JPS5840828B2 - Manufacturing method of hydrogen storage electrode - Google Patents
Manufacturing method of hydrogen storage electrodeInfo
- Publication number
- JPS5840828B2 JPS5840828B2 JP52081837A JP8183777A JPS5840828B2 JP S5840828 B2 JPS5840828 B2 JP S5840828B2 JP 52081837 A JP52081837 A JP 52081837A JP 8183777 A JP8183777 A JP 8183777A JP S5840828 B2 JPS5840828 B2 JP S5840828B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- net
- metal
- hydrogen storage
- nickel
- 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
Links
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
-
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Battery Electrode And Active Subsutance (AREA)
- Inert Electrodes (AREA)
Description
【発明の詳細な説明】
本発明は、例えばアルカリ蓄電池の陰極に用いられる水
素吸蔵電極の改良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in hydrogen storage electrodes used, for example, as cathodes of alkaline storage batteries.
水素吸蔵電極は、水素吸蔵材を活物質とし、これを集電
体あるいは電極支持体のニッケルネット、ニッケルメッ
キした鉄のネット、あるいは三次元の網目状構造を有す
るニッケルなどの金属多孔体、いわゆる発泡金属に保持
させる構造がとられる。A hydrogen storage electrode uses a hydrogen storage material as an active material, and uses it as a current collector or electrode support, such as a nickel net, a nickel-plated iron net, or a metal porous material such as nickel that has a three-dimensional network structure, so-called A structure is used in which the metal foam is used to hold it.
モして集電体に金属ネットを用いる電極は、一般にネッ
トを中央にしてその両面に水素吸蔵材粉末を焼結により
結合する方法により製造される。Electrodes using a metal net as a current collector are generally manufactured by a method in which hydrogen storage material powder is bonded to both sides of the net by sintering, with the net in the center.
しかし、その結合力は、単体金属の焼結体のように強く
ない。However, the bonding force is not as strong as that of a sintered body of a single metal.
特に充放電に伴う水素の吸蔵、放出により水素吸蔵材の
体積変化が起こり、これを繰り返すと電極構成材料相互
の結合カニま弱まり、活物質の剥離、脱落が生じ、電極
容量が低下する欠点がある。In particular, the volume of the hydrogen storage material changes due to the storage and release of hydrogen during charging and discharging, and if this happens repeatedly, the bond between the electrode constituent materials weakens, the active material peels off or falls off, and the electrode capacity decreases. be.
一方、発泡金属を用いる電極は、三次元の網目の中に活
物質が存在する構造で、発泡金属に水素吸蔵材粉末、あ
るいは水素吸蔵合金を形成する単体金属の混合粉末を充
填して加圧成形し、焼結温度あるいは合金化する温度で
熱処理を行って製造される。On the other hand, electrodes using foamed metal have a structure in which the active material exists in a three-dimensional network, and the foamed metal is filled with hydrogen-absorbing material powder or a mixed powder of single metals that form a hydrogen-absorbing alloy and then pressurized. It is manufactured by molding and heat treatment at sintering or alloying temperatures.
この場合に支持体に活物質を内蔵させているので、電極
の特性と寿命は前者に比べて一段と向上する。In this case, since the active material is incorporated into the support, the characteristics and life of the electrode are further improved compared to the former.
しかし、ここに用いられる高多孔度の発泡金属は、その
骨格の線径が約40〜60μと細く、熱処理によって水
素吸蔵合金あるいは単体金属の一部と反応し、発泡金属
が合金化する場合がある。However, the highly porous metal foam used here has a thin wire diameter of about 40 to 60 μm, and when heat treated, it may react with the hydrogen storage alloy or a part of the single metal, causing the foam metal to become alloyed. be.
その結果、発泡金属本来の強度を消失してもろくなり、
電極に亀裂を生じたりし、電極自体の強度も低下する。As a result, the foam metal loses its original strength and becomes brittle.
This can cause cracks in the electrode and reduce the strength of the electrode itself.
また、発泡金属が形成する合金の一部には金属水素化物
を形成するものもある。Furthermore, some of the alloys formed by foamed metals form metal hydrides.
この様な場合、電極強度は更に低下する。In such a case, the electrode strength is further reduced.
従って、低電流密度での完全放電のような苛酷な条件で
の充放電を繰り返すと活物質の体積変化による応力に耐
え切れなくなり、電極の一部分が脱落してしまうことが
ある。Therefore, if charging and discharging are repeated under severe conditions such as complete discharge at a low current density, the active material may not be able to withstand the stress caused by the change in volume, and a portion of the electrode may fall off.
たとえば、活物質としてチタン−ニッケル系合金わ用い
た場合、発泡金属の材質がニッケルであれば、Ti2N
i、T1Ni等の金属水素化物を形成する合金を生成す
る。For example, when using a titanium-nickel alloy as the active material, if the material of the foam metal is nickel, Ti2N
i, T1Ni, etc. to form metal hydride-forming alloys.
電極を切断して、その断面を観察すると、発泡金属の原
形が一部消失していることが良くわかる。If you cut the electrode and observe its cross section, you can clearly see that the original shape of the foamed metal has partially disappeared.
本発明は活物質の脱落がなく、長期間、苛酷な条件にお
ける充放電の可能な水素吸蔵電極を提供することを目的
とする。An object of the present invention is to provide a hydrogen storage electrode that can be charged and discharged under severe conditions for a long period of time without causing any active material to fall off.
本発明は、水素吸蔵材の粉末を内蔵する発泡金属の表面
、特に板状体の両面に耐電解性の金属ネットを加圧して
一体化し、電極構成材料の融点以下の温度で熱処理をし
て金属ネットを一体に結合するものである。In the present invention, an electrolytic resistant metal net is pressurized and integrated on the surface of a foamed metal containing powder of a hydrogen absorbing material, particularly on both sides of a plate-like body, and heat treated at a temperature below the melting point of the electrode constituent material. It connects metal nets together.
ここに、金属ネットにはニッケル、ステンレス鋼などが
用いられ、それらの線径は少なくとも発泡金属の骨格の
線径よりも大きく、かつあまり太くなく、網目間隔が適
度のものを用いる。Here, nickel, stainless steel, or the like is used for the metal net, and the wire diameter thereof is at least larger than the wire diameter of the foam metal skeleton, and is not very thick, and the mesh spacing is appropriate.
ネットの線径か細いと熱処理によって発泡金属と同様に
合金化してネ、ットによる補強効果が得られない。If the wire diameter of the net is small, it will become alloyed like foamed metal during heat treatment, and the reinforcing effect of the net will not be obtained.
また逆に太いと電極の重量および体積にネットの占める
割合が多くなり、電極の単位重量、単位体積当たりの出
力容量を低下させる。On the other hand, if the electrode is thick, the ratio of the net to the weight and volume of the electrode increases, reducing the output capacity per unit weight and unit volume of the electrode.
また、網目間隔が小さいと発泡金属へのネットの食いこ
みが十分でなく、ネットの剥離を生ずる。Furthermore, if the mesh spacing is small, the net will not penetrate into the foamed metal sufficiently, resulting in peeling of the net.
網目間隔が大きいと、電極表面から活物質の剥離、脱落
が起こり易く、ネットによる補強効果を得られない。If the mesh spacing is large, the active material is likely to peel off or fall off from the electrode surface, making it impossible to obtain the reinforcing effect of the net.
以下本発明をその実施例により説明する。The present invention will be explained below with reference to Examples.
実施例 1
市販の純度99.5%以上のチタンとニッケルとを原子
比で2:1になるように混合する。Example 1 Commercially available titanium with a purity of 99.5% or more and nickel are mixed at an atomic ratio of 2:1.
この試料をアルゴン雰囲気中のアーク溶解炉で合金に合
成した後、粉砕して46μ以下の合金粉末を得た。This sample was synthesized into an alloy in an arc melting furnace in an argon atmosphere, and then pulverized to obtain an alloy powder of 46 μm or less.
得られた合金粉末は主としてT I 2 N i相から
なり、その他にはT1Ni相、TtNt3相、およびT
i相、Ni相の単体金属から成る。The obtained alloy powder mainly consists of T I 2 N i phase, and also T1Ni phase, TtNt3 phase, and T
Consists of an i-phase and a Ni-phase single metal.
次にこの合金粉末10gを材質がニッケルである大きさ
50X50mmの発泡金属に充填し、両面に線径0.1
5mm、網目間隔1間で、発泡金属と同じ大きさのニッ
ケルネットをおき、1トン/dの圧力で成形して両者を
一体化させた後、真空中(10= 〜10−”Torr
、)で950℃の温度で30分間熱処理を行って厚さ1
.4mmの電極を得た。Next, 10 g of this alloy powder was filled into a foamed metal made of nickel with a size of 50 x 50 mm, and both sides were filled with a wire diameter of 0.1.
A nickel net of the same size as the foamed metal was placed with a mesh spacing of 5 mm and a mesh spacing of 1, and after molding at a pressure of 1 ton/d to integrate the two, it was heated in a vacuum (10 = ~10-”Torr).
, ) at a temperature of 950℃ for 30 minutes to obtain a thickness of 1.
.. A 4 mm electrode was obtained.
この電極をAとし、比較のためにニッケルネットを結合
せず上記と同様の条件で成形、熱処理をして得た電極を
B1またニッケルネットを電極支持体としてその両面に
合金粉末を1トン、′−の圧力で成形し、上記と同様の
条件で熱処理して得た電極をCとする。This electrode is referred to as A, and for comparison, an electrode obtained by molding and heat-treating under the same conditions as above without bonding the nickel net is B1.Also, nickel net is used as an electrode support, and 1 ton of alloy powder is applied to both sides of the electrode. C is an electrode obtained by molding at a pressure of - and heat-treating under the same conditions as above.
これらの電極を陰極とし、公知のニッケル電極を陽極と
してアルカリ蓄電池を構成し、陰極の活物質1g当たり
100mAの電流で充放電を繰り返したときの放電容量
の変化を図面に示す。An alkaline storage battery was constructed using these electrodes as a cathode and a known nickel electrode as an anode, and the drawing shows the change in discharge capacity when charging and discharging were repeated at a current of 100 mA per gram of active material of the cathode.
なお放電は標準酸化水銀電極に対する陰極電位で750
mVまでとし、寿命は初期1〜5サイクルの容量の1乃
以下に低下した時点とした。The discharge is at a cathode potential of 750 with respect to a standard mercury oxide electrode.
mV, and the lifetime was defined as the time when the capacity decreased to 1 or less of the initial 1 to 5 cycle capacity.
放電容量は陰極活物質の単位重量当たりの値で示した。The discharge capacity was expressed as a value per unit weight of the cathode active material.
図からも明らかな如く、本発明の電極は初期容量は比較
例に比べて多くないが、寿命特性がすぐれており、Cの
4倍以上、Bの1.5倍以上向上している。As is clear from the figure, although the initial capacity of the electrode of the present invention is not as large as that of the comparative example, it has excellent life characteristics, which is more than 4 times better than C and 1.5 times better than B.
すなわち、Cは活物質の電極支持体への保持が合金粒子
の焼結による結合のみであり、充放電の繰り返しで、そ
の結合力が次第に弱まり、充放電サイクルを重ねると支
持体のニッケルネットから、活物質の剥離、脱落が多く
なって、容量低下を起こし電極寿命が短い。In other words, in C, the active material is held on the electrode support only by bonding through sintering of the alloy particles, and with repeated charging and discharging, the bonding force gradually weakens, and as the charge and discharge cycles are repeated, the nickel net of the support is removed. , the active material often peels off and falls off, causing a decrease in capacity and shortening the life of the electrode.
また、Bは支持体の発泡金属が活物質の合金と合金をつ
くり、強度が低下して一部亀裂を生じたものがあり、充
放電の繰り返しでその部分からの脱落が認められた。In addition, in B, the foamed metal of the support formed an alloy with the alloy of the active material, resulting in a decrease in strength and cracking in some parts, and falling off from those parts was observed after repeated charging and discharging.
これに対し、本発明の電極Aは、発泡金属の両面をニッ
ケルネットで補強しているので、電極板の亀裂および補
強ネットの合金化による原形消失もない。In contrast, in the electrode A of the present invention, both sides of the foamed metal are reinforced with nickel nets, so there is no loss of original shape due to cracks in the electrode plates or alloying of the reinforcing nets.
従って、300サイクル以上充放電を繰り返しても活物
質の脱落はほとんど認められず、容量低下もほとんどな
く良好な特性を示している。Therefore, even after repeated charging and discharging cycles of 300 cycles or more, there is hardly any dropout of the active material, and there is almost no decrease in capacity, showing good characteristics.
実施例 2
市販の純度9965%以上のチタンとニッケルの粉末と
を原子比で2:1になるように混合し、この混合粉末1
0gを材質がニッケルである大きさ50X50mmの発
泡金属に充填し、両面にニッケルネットをおき、1トン
/dの圧力で加圧成形して一体化させた後、真空中(1
0−4〜1.0−5Torr、)で850℃の温度で5
時間熱処理して焼結電極を得た。Example 2 Commercially available titanium and nickel powders with a purity of 9965% or higher were mixed at an atomic ratio of 2:1, and this mixed powder 1
0 g was filled into a foamed metal made of nickel with a size of 50 x 50 mm, nickel net was placed on both sides, and the mixture was press-formed at a pressure of 1 ton/d to integrate it.
5 at a temperature of 850℃ at 0-4~1.0-5Torr,)
A sintered electrode was obtained by heat treatment for a period of time.
この場合ニッケルネットは線径を0、05 mm〜0.
6 mw、網目間隔を0.1〜8mmのものを用いた。In this case, the nickel net has a wire diameter of 0.05 mm to 0.05 mm.
6 mw and mesh spacing of 0.1 to 8 mm were used.
このようにして製作した電極を陰極とし、実施例1と同
じ方法で充放電試験をした。The electrode thus produced was used as a cathode, and a charge/discharge test was conducted in the same manner as in Example 1.
この結果を次表に示す。The results are shown in the table below.
表において放電容量(Ah/g)は電極1g当たりの容
量で、1〜10サイクルの平均値を示す。In the table, the discharge capacity (Ah/g) is the capacity per 1 g of electrode, and shows the average value for 1 to 10 cycles.
表に示した8種類の電極において、イはネットの線径か
細いために活物質と合金化し、大半のニッケル線が原形
を消失しており、口は充放電80サイクルでネットの一
部が剥離し、充放電サイクルを重ねると剥離部分が次第
に広がり、活物質の脱落も多くなった。In the eight types of electrodes shown in the table, the net wire diameter is small and alloys with the active material, most of the nickel wires have lost their original shape, and part of the net has peeled off after 80 charging and discharging cycles. However, as charge and discharge cycles were repeated, the peeled area gradually expanded and more active material fell off.
トおよびチはネットの網目の間からの活物質の脱落があ
り、充放電サイクルを重ねることによってトの増加量は
少なか°つたが、チは多かった。In cases 1 and 2, the active material fell out from between the meshes of the net, and as the charge/discharge cycles were repeated, the amount of increase in case 3 decreased, but the amount of increase in case 1 increased.
これらの結果からイ22ロ、チネットは電極板補強の効
果をほとんど得られないことがわかる。From these results, it can be seen that (1) and (2), Chinette hardly achieves the effect of reinforcing the electrode plate.
一方、ハ、二、ホ、への電極は300サイクルでほとん
ど変化もなく、これらに用いたネットは効果があること
がわかる。On the other hand, the electrodes C, 2, and E showed almost no change after 300 cycles, indicating that the net used for these electrodes was effective.
以上の結果より、発泡金属の両面に取り付ける金属ネッ
トの線径は発泡金属の骨格の線径の約40〜60μより
大きく、かつ0.5 mm以下で、ネットの網目間隔は
0.2〜5朋の範囲が補強効果および出力容量密度の両
者から適切であることがわかる。From the above results, the wire diameter of the metal net attached to both sides of the foamed metal is larger than the wire diameter of the foamed metal skeleton by about 40 to 60μ, and is 0.5 mm or less, and the mesh spacing of the net is 0.2 to 5. It can be seen that the above range is appropriate from both the reinforcement effect and output capacity density.
なお実施例では水素吸蔵合金としてチタン−ニッケル系
合金を用いたが、発泡金属と合金を生成する、他の水素
吸蔵合金、例えば、La Ni5 。In the examples, a titanium-nickel alloy was used as the hydrogen storage alloy, but other hydrogen storage alloys that form an alloy with the foam metal, such as La Ni5, may be used.
Mm Ni、 、 TiFe、Mg2Niも適用するこ
とができる。MmNi, TiFe, Mg2Ni can also be applied.
また、金属ネットの材質も、導電性、アルカリ電解液を
有するニッケルメッキした鉄、ニッケルメッキした銅、
あるいは銀、ステンレス鋼などに適用できる。In addition, the material of the metal net is conductive, nickel-plated iron with alkaline electrolyte, nickel-plated copper,
Alternatively, it can be applied to silver, stainless steel, etc.
以上のように、本発明によれば長期にわたって良好な特
性を有する水素吸蔵電極が得られる。As described above, according to the present invention, a hydrogen storage electrode having good characteristics over a long period of time can be obtained.
図面は各種水素吸蔵電極を用いたアルカリ蓄電池の充放
電に伴う放電容量の変化を示す。The drawings show changes in discharge capacity during charging and discharging of alkaline storage batteries using various hydrogen storage electrodes.
Claims (1)
有する金属多孔体の表面に、加圧により金属ネットを一
体にするとともに前記粉末の焼結す温度で加熱処理して
前記金属ネットを一体に結合することを特徴とする水素
吸蔵電極の製造法。1. A metal net is integrated with the surface of a metal porous body having a three-dimensional network structure containing powder of a hydrogen storage material by applying pressure, and is heated at a temperature at which the powder is sintered to form the metal net. A method for manufacturing a hydrogen storage electrode characterized by being integrally bonded.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52081837A JPS5840828B2 (en) | 1977-07-07 | 1977-07-07 | Manufacturing method of hydrogen storage electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52081837A JPS5840828B2 (en) | 1977-07-07 | 1977-07-07 | Manufacturing method of hydrogen storage electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5416632A JPS5416632A (en) | 1979-02-07 |
| JPS5840828B2 true JPS5840828B2 (en) | 1983-09-08 |
Family
ID=13757572
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52081837A Expired JPS5840828B2 (en) | 1977-07-07 | 1977-07-07 | Manufacturing method of hydrogen storage electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5840828B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59181459A (en) * | 1983-03-31 | 1984-10-15 | Toshiba Corp | Metal oxide hydrogen battery |
| JP2733231B2 (en) * | 1987-11-17 | 1998-03-30 | 松下電器産業株式会社 | Manufacturing method of hydrogen storage alloy electrode |
-
1977
- 1977-07-07 JP JP52081837A patent/JPS5840828B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5416632A (en) | 1979-02-07 |
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