JPH05275108A - Battery - Google Patents
BatteryInfo
- Publication number
- JPH05275108A JPH05275108A JP4054782A JP5478292A JPH05275108A JP H05275108 A JPH05275108 A JP H05275108A JP 4054782 A JP4054782 A JP 4054782A JP 5478292 A JP5478292 A JP 5478292A JP H05275108 A JPH05275108 A JP H05275108A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- battery
- hydrogen storage
- negative electrode
- ion exchange
- 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.)
- Pending
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
- Hybrid Cells (AREA)
- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は電池に係り、特に、水素
吸蔵合金中に含まれる水素と空気中の酸素の反応により
構成される一次または二次電池に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a battery, and more particularly to a primary or secondary battery formed by a reaction between hydrogen contained in a hydrogen storage alloy and oxygen in the air.
【0002】[0002]
【従来の技術】高エネルギ密度、長寿命の高性能電池
は、コードレス機器用の小型電池,電気自動車用電池、
さらには電力貯蔵用の大型電池に至るまで、近年その必
要性が益々高くなっている。水素吸蔵合金は、理論エネ
ルギ密度が最も大きな元素である水素を利用するための
担体として有効な材料であり、ニッケル−金属水素化物
電池に利用されている(特開昭63−6746号公報)。2. Description of the Related Art High-performance batteries with high energy density and long life are used in small batteries for cordless equipment, batteries for electric vehicles,
In addition, even in the case of large-sized batteries for storing electric power, the need for them is increasing more and more in recent years. The hydrogen storage alloy is a material effective as a carrier for utilizing hydrogen, which is the element having the highest theoretical energy density, and is used for nickel-metal hydride batteries (Japanese Patent Laid-Open No. 63-6746).
【0003】また、空気中の酸素を活物質として利用す
る空気電池は、少ない電池内蔵活物質量でエネルギ密度
を増加させるには、有効な方法である。すでに空気−亜
鉛一次電池は実用化されており、空気−亜鉛二次電池は
電気自動車用に研究された(特開昭60−172173号公
報)。An air battery that uses oxygen in the air as an active material is an effective method for increasing the energy density with a small amount of active material with a built-in battery. Air-zinc primary batteries have already been put to practical use, and air-zinc secondary batteries have been studied for electric vehicles (Japanese Patent Laid-Open No. 60-172173).
【0004】[0004]
【発明が解決しようとする課題】従来のニッケル−金属
水素化物電池は、既存のニッケル−カドミウム電池より
体積エネルギ密度(Wh/リットル)は約50%以上も
高くなるのに対し、重量エネルギ密度(Wh/kg)は、
ほぼ同じであり、エネルギ密度を高くするという点から
は不十分であった。一方、空気−亜鉛二次電池では、エ
ネルギ密度は高くなるものの、電池の寿命が200サイ
クル程度であった。原因は、空気中の二酸化炭素の取り
込みなどのため、充放電と共に負極の形態変化が著しい
こと、あるいは空気極性能が低下することなどである。
また、空気極の出力密度が低く、大電流放電に不適であ
った。The conventional nickel-metal hydride battery has a volume energy density (Wh / liter) higher than that of the existing nickel-cadmium battery by about 50% or more, while the weight energy density (Wh / l) is higher than that of the existing nickel-cadmium battery. Wh / kg) is
It was almost the same, and it was insufficient from the viewpoint of increasing the energy density. On the other hand, in the air-zinc secondary battery, although the energy density was high, the battery life was about 200 cycles. The cause is that the shape of the negative electrode changes remarkably with charge and discharge due to the uptake of carbon dioxide in the air, or the air electrode performance deteriorates.
In addition, the output density of the air electrode was low, which was not suitable for large-current discharge.
【0005】本発明の目的は、従来のニッケル−金属水
素化物電池と空気電池の問題点を解決した高性能電池を
提供することにある。An object of the present invention is to provide a high performance battery which solves the problems of the conventional nickel-metal hydride battery and air battery.
【0006】[0006]
【課題を解決するための手段】本発明の特徴は、上記従
来技術の問題点を解決するために、既存の空気極を金属
水素化物と組み合わせただけでは実現できない以下の改
良を加えて大幅なエネルギ密度の向上を達成したことに
ある。すなわち、正極に空気極を用いると同時に電解質
を固体膜にし、更に、負極に高容量密度の水素吸蔵合金
を用いるとともに高出力密度が可能な有効表面積を確保
できる構造にして一次または二次電池を構成したことに
ある。In order to solve the above-mentioned problems of the prior art, the features of the present invention are greatly improved by adding the following improvements which cannot be realized only by combining an existing air electrode with a metal hydride. The purpose is to achieve improvement in energy density. That is, an air electrode is used for the positive electrode, a solid film is used for the electrolyte at the same time, a hydrogen storage alloy having a high capacity density is used for the negative electrode, and a structure capable of ensuring an effective surface area capable of high output density is used to form a primary or secondary battery. I have configured it.
【0007】高エネルギ密度化のために正極を空気極に
すると必然的に生じる問題は、空気極の寿命であり、そ
れを解決するために電解液を水酸化カリウム水溶液から
化学的安定性に優れるフッ素樹脂を骨格とするイオン交
換膜に変換した。これにより、電解質の劣化,電解質の
空気極への浸透による空気極の性能低下が抑制できる。
イオン交換膜は、陽イオン交換膜,陰イオン交換膜のい
ずれでも、本発明は構成できる。これらの電池の反応は
以下のとおりである。The problem inevitably caused when the positive electrode is changed to the air electrode to increase the energy density is the life of the air electrode, and in order to solve the problem, the electrolytic solution from the potassium hydroxide aqueous solution is excellent in chemical stability. It was converted to an ion exchange membrane having a fluororesin as a skeleton. As a result, deterioration of the electrolyte and performance deterioration of the air electrode due to permeation of the electrolyte into the air electrode can be suppressed.
The present invention can be constructed by using either a cation exchange membrane or an anion exchange membrane as the ion exchange membrane. The reactions of these batteries are as follows.
【0008】[0008]
【化1】 [Chemical 1]
【0009】(1)と(2)を比較すると、陽イオン交
換膜を用いた方が、空気中の二酸化炭素の影響を無視で
きること、および電極反応にともなう水の出入りを空気
極側だけに限定できることから有利である。また、イオ
ン交換膜を低抵抗の電解質膜として安定に作動させるに
は膜が湿潤状態であることが必要であり、膜へ水分を供
給する手段を備えなければならない。しかし、膜が濡れ
すぎであっても空気極がガス電極として作用しにくくな
るので、反応により生成した水を除去する手段を備え
て、膜を適度な湿潤状態に保持することが不可欠であ
る。膜の材料は、フッ素樹脂の骨格にスルホン酸基など
の強酸基、あるいはアルキルアンモニウム基などの強塩
基基の結合した構造の材料が電気伝導性の点から好まし
い。Comparing (1) and (2), the effect of carbon dioxide in the air can be neglected by using the cation exchange membrane, and the ingress and egress of water accompanying the electrode reaction is limited to the air electrode side. This is advantageous because it can be done. Further, in order to stably operate the ion exchange membrane as a low resistance electrolyte membrane, the membrane needs to be in a wet state, and means for supplying water to the membrane must be provided. However, even if the membrane is too wet, the air electrode becomes difficult to act as a gas electrode. Therefore, it is indispensable to provide a means for removing water generated by the reaction and keep the membrane in an appropriate wet state. The material of the film is preferably a material having a structure in which a strong acid group such as a sulfonic acid group or a strong base group such as an alkylammonium group is bonded to the skeleton of the fluororesin from the viewpoint of electrical conductivity.
【0010】負極を水素吸蔵合金とすることにより充放
電にともなう形態の変化をなくすことができ長寿命化に
寄与できる。しかし、電気容量が小さくなるのでその分
を補うために、高容量密度の材料が必要になる。従来、
ニッケル−金属水素化物電池に主として利用されてきた
LaNi5で代表されるAB5型合金の水素吸蔵量は、約
1.4wt% であるのに対し、ZrMn2 あるいはその
置換体で代表されるAB2型合金では、約1.7wt%
、さらにMg2Niあるいはその置換体で代表されるマ
グネシウム系のA2B 型合金では約3wt%まで増加す
ることが期待できる。ただし、マグネシウム系のMg2
Ni 合金では、水素吸蔵反応の平衡圧が室温では低過
ぎるので、合金化により平衡圧を高くすることが望まし
い。By using a hydrogen storage alloy for the negative electrode, it is possible to eliminate the change in the form associated with charge and discharge, which can contribute to a longer life. However, since the electric capacity becomes small, a material having a high capacity density is required to make up for it. Conventionally,
The AB 5 type alloy represented by LaNi 5 which has been mainly used for nickel-metal hydride batteries has a hydrogen storage capacity of about 1.4 wt%, whereas the AB represented by ZrMn 2 or its substitution product. For type 2 alloys, approximately 1.7 wt%
Further, it can be expected that the magnesium-based A 2 B type alloy represented by Mg 2 Ni or a substitution product thereof will increase to about 3 wt%. However, magnesium-based Mg 2
With Ni alloys, the equilibrium pressure of the hydrogen storage reaction is too low at room temperature, so it is desirable to increase the equilibrium pressure by alloying.
【0011】正極を空気極とすることの問題点である出
力密度の低下は、電解質のイオン交換膜と電極を一体化
すれば、電気抵抗および反応抵抗を低減でき、解決でき
る。一体化の方法は、電極触媒,導電剤,撥水剤などか
らなる空気極層をイオン交換膜にホットプレスにより熱
圧着するか、あるいは、イオン交換によりイオン交換膜
の表面に触媒金属を析出させる方法などが適用できる。
また、空気極中にイオン交換樹脂を分散させる技術は空
気極の有効反応表面積を増加させるのに有効である。同
様に負極の水素吸蔵合金層にイオン交換樹脂を共存させ
ることも本発明のような構造の電池では有効であること
を、発明者らは明らかにした。電極中にイオン交換樹脂
を共存させる方法は、電極作製時に他の電極材料と共に
成形する方法、あるいは電極成形後に塗布、または、含
浸などによって添加する方法などが適している。The decrease in power density, which is a problem of using the positive electrode as an air electrode, can be solved by reducing the electric resistance and the reaction resistance by integrating the electrolyte ion exchange membrane and the electrode. The method of integration is as follows: An air electrode layer composed of an electrode catalyst, a conductive agent, a water repellent agent, etc. is thermocompression-bonded to the ion exchange membrane by hot pressing, or a catalytic metal is deposited on the surface of the ion exchange membrane by ion exchange. The method etc. can be applied.
Further, the technique of dispersing the ion exchange resin in the air electrode is effective in increasing the effective reaction surface area of the air electrode. Similarly, the inventors have found that coexistence of an ion exchange resin in the hydrogen storage alloy layer of the negative electrode is also effective in the battery having the structure of the present invention. As a method of coexisting the ion exchange resin in the electrode, a method of molding together with another electrode material at the time of manufacturing the electrode, a method of applying after the electrode molding, or a method of adding by impregnation or the like is suitable.
【0012】水素吸蔵合金への水素原子の出入りを円滑
にするために、イオン交換膜の水素吸蔵合金側にも電極
触媒を添加することも電極の反応効率を向上させる上で
有効である。加えるべき触媒は、水素のイオン化反応促
進の触媒能が必要であり、より具体的には、白金,ニッ
ケル,パラジウムなどが好ましい。It is also effective to improve the reaction efficiency of the electrode by adding an electrode catalyst also to the hydrogen storage alloy side of the ion exchange membrane in order to make hydrogen atoms in and out of the hydrogen storage alloy smooth. The catalyst to be added needs to have a catalytic ability to accelerate the ionization reaction of hydrogen, and more specifically, platinum, nickel, palladium, etc. are preferable.
【0013】[0013]
【作用】本発明の作用の要点は、高エネルギ密度化のた
めに、正極を空気極とするとともに負極に水素吸蔵量の
より大きな水素吸蔵合金を用い、かつ、電解質として化
学的安定性に優れるフッ素樹脂を骨格とするイオン交換
膜を用いて長寿命化を図り、さらに高出力密度化のため
に空気極と電解質膜の一体化およびイオン交換樹脂の電
極への添加を採用したことにある。The essential point of the operation of the present invention is to use the positive electrode as an air electrode and to use a hydrogen storage alloy having a larger hydrogen storage capacity for the negative electrode in order to increase the energy density, and to have excellent chemical stability as an electrolyte. This is because an ion exchange membrane having a fluororesin as a skeleton was used to extend the life, and in order to further increase the power density, the air electrode and the electrolyte membrane were integrated and the ion exchange resin was added to the electrode.
【0014】[0014]
【実施例】以下、本発明を具体化した一実施例を図面を
用いて説明する。An embodiment of the present invention will be described below with reference to the drawings.
【0015】図1は本発明の二次電池の断面図である。
図において、1が水素吸蔵合金を主体に構成される負
極、2が電解質である陽イオン交換膜、3は正極である
空気極、4は空気の送りこまれる空気室、5は空気入
口、6は空気出口である。7は陽イオン交換膜2へ水を
供給する手段となる細管であり、8は電池を収納する電
池容器である。FIG. 1 is a sectional view of a secondary battery of the present invention.
In the figure, 1 is a negative electrode mainly composed of a hydrogen storage alloy, 2 is a cation exchange membrane that is an electrolyte, 3 is an air electrode that is a positive electrode, 4 is an air chamber into which air is sent, 5 is an air inlet, and 6 is It is an air outlet. Reference numeral 7 is a thin tube that serves as a means for supplying water to the cation exchange membrane 2, and 8 is a battery container that houses a battery.
【0016】〈実施例1〉次に、図1に示した本発明の
実施内容を説明する。負極は気孔率95%の発泡ニッケ
ルの基体に粒径100μm以下に粉砕した水素吸蔵合金
を結着剤のポリビニルアルコールにより水系スラリとし
て充填した。乾燥後、ローラプレスにより厚さを調整し
た。結着剤のポリビニルアルコール添加量は1wt%と
した。用いた水素吸蔵合金の合金組成はZrMn0.5C
r0.2Co0.3Ni1.0である。<Embodiment 1> Next, the embodiment of the present invention shown in FIG. 1 will be described. The negative electrode was prepared by filling a hydrogen-occlusion alloy crushed to a particle size of 100 μm or less on a foamed nickel substrate having a porosity of 95% as an aqueous slurry using polyvinyl alcohol as a binder. After drying, the thickness was adjusted by a roller press. The amount of polyvinyl alcohol added to the binder was 1 wt%. The alloy composition of the hydrogen storage alloy used ZrMn 0. 5 C
r 0. 2 Co 0. 3 Ni 1. 0.
【0017】空気極は、カーボンブラック粉末に20w
t%の白金を担持した電極触媒80重量部と、結着剤の
ポリテトラフルオロエチレン微粉末20重量部へ、イオ
ン交換樹脂として液状イオン交換樹脂(Aリットルdrich
Chemicaリットル製,Nafion液)を乾燥後イオン交換樹
脂の重量に換算して20重量部になるように添加したペ
ーストを多孔質の炭素繊維板電極支持体へ塗布して形成
した。The air electrode is carbon black powder 20w
80 parts by weight of an electrode catalyst supporting t% of platinum and 20 parts by weight of polytetrafluoroethylene fine powder as a binder are added to a liquid ion exchange resin (A liter drich
Chemica liter, Nafion solution) was dried and then added so as to be 20 parts by weight in terms of the weight of the ion-exchange resin, and the paste was applied to a porous carbon fiber plate electrode support.
【0018】負極へ液状イオン交換樹脂を1mg/cm2 含
浸したのち、電解質としてのフッ素樹脂−スルホン酸系
の陽イオン交換膜(Du Pont社製のNafion 117)と空
気極を重ね合わせたのち120℃,200kg/cm2 の条
件で熱圧着し一体化した。得られた一体化電極を図1に
示す電池容器に収納して電池を作製した。電極有効電極
面積は70cm2 であり、電池の充填容量は、4000m
Ahである。室温下でこの電池に7の水供給細管から水
を0.11ミリリットル/分 の速度で供給し、かつ空気
を1リットル/分流通しながら2Aの電流で2時間充電
し、4Aで放電した。得られた放電特性を図2のAに示
す。3700mAhの放電容量が得られた。The negative electrode was impregnated with a liquid ion exchange resin at 1 mg / cm 2, and a fluororesin-sulfonic acid type cation exchange membrane (Nafion 117 manufactured by Du Pont) as an electrolyte was superposed on the air electrode. They were integrated by thermocompression bonding under the conditions of ℃ and 200 kg / cm 2 . The obtained integrated electrode was housed in the battery container shown in FIG. 1 to prepare a battery. Electrode Effective electrode area is 70 cm 2 and the filling capacity of the battery is 4000 m
It is Ah. Water was supplied at a rate of 0.11 ml / min to the battery at room temperature at a rate of 0.11 ml / min, and air was flowed at 1 l / min for 2 hours at a current of 2 A and discharged at 4 A. The obtained discharge characteristics are shown in A of FIG. A discharge capacity of 3700 mAh was obtained.
【0019】〈実施例2〉水素吸蔵合金にLaNi4.4
Co0.3Aリットル0.3 を用いた以外はすべて実施例1
と同じ条件で作製評価した電池の放電特性を図2のBに
示す。3030mAh の放電容量が得られた。[0019] <Example 2> hydrogen storage alloy LaNi 4. 4
Co 0. 3 A liter 0. All 3 except for using Example 1
2B shows the discharge characteristics of the battery manufactured and evaluated under the same conditions as described above. A discharge capacity of 3030 mAh was obtained.
【0020】〈比較例〉比較例として、従来技術のニッ
ケル−金属水素化物電池を作製した。金属水素化物電極
は実施例の負極と同様に作製した。ニッケル極は通常の
焼結式ニッケル極である。電解液には31wt%の水酸
化カリウム水溶液を用いた。実施例と同じ大きさの電極
容器に収納し、1Aの電流で2.5 時間充電し、2Aで
放電し、充放電評価をした。得られた結果を図2のCに
示す。放電容量は1800mAh であった。実施例になる電池
は従来技術になるニッケル−金属水素化物電池よりも大
きな放電容量の得られる高エネルギ密度電池である。<Comparative Example> As a comparative example, a conventional nickel-metal hydride battery was manufactured. The metal hydride electrode was prepared in the same manner as the negative electrode of the example. The nickel electrode is a normal sintered nickel electrode. A 31 wt% potassium hydroxide aqueous solution was used as the electrolytic solution. It was stored in an electrode container having the same size as that of the example, charged at a current of 1 A for 2.5 hours, discharged at 2 A, and evaluated for charge and discharge. The obtained results are shown in C of FIG. The discharge capacity was 1800 mAh. The example battery is a high energy density battery that provides a larger discharge capacity than the nickel-metal hydride battery of the prior art.
【0021】[0021]
【発明の効果】本発明によれば、従来技術よりも容量密
度とエネルギ密度が大幅に向上した高性能二次電池が得
られた。According to the present invention, a high performance secondary battery having a significantly improved capacity density and energy density as compared with the prior art was obtained.
【図1】本発明になる電池の構造を示す断面図。FIG. 1 is a cross-sectional view showing the structure of a battery according to the present invention.
【図2】本発明になる電池と従来技術になる電池の放電
特性図。FIG. 2 is a discharge characteristic diagram of a battery according to the present invention and a battery according to the related art.
1…水素吸蔵合金負極、2…陽イオン交換膜、3…空気
極、4…空気室、5…空気入口、6…空気出口、7…水
供給細管、8…電池容器。DESCRIPTION OF SYMBOLS 1 ... Hydrogen storage alloy negative electrode, 2 ... Cation exchange membrane, 3 ... Air electrode, 4 ... Air chamber, 5 ... Air inlet, 6 ... Air outlet, 7 ... Water supply thin tube, 8 ... Battery container.
Claims (7)
拡散電極を正極とし、フッ素樹脂を骨格とするイオン交
換膜を電解質とし、水素を吸蔵,放出することのできる
水素吸蔵合金を負極作用物質とすることを特徴とする電
池。1. A gas diffusion electrode in which oxygen in the air acts as an active material serves as a positive electrode, and an ion exchange membrane having a fluororesin skeleton serves as an electrolyte, and a hydrogen storage alloy capable of storing and releasing hydrogen as a negative electrode. A battery characterized by being a substance.
少なくとも一方に水を供給する機構を備えた電池。2. The battery according to claim 1, comprising a mechanism for supplying water to at least one of the positive electrode and the negative electrode.
フッ素樹脂を骨格とする陽イオン交換膜である電池。3. The battery according to claim 1, wherein the electrolyte is a cation exchange membrane having a fluororesin as a skeleton.
フッ素樹脂を骨格とする陰イオン交換膜である電池。4. The battery according to claim 1, wherein the electrolyte is an anion exchange membrane having a fluororesin as a skeleton.
負極の水素吸蔵合金層にイオン交換樹脂が共存する電
池。5. The battery according to claim 1, 2, 3 or 4, wherein an ion exchange resin coexists in the hydrogen storage alloy layer of the negative electrode.
前記イオン交換膜の水素吸蔵合金層側に白金触媒が存在
する電池。6. The method according to claim 1, 2, 3, 4 or 5.
A battery in which a platinum catalyst is present on the hydrogen storage alloy layer side of the ion exchange membrane.
て、前記負極の水素吸蔵合金がLaNi5 で代表される
AB5 型合金、ZrMn2 あるいはその置換体で代表さ
れるAB2型合金、またはMg2Niあるいはその置換体
で代表されるマグネシウム系のA2B 型合金のうちの少
なくとも1種類からなる電池。7. claim in 2, 3, 4, 5 or 6, wherein the negative electrode of the AB 5 type alloy hydrogen storage alloy represented by LaNi 5, AB 2 represented by ZrMn 2 or derivatives thereof Type alloy, or a battery made of at least one of magnesium-based A 2 B type alloys represented by Mg 2 Ni or a substitution product thereof.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4054782A JPH05275108A (en) | 1992-03-13 | 1992-03-13 | Battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4054782A JPH05275108A (en) | 1992-03-13 | 1992-03-13 | Battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH05275108A true JPH05275108A (en) | 1993-10-22 |
Family
ID=12980343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4054782A Pending JPH05275108A (en) | 1992-03-13 | 1992-03-13 | Battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH05275108A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002017428A1 (en) * | 2000-08-22 | 2002-02-28 | Hitachi Maxell, Ltd. | Air-hydrogen cell |
| JP2007073243A (en) * | 2005-09-05 | 2007-03-22 | Toyota Auto Body Co Ltd | Electrode structure for fuel cell |
| WO2013100087A1 (en) * | 2011-12-28 | 2013-07-04 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary batteries |
| WO2013100079A1 (en) * | 2011-12-28 | 2013-07-04 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary batteries |
| US8501349B2 (en) | 2008-09-24 | 2013-08-06 | Alliance For Sustainable Energy, Llc | Hydrogen-based electrochemical energy storage |
| US9905875B2 (en) | 2011-12-28 | 2018-02-27 | Asahi Kasei Kabushiki Kaisha | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| US10211474B2 (en) | 2011-12-28 | 2019-02-19 | Asahi Kasei E-Materials Corporation | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
-
1992
- 1992-03-13 JP JP4054782A patent/JPH05275108A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6905794B2 (en) | 2000-08-22 | 2005-06-14 | Hitachi Maxell, Ltd. | Air-hydrogen battery |
| WO2002017428A1 (en) * | 2000-08-22 | 2002-02-28 | Hitachi Maxell, Ltd. | Air-hydrogen cell |
| JP2007073243A (en) * | 2005-09-05 | 2007-03-22 | Toyota Auto Body Co Ltd | Electrode structure for fuel cell |
| US8501349B2 (en) | 2008-09-24 | 2013-08-06 | Alliance For Sustainable Energy, Llc | Hydrogen-based electrochemical energy storage |
| CN104011921A (en) * | 2011-12-28 | 2014-08-27 | 旭化成电子材料株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| WO2013100079A1 (en) * | 2011-12-28 | 2013-07-04 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary batteries |
| WO2013100087A1 (en) * | 2011-12-28 | 2013-07-04 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary batteries |
| JPWO2013100087A1 (en) * | 2011-12-28 | 2015-05-11 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| JPWO2013100079A1 (en) * | 2011-12-28 | 2015-05-11 | 旭化成イーマテリアルズ株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| CN104011921B (en) * | 2011-12-28 | 2016-03-09 | 旭化成电子材料株式会社 | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| US9799906B2 (en) | 2011-12-28 | 2017-10-24 | Asahi Kasei Kabushiki Kaisha | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| US9905875B2 (en) | 2011-12-28 | 2018-02-27 | Asahi Kasei Kabushiki Kaisha | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| US10211474B2 (en) | 2011-12-28 | 2019-02-19 | Asahi Kasei E-Materials Corporation | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
| US10256493B2 (en) | 2011-12-28 | 2019-04-09 | Asahi Kasei Kabushiki Kaisha | Redox flow secondary battery and electrolyte membrane for redox flow secondary battery |
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