方、金属集電体4は、その表面に、PTFE粒子
6を包含するニッケルメッキ被膜5を有する。また、電
極Aにおいては、複合メッキされたPTFE粒子がプレ
ス熱で溶解してバインダーとして働く効果も作用してい
る。一方、比較電極Fは、基盤に穴があいているため、
基盤の表と裏の合金がバインダーを介して結着するので
密着性が高い。そのほかの電極は、合金と基盤の密着性
が不良であったため、基盤から合金が剥離または脱落
し、放電容量が減少した。The electrode prepared as described above was dipped in a 6 mol / L potassium hydroxide aqueous solution together with the nickel hydroxide electrode of the opposite electrode to prepare an open type battery. And
At an ambient temperature of 20 ° C., a charge / discharge test was performed in which the battery was charged at 0.1 C (30 mA / g) at 150% and discharged at 0.2 C (60 mA / g) to −0.6 V based on the mercury oxide electrode standard. The result is shown in FIG. As is clear from FIG.
Only the electrode A and the comparative electrode F according to the present invention showed stable discharge capacity. This is related to the adhesion between the alloy and the substrate. Since the electrode A has many irregularities on the surfaces of both the alloy and the substrate, as shown in the schematic view of FIG. 3, just by pressing, the adhesion effect increases due to the anchor effect of both. In FIG. 3, 1 represents a hydrogen storage alloy particle. Particle 1 is
It has a nickel plated coating 2 containing PTFE particles 3. On the other hand, the metal current collector 4 has a nickel-plated coating 5 containing PTFE particles 6 on its surface. In addition, in the electrode A, the composite-plated PTFE particles are melted by pressing heat and act as a binder. On the other hand, since the reference electrode F has a hole in the base,
Since the alloys on the front and back of the base are bound via a binder, the adhesion is high. The other electrodes had poor adhesion between the alloy and the substrate, so the alloy was peeled or dropped from the substrate, and the discharge capacity decreased.
【0017】次に、上記電極Aおよび比較電極B〜F
と、ペースト式水酸化ニッケル電極を用いて公称容量1
300mAhのAAサイズ密閉型電池を作製した。それ
ぞれ、本発明による電池A、比較電池B〜Fとする。こ
れらの電池を活性化させた後、周囲温度20℃におい
て、0.1C(130mA)で150%充電し、0.2
C(260mA)で端子電圧が1.0Vに低下するまで
放電する充放電を10サイクル繰り返した。その後、周
囲温度20℃において、電池に内圧センサーを取り付
け、1.0C(1300mA)で200%充電し、0.
2C(260mA)で端子電圧が1.0Vに低下するま
で放電する充放電を繰り返し、電池の内圧測定試験を行
った。図4に11サイクル目以降の充電末期における電
池内圧の測定結果を示す。図4から明らかなとおり、本
発明の電極Aのみが安定して低い内圧を示した。合金A
を用いた電極A、比較電極Bおよび比較電極Cは、いず
れも初期は低い内圧を示しているが、電極A以外は充放
電サイクルの経過とともに内圧が上昇した。基盤からの
合金の剥離により、局部的に電流密度が増大し、ガス発
生が顕著になったためである。また、PTFE粒子を含
まない比較電極D〜Fは、撥水効果が低いため、初期か
ら内圧が高い。Next, the electrode A and the reference electrodes B to F are used.
And a nominal capacity of 1 using a paste type nickel hydroxide electrode
An AA size sealed battery of 300 mAh was produced. These are referred to as Battery A and Comparative Batteries B to F according to the present invention, respectively. After activating these batteries, at ambient temperature of 20 ° C., charge them 150% at 0.1 C (130 mA), and
Charging / discharging in which the terminal voltage was lowered to 1.0 V at C (260 mA) was repeated 10 cycles. Then, at an ambient temperature of 20 ° C., an internal pressure sensor was attached to the battery and charged to 200% at 1.0 C (1300 mA),
Charging / discharging was repeated at 2 C (260 mA) until the terminal voltage dropped to 1.0 V, and a battery internal pressure measurement test was performed. FIG. 4 shows the measurement results of the battery internal pressure at the end of charging after the 11th cycle. As is clear from FIG. 4, only the electrode A of the present invention stably showed a low internal pressure. Alloy A
The electrode A, the comparative electrode B, and the comparative electrode C, each of which had a low internal pressure, initially showed low internal pressures, but the internal pressures of the electrodes other than the electrode A increased as the charge / discharge cycle progressed. This is because the peeling of the alloy from the substrate locally increased the current density and the gas generation became remarkable. Further, the comparative electrodes D to F containing no PTFE particles have a low water-repellent effect, and thus have a high internal pressure from the initial stage.
【0018】実施例2
上記比較合金Bと同様の方法で合金粉末試料を作製し、
38μm以上と38μm未満にふるい分けし、このうち
38μm以上の合金を用いて脱脂、活性化処理をした
後、PTFE粒子を含むニッケルメッキ液中でメッキ量
が合金の5重量%、10重量%、20重量%および30
重量%相当となるように電解メッキを行い、水洗乾燥し
た。これらの複合メッキ被膜を有する合金粉末試料を合
金G、合金H、合金Iおよび比較合金Jとする。これら
の合金を用いて電極Aと同様の方法で電極を作製し、電
極G、電極H、電極Iおよび比較電極Jとする。これら
の電極を用いて、実施例1と同様に水酸化ニッケル電極
を相手極として開放型電池を作製し、充放電試験を行っ
た。その結果を図5に示す。図5から明らかなとおり、
メッキ量が多い合金ほど重量あたりの放電容量は小さく
なる。Example 2 An alloy powder sample was prepared in the same manner as in Comparative Alloy B above,
After sieving into 38 μm or more and less than 38 μm, and degreasing and activating treatment using an alloy of 38 μm or more, the plating amount in the nickel plating solution containing PTFE particles is 5% by weight, 10% by weight of the alloy, and 20% by weight. Wt% and 30
Electroplating was performed so as to be equivalent to wt%, washed with water and dried. Alloy powder samples having these composite plating films are designated as alloy G, alloy H, alloy I and comparative alloy J. Electrodes are produced using these alloys in the same manner as the electrode A, and are used as the electrode G, the electrode H, the electrode I, and the reference electrode J. Using these electrodes, an open-type battery was prepared using the nickel hydroxide electrode as a counter electrode in the same manner as in Example 1, and a charge / discharge test was conducted. The result is shown in FIG. As is clear from FIG.
The larger the amount of plating, the smaller the discharge capacity per weight.
【0019】ここでメッキ量が10重量%、20重量%
および30重量%の合金に前述の38μm以下の合金粉
末試料を見かけメッキ量が5重量%となるように混合
し、電極Aと同様の方法で電極を作製し、電極K、電極
L、比較電極Mとする。これらの電極を用いて、実施例
1と同様に水酸化ニッケル電極を相手極として開放型電
池を作製し、充放電試験を行った。その結果を図6に示
す。図6から明らかなとおり、いずれも見かけメッキ量
を5重量%としたので放電容量は同等であった。しか
し、実質メッキ量が多いものほどメッキ無しの合金粉末
試料の混合量が多くなるため、粒子同士の密着性が低下
し、充放電サイクルの経過とともに放電容量が減少し
た。Here, the plating amount is 10% by weight, 20% by weight
And an alloy of 30% by weight were mixed so that the above alloy powder sample of 38 μm or less was apparently plated at an amount of 5% by weight, and an electrode was prepared in the same manner as the electrode A. Electrode K, electrode L, reference electrode Let M. Using these electrodes, an open-type battery was prepared using the nickel hydroxide electrode as a counter electrode in the same manner as in Example 1, and a charge / discharge test was conducted. The result is shown in FIG. As apparent from FIG. 6, the discharge capacity was the same because the apparent plating amount was set to 5% by weight in all cases. However, the larger the substantial amount of plating, the greater the amount of the alloy powder sample without plating mixed, resulting in a decrease in the adhesion between particles and a decrease in the discharge capacity with the progress of charge / discharge cycles.
【0020】次に、上記電極を用いて公称1300mA
hの密閉電池を作製し、電池K、電池Lおよび比較電池
Mとする。これらの電池を用いて、実施例1と同様の内
圧測定試験を行った結果を図7に示す。図7から明らか
なとおり、内圧測定試験においても内圧が低く安定して
いるのは本発明による電池Kおよび電極Lのみであっ
た。Next, using the above electrodes, a nominal 1300 mA
The sealed battery of h is manufactured and used as battery K, battery L and comparative battery M. FIG. 7 shows the results of an internal pressure measurement test similar to that of Example 1 using these batteries. As is clear from FIG. 7, it was only the battery K and the electrode L according to the present invention that the internal pressure was low and stable even in the internal pressure measurement test.
【0021】[0021]
【発明の効果】上記のように、本発明の水素吸蔵電極
は、密閉電池にしたときに内圧上昇を抑制することがで
きる。また、増粘剤、結着剤、乾燥工程、撥水剤塗布工
程が不要という簡便な方法で作製できる電極を提供する
とともに、穴不要の基盤を用いることができるため、低
コスト化が図れるというきわめて優れた効果が得られ
る。As described above, the hydrogen storage electrode of the present invention can suppress an increase in internal pressure when it is used as a sealed battery. In addition, it is possible to provide an electrode that can be manufactured by a simple method that does not require a thickening agent, a binder, a drying step, and a water repellent application step, and at the same time, it is possible to use a substrate that does not require holes, thereby reducing costs. An extremely excellent effect can be obtained.
【図1】本発明の実施例における合金粒子の構造を示す
電子顕微鏡写真である。FIG. 1 is an electron micrograph showing the structure of alloy particles in an example of the present invention.
【図2】本発明の実施例における各種電極の放電容量と
サイクル数との関係を示す図である。FIG. 2 is a diagram showing the relationship between the discharge capacity of various electrodes and the number of cycles in the example of the present invention.
【図3】本発明の実施例における電極細部の模式図であ
る。FIG. 3 is a schematic view of details of electrodes in an example of the present invention.
【図4】本発明の実施例における各種電極を用いた電池
の内圧とサイクル数の関係を示す図である。FIG. 4 is a diagram showing the relationship between the internal pressure and the cycle number of a battery using various electrodes in an example of the present invention.
【図5】本発明の実施例における各種電極を用いた電池
の放電容量とサイクル数との関係を示す図である。FIG. 5 is a diagram showing a relationship between a discharge capacity and a cycle number of a battery using various electrodes according to an example of the present invention.
【図6】本発明の実施例における各種電極を用いた電池
の放電容量とサイクル数との関係を示す図である。FIG. 6 is a diagram showing a relationship between a discharge capacity and a cycle number of a battery using various electrodes according to an example of the present invention.
【図7】本発明の実施例における各種電極を用いた電池
の充電量と電池内圧との関係を示す図である。FIG. 7 is a diagram showing a relationship between a charge amount and a battery internal pressure of a battery using various electrodes in an example of the present invention.
1 水素吸蔵合金粒子 2、5 メッキ被膜 3、6 PTFE粒子 4 集電体 1 Hydrogen storage alloy particles 2, 5 plating film 3,6 PTFE particles 4 Current collector
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI H01M 4/66 H01M 4/66 A 4/70 4/70 A (58)調査した分野(Int.Cl.7,DB名) H01M 4/14 - 4/84 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 identification code FI H01M 4/66 H01M 4/66 A 4/70 4/70 A (58) Fields investigated (Int.Cl. 7 , DB name) H01M 4/14-4/84
Claims (11)
合金を用いる電極であって、 主電極構成材が、水素吸蔵合金粒子と、表面に熱可塑性
樹脂の微粒子を包含した金属メッキ被膜を有する平板状
の金属集電体とからなり、 前記水素吸蔵合金粒子の少なくとも一部が、表面に熱可
塑性樹脂の微粒子を包含した金属メッキ被膜を有し、 前記水素吸蔵合金粒子が、乾式で、かつローラープレス
によって、前記金属集電体に圧着して加圧成形されてい
る水素吸蔵電極。1. An electrode using a hydrogen storage alloy capable of reversibly storing and releasing hydrogen, wherein the main electrode constituent material is a hydrogen storage alloy particle, and a metal plating film containing fine particles of a thermoplastic resin on the surface. It consists of a plate-like metal current collector having, at least a portion of the hydrogen-absorbing alloy particles have a metal plating film that includes fine particles of a thermoplastic resin on the surface, said hydrogen storage alloy particles, a dry, And roller press
A hydrogen storage electrode, which is pressure-molded by pressure bonding to the metal current collector .
が水素の拡散を許容する多孔質被膜である請求項1記載
の水素吸蔵電極。2. The hydrogen storage electrode according to claim 1, wherein the metal plating film of the hydrogen storage alloy particles is a porous film which allows diffusion of hydrogen.
が水素吸蔵合金重量あたり20重量%以下である請求項
1記載の水素吸蔵電極。3. The hydrogen storage electrode according to claim 1, wherein the metal plating film of the hydrogen storage alloy particles is 20% by weight or less based on the weight of the hydrogen storage alloy.
がNi、Cu、Co、Ni−P、Ni−B、Co−P、
およびCo−Bからなる群より選ばれる請求項1記載の
水素吸蔵電極。4. The metal plating film of the hydrogen storage alloy particles is Ni, Cu, Co, Ni-P, Ni-B, Co-P,
The hydrogen storage electrode according to claim 1, which is selected from the group consisting of Co-B and Co-B.
i、Cu、Ni−P、およびNi−Bからなる群より選
ばれる請求項1記載の水素吸蔵電極。5. The metal plating film of the metal current collector is N
The hydrogen storage electrode according to claim 1, which is selected from the group consisting of i, Cu, Ni-P, and Ni-B.
および前記金属集電体の金属メッキ被膜がNi、Cu、
Ni−P、およびNi−Bからなる群より選ばれる同一
素材である請求項1記載の水素吸蔵電極。6. The metal plating film of the hydrogen storage alloy particles and the metal plating film of the metal current collector are Ni, Cu,
The hydrogen storage electrode according to claim 1, which is the same material selected from the group consisting of Ni-P and Ni-B.
が包含する熱可塑性樹脂が、ポリテトラフルオロエチレ
ン、ポリエチレン、ABS樹脂、ポリアミド、ポリスル
フォン、AS樹脂、ポリスチレン、塩化ビニリデン樹
脂、ポリフェニレンエーテル、メチルペンテン樹脂、お
よびメタクリル酸樹脂からなる群より選ばれる一つ以上
である請求項1記載の水素吸蔵電極。7. The thermoplastic resin contained in the metal plating film of the hydrogen storage alloy particles is polytetrafluoroethylene, polyethylene, ABS resin, polyamide, polysulfone, AS resin, polystyrene, vinylidene chloride resin, polyphenylene ether, methyl. The hydrogen storage electrode according to claim 1, which is one or more selected from the group consisting of a pentene resin and a methacrylic acid resin.
する熱可塑性樹脂が、ポリテトラフルオロエチレン、ポ
リエチレン、ABS樹脂、ポリアミド、ポリスルフォ
ン、AS樹脂、ポリスチレン、塩化ビニリデン樹脂、ポ
リフェニレンエーテル、メチルペンテン樹脂、およびメ
タクリル酸樹脂からなる群より選ばれる一つ以上である
請求項1記載の水素吸蔵電極。8. The thermoplastic resin contained in the metal plating film of the metal current collector is polytetrafluoroethylene, polyethylene, ABS resin, polyamide, polysulfone, AS resin, polystyrene, vinylidene chloride resin, polyphenylene ether, methyl. The hydrogen storage electrode according to claim 1, which is one or more selected from the group consisting of a pentene resin and a methacrylic acid resin.
が包含する熱可塑性樹脂および前記金属集電体の金属メ
ッキ被膜が包含する熱可塑性樹脂が、ポリテトラフルオ
ロエチレン、ポリエチレン、ABS樹脂、ポリアミド、
ポリスルフォン、AS樹脂、ポリスチレン、塩化ビニリ
デン樹脂、ポリフェニレンエーテル、メチルペンテン樹
脂、およびメタクリル酸樹脂からなる群より選ばれる一
つ以上の同一素材である請求項1記載の水素吸蔵電極。9. The thermoplastic resin included in the metal plating film of the hydrogen storage alloy particles and the thermoplastic resin included in the metal plating film of the metal current collector are polytetrafluoroethylene, polyethylene, ABS resin, polyamide,
The hydrogen storage electrode according to claim 1, which is one or more same materials selected from the group consisting of polysulfone, AS resin, polystyrene, vinylidene chloride resin, polyphenylene ether, methylpentene resin, and methacrylic acid resin.
i、およびCuからなる群より選ばれる一つ以上を含む
請求項1記載の水素吸蔵電極。10. The metal current collector is at least Fe, N
The hydrogen storage electrode according to claim 1, comprising at least one selected from the group consisting of i and Cu.
た金属メッキ被膜を有する平板状の金属集電体上に、少
なくとも一部が表面に熱可塑性樹脂の微粒子を包含した
金属メッキ被膜を有する水素吸蔵合金粒子を、乾式で、
かつローラープレスによって、圧着することを特徴とす
る水素吸蔵電極の製造方法。11. A hydrogen plate having a metal-plated coating, the surface of which has a metal-plated coating containing fine particles of a thermoplastic resin, at least a portion of which has a metal-plated coating containing fine particles of a thermoplastic resin. The occlusion alloy particles are dry type,
A method for producing a hydrogen storage electrode , which comprises pressing with a roller press .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25930198A JP3472489B2 (en) | 1998-08-27 | 1998-08-27 | Hydrogen storage electrode and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25930198A JP3472489B2 (en) | 1998-08-27 | 1998-08-27 | Hydrogen storage electrode and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000077064A JP2000077064A (en) | 2000-03-14 |
| JP3472489B2 true JP3472489B2 (en) | 2003-12-02 |
Family
ID=17332186
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25930198A Expired - Lifetime JP3472489B2 (en) | 1998-08-27 | 1998-08-27 | Hydrogen storage electrode and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3472489B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4644801B2 (en) * | 2005-01-13 | 2011-03-09 | 国立大学法人福井大学 | Composite sheet body and method for producing the same |
| JP5186909B2 (en) * | 2007-12-14 | 2013-04-24 | 日産自動車株式会社 | Current collector for lithium ion secondary battery |
| JP7309376B2 (en) * | 2017-11-06 | 2023-07-18 | キヤノンアネルバ株式会社 | Heat generating method and apparatus |
| WO2019087390A1 (en) | 2017-11-06 | 2019-05-09 | キヤノンアネルバ株式会社 | Structure and production method therefor |
-
1998
- 1998-08-27 JP JP25930198A patent/JP3472489B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JP2000077064A (en) | 2000-03-14 |
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