JPS5846441B2 - Hydrogen storage structure with electrode part - Google Patents
Hydrogen storage structure with electrode partInfo
- Publication number
- JPS5846441B2 JPS5846441B2 JP53103514A JP10351478A JPS5846441B2 JP S5846441 B2 JPS5846441 B2 JP S5846441B2 JP 53103514 A JP53103514 A JP 53103514A JP 10351478 A JP10351478 A JP 10351478A JP S5846441 B2 JPS5846441 B2 JP S5846441B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- hydrogen storage
- electrode
- metal
- storage
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/065—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloys; by dehydriding metallic substances
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
-
- 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
- Y02E60/32—Hydrogen storage
-
- 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
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Description
【発明の詳細な説明】
本発明は電気分解によって発生させた水素を金属水素化
物の形態で貯蔵する構造体およびその利用に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a structure for storing hydrogen generated by electrolysis in the form of a metal hydride and its use.
電気分解以外の方法で発生させた水素を金属水素化物の
形態で貯蔵し、利用する際にも本発明の構造体を利用す
ることができる。The structure of the present invention can also be used when hydrogen generated by a method other than electrolysis is stored and utilized in the form of a metal hydride.
電気エネルギーを電気分解によって水素の形にして貯蔵
、輸送、利用する方法は原料に資源的な制約がなく、最
終酸化性成物が水であるので自然の環境を乱すことが少
なく、清浄な燃料として用いることができるなど、多く
の利点を有するのでこの方面での研究が広く進められて
いる。The method of storing, transporting, and using electrical energy in the form of hydrogen through electrolysis has no resource constraints on raw materials, and since the final oxidizing product is water, it does not disturb the natural environment and is a clean fuel. Because it has many advantages, such as being able to be used as a
水素をこのような二次エネルギーとして利用する場合、
一番問題となるのはエネルギーの変換効率であって、従
来から電気分解による水素の発生、発生した水素の貯蔵
および輸送、最終の利用方法の各段階について研究改良
が行われている。When hydrogen is used as secondary energy,
The most important issue is energy conversion efficiency, and research and improvement have been conducted at each stage of hydrogen generation through electrolysis, storage and transportation of the generated hydrogen, and final usage.
本発明の目的も前記の研究改良の目的と一致するが、従
来のものと比較して最終の利用形態を含めた全体として
のエネルギー効率が高く、しかも非常に利用し易い形態
にしたことを特徴とするものである。The purpose of the present invention also coincides with the purpose of the above-mentioned research and improvement, but it is characterized by having a form that has higher overall energy efficiency, including the final usage form, and is extremely easy to use compared to conventional ones. That is.
先ず第一に我国において、いかなる場合に電気エネルギ
ーを電解によって水素の形にすることが必要になるかを
考えるならば、先ず、水素を化石燃料の代替物として使
用する場合である。First of all, if we consider under what circumstances it would be necessary to convert electrical energy into hydrogen through electrolysis in our country, the first would be when hydrogen is used as a substitute for fossil fuels.
この場合、水素ガスそのものは化石燃料の代替物として
充分な特性を有しているが、問題は貯蔵形態である。In this case, hydrogen gas itself has sufficient properties as a substitute for fossil fuels, but the problem is the storage form.
気体水素は取扱いが難かしく、液体水素は貯蔵、取扱い
、その他にも問題がある、化石燃料と略同等の取扱がで
きる貯蔵形態は本発明において使用されている水素貯蔵
用金属材料に金属水素化物を形で吸蔵させる方法である
。Gaseous hydrogen is difficult to handle, and liquid hydrogen has storage, handling, and other problems.A storage form that can be handled almost in the same way as fossil fuels is metal hydride as the metal material for hydrogen storage used in the present invention. This is a method of occluding in the form of
第二に、夜間の余剰電力の貯蔵手段とする場合が考えら
れる。Second, it may be used as a means of storing surplus electricity at night.
現在では揚水式発電でこの問題に対処しているが将来も
同様であろう。Currently, pumped storage power generation is addressing this problem, and the same will likely be the case in the future.
しかし将来化石燃料が不足し、電力が原子力発電、その
他火力発電以外の方法で供給されるようになった時、化
石燃料の不足を補うため夜間の余剰電力は水素ガス生成
に用いられることが充分考えられる。However, in the future when there is a shortage of fossil fuels and electricity is supplied by nuclear power generation or other methods other than thermal power generation, it will be sufficient to use surplus electricity at night to generate hydrogen gas to compensate for the shortage of fossil fuels. Conceivable.
第三に太陽電池によって得た電力の貯蔵方法としてであ
る。Thirdly, it is a method of storing electricity obtained by solar cells.
太陽エネルギーのような単位面積、単位時間当りのエネ
ルギー量の少いエネルギー(薄いエネルギー)は何等か
の方法で濃縮しない限り用途が極めて限定されてしまう
。Energy such as solar energy, which has a small amount of energy per unit area and unit time (thin energy), has extremely limited uses unless it is concentrated in some way.
水素に変換しておけば種々の利用方法が可能である。If it is converted to hydrogen, it can be used in various ways.
薄いエネルギーの集積にはなるべくエネルギー効率の高
い方法を用いなければならない。The most energy efficient method must be used for thin energy accumulation.
例え水素ガスを発生させても、これをボンベに圧縮して
詰めたり、冷却して液化するなどの工程を通せばそれら
の仕事に要するエネルギー損失は極めて太きいため実際
的ではない。Even if hydrogen gas were to be generated, it would be impractical to compress it into cylinders, cool it, and liquefy it, as the energy loss required for these tasks would be extremely large.
この場合も金属水素化物とする方法が好しく、しかも発
生した水素を一度集めてから金属に吸蔵させるよりも、
その場で直ちに金属に吸蔵させる方がエネルギー効率の
点からも好ましいことである。In this case as well, it is preferable to form a metal hydride, and moreover, rather than collecting the generated hydrogen once and then storing it in the metal,
From the point of view of energy efficiency, it is also preferable to occlude the metal immediately on the spot.
第四に、将来、鉛電池に取ってかわる性能を有する水素
燃料電池ができたときの燃料源として考えられる。Fourth, it can be considered as a fuel source when hydrogen fuel cells with performance that can replace lead batteries are created in the future.
この場合にも金属水素化物の形態であることが取扱いの
点から好ましい。In this case as well, it is preferable to use the form of a metal hydride from the viewpoint of handling.
以上を要するに、将来少くとも我国で電気分解によって
得た水素を貯蔵する方法としては金属水素化物とする方
法が最適であり、その中でも取扱が楽で最終の利用形態
に至るまでのエネルギー損失が少いものが好ましいとい
える。In summary, in the future, at least in Japan, the best way to store hydrogen obtained through electrolysis is to use metal hydrides, which are easier to handle and have less energy loss up to the final form of use. It can be said that a sweet potato is preferable.
上記の目的を達成するために従来技術を利用した場合の
欠点と本発明による構造体を用いた場合の利点を比較し
ながら述べれば以下のようである。The disadvantages of using the conventional technology and the advantages of using the structure according to the present invention in order to achieve the above object are as follows.
またそれらの欠点は基本的には従来技術が電気分解によ
る水素の発生、水素の貯蔵、輸送、水素の利用のいずれ
か一つに偏して追及されており、全体としての効率をあ
まり考慮していない結果とも考えられる。In addition, these drawbacks are basically that the conventional technology pursues only one of hydrogen generation by electrolysis, hydrogen storage, transportation, and hydrogen utilization, and does not give much consideration to overall efficiency. This may also be due to the fact that it is not.
次に本発明の電極部を有する水素貯蔵用構造体について
述べる。Next, a hydrogen storage structure having an electrode portion according to the present invention will be described.
すなわち本発明の構造体の特徴は水素透過型電極と、水
素と化合物を作る金属体つまり水素貯蔵ができる金属体
とを一体化し、これを電気絶縁性材料で上記水素透過型
電極部を除く全表面を被覆した点にある。In other words, the structure of the present invention is characterized by integrating a hydrogen-permeable electrode with a metal body that forms a compound with hydrogen, that is, a metal body that can store hydrogen, and using an electrically insulating material to cover the entire structure except for the hydrogen-permeable electrode part. It is at the point where the surface is covered.
その作用上の特徴は電気分解によって発生した水素が電
解液側に泡出することなく、はとんど全べて水素透過型
電極を透過して直ちに水素貯蔵用金属体と反応して金属
水素化物を生成することと、電気分解のカソード部とし
て用いず単にその水素貯蔵用金属材料の平衡水素圧より
高い雰囲気中に置くことにより水素ガスを吸蔵させるこ
とかできる点と、逆に平衡水素圧より低い水素分圧の雰
囲気中に置くことにより純度の高い水素ガスを放出する
点と、水素燃料電池の水素貯蔵部付きの水素極として用
いることができる点にある。Its functional feature is that the hydrogen generated by electrolysis does not bubble out into the electrolyte, and almost all of it passes through the hydrogen-permeable electrode and immediately reacts with the hydrogen storage metal body, producing metallic hydrogen. hydrogen gas can be stored by simply placing it in an atmosphere higher than the equilibrium hydrogen pressure of the metal material for hydrogen storage without using it as a cathode part of electrolysis, and conversely, the equilibrium hydrogen pressure The two advantages are that it releases highly pure hydrogen gas by placing it in an atmosphere with a lower hydrogen partial pressure, and that it can be used as a hydrogen electrode with a hydrogen storage section in a hydrogen fuel cell.
さらにまた燃料電池や電気分解装置に用いた場合、その
構造上の特徴を生かして水素の貯蔵、放出に伴う発熱、
吸熱をエネルギー損失が少くなる方法で利用できるよう
にすることが可能である点も特徴にあげられる。Furthermore, when used in fuel cells or electrolyzers, the structural features of hydrogen can be utilized to reduce the heat generated by hydrogen storage and release.
Another feature is that it is possible to utilize endothermic heat in a way that reduces energy loss.
この点に関しては後に電解装置および燃料電池の説明に
おいて詳しく述べる。This point will be discussed in detail later in the description of the electrolyzer and fuel cell.
本発明における水素透過型電極とは「電気化学および工
業物理学J VOl、40.NO,2,127ページ以
下、特公昭46−5561、特公昭418416、特公
昭46−25423号公報に記載されている水素透過能
を有する膜を用いた電極であって、金属パラジウム、パ
ラジウム−銀合金、パラジウム−金合金、パラジウム−
銀−金合金などの膜が用いられる。The hydrogen-permeable electrode in the present invention is described in "Electrochemistry and Industrial Physics J VOl, 40. NO, 2, 127 et seq., in Japanese Patent Publications No. 5561-1982, No. 418-416, and No. 25423-1982. An electrode using a membrane having a hydrogen permeability of metal palladium, palladium-silver alloy, palladium-gold alloy, palladium-
A film of silver-gold alloy or the like is used.
またその膜の表面にパラジウム黒、パラジウム−白金ブ
ラック被覆を施したものも水素透過型電極膜として用い
られる。Further, membranes whose surfaces are coated with palladium black or palladium-platinum black can also be used as hydrogen-permeable electrode membranes.
また水素貯蔵用金属材料とは水素吸蔵量が多く、金属−
水素ガスの相平衡条件が水素貯蔵用として適しているも
のであって、例えば特公昭49−34315、特公昭3
6−23479号公報等に記載されており、その他、鉄
−チタン、マグネシウム−ニッケル合金、金属ニオブ、
金属バナジウム、その他が知られているが、本発明にお
いてはこれらの材料に限定されるものではない。In addition, metal materials for hydrogen storage have a large hydrogen storage capacity,
The phase equilibrium conditions of hydrogen gas are suitable for hydrogen storage, for example, Japanese Patent Publication No. 49-34315,
6-23479, etc., and in addition, iron-titanium, magnesium-nickel alloy, metallic niobium,
Although metal vanadium and others are known, the present invention is not limited to these materials.
水素貯蔵用金属は一般に水素を吸蔵するときには発熱し
、放出するときには吸熱する。Hydrogen storage metals generally generate heat when storing hydrogen, and absorb heat when releasing hydrogen.
第1図は電気分解による水素を水素貯蔵用金属材料に吸
蔵させる従来の方法を示す説明図であって、水素透過型
電極を用いたものが前記の目的を達成するための従来の
技術として最も優れていると考えられることから、水素
ガス発生部は特公昭46−5561号公報記載のものに
倣っている。Figure 1 is an explanatory diagram showing a conventional method of occluding hydrogen by electrolysis into a metal material for hydrogen storage, and the method using a hydrogen-permeable electrode is the most conventional technique for achieving the above purpose. Since it is considered to be superior, the hydrogen gas generating section is modeled after that described in Japanese Patent Publication No. 46-5561.
1は対極、2は水素透過型電極膜、3は電極支持体、4
は水素ガス室である。1 is a counter electrode, 2 is a hydrogen permeable electrode membrane, 3 is an electrode support, 4
is a hydrogen gas chamber.
また5は電解液(ホ)、6は電解槽、Iは電源、8は水
素貯蔵用金属、16はその容器、10はコックである。Further, 5 is an electrolytic solution (E), 6 is an electrolytic tank, I is a power source, 8 is a hydrogen storage metal, 16 is a container thereof, and 10 is a cock.
電解液(ホ)の電気分解により発生する水素は条件が適
当であれば水素透過型電極膜2を通過してほぼ100%
の電流効率で水素ガス室4に集まり、電解液(水)側に
泡出することはない。If the conditions are suitable, almost 100% of the hydrogen generated by electrolysis of the electrolytic solution (e) passes through the hydrogen-permeable electrode membrane 2.
Hydrogen collects in the gas chamber 4 with a current efficiency of , and does not bubble out to the electrolyte (water) side.
例えば第2図は電極の説明図であるが、水素透過膜とし
て通常約Q、 l ynx厚のパラジウム板a(純度9
9.9%)の1面にパラジウム黒を20僧/−で被覆し
くb)、他面にパラジウム−白金混合黒(パラジウム黒
i o onyi7cyi、白金黒1■/瀝)を被覆(
C)シたものを用い、パラジウム黒側をガス室側とし、
5規定の水酸化カリウムを電解液として、25℃で電気
分解を行った場合、30〜120 rm A/crAの
電気密度において、水素捕集効率(電気効率)は92〜
100%であることが知られている。For example, Fig. 2 is an explanatory diagram of an electrode, and as a hydrogen permeable membrane, a palladium plate a (purity 9
9.9%), one side is coated with palladium black at a rate of 20 mm/-, and the other side is coated with palladium-platinum mixed black (palladium black io onyi 7 cyi, platinum black 1 mm/g) (b).
C) Use a metal plate with the palladium black side facing the gas chamber,
When electrolysis is performed at 25°C using 5N potassium hydroxide as an electrolyte, the hydrogen trapping efficiency (electrical efficiency) is 92 to 120 rmA/crA at an electrical density of 30 to 120 rmA/crA.
It is known that it is 100%.
発生した水素ガスは例えば特公昭49−34315号に
示されているような水素貯蔵用金属の容器内に導かれ、
そこで水素貯蔵用金属と接触し、吸収される。The generated hydrogen gas is led into a hydrogen storage metal container as shown in Japanese Patent Publication No. 49-34315, for example.
There, it comes into contact with the hydrogen storage metal and is absorbed.
水素貯蔵用金属は水素を貯蔵する際に発熱するので、こ
のような従来の電気分解装置を用いた場合、水素の貯蔵
量を増加させるためには金属体を冷却しなければならず
、水素吸蔵時の発熱は完全にエネルギー損失として利用
されないままに終ってしまう欠点がある。Hydrogen storage metal generates heat when storing hydrogen, so when using such a conventional electrolyzer, the metal body must be cooled in order to increase the amount of hydrogen stored, and the hydrogen storage The disadvantage is that the heat generated during this process ends up being completely unused as energy loss.
水素透過型電極を用いない通常の電気分解装置において
も事情は全く同様である。The situation is exactly the same in ordinary electrolyzers that do not use hydrogen permeable electrodes.
これに対し、本発明の電極部を有する水素貯蔵用構造体
は第3図の説明図のように水素貯蔵用金属材料8の表面
に水素透過膜2を設けたものであり、この膜2を上記の
金属材料8表面に設ける方法としては電気メッキ、無電
解メッキ、蒸着等の物理的・化学的手段を用いる。On the other hand, the hydrogen storage structure having an electrode part of the present invention has a hydrogen permeable membrane 2 provided on the surface of a hydrogen storage metal material 8, as shown in the explanatory diagram of FIG. As a method for providing on the surface of the metal material 8, physical/chemical means such as electroplating, electroless plating, and vapor deposition are used.
水素透過型電極膜2をさらに詳細に説明すると第3図の
説明図において、Aはパラジウム−金−銀合金の膜、B
はパラジウムブラック膜、Cは白金ブラック膜であると
き最も良好である。To explain the hydrogen permeable electrode membrane 2 in more detail, in the explanatory diagram of FIG. 3, A is a palladium-gold-silver alloy membrane, B is
It is best when C is a palladium black film and C is a platinum black film.
9は電気絶縁シールである。9 is an electrical insulation seal.
また外見上第3図に類似した構造になるが、水素透過型
電極膜2は水素貯蔵用金属体8の上に形成されるのでは
なく、別個に形成されたものであり、水素貯蔵用金属体
8とは機械的に密着しているに過ぎないもので、また、
電気絶縁シール9で被覆するのではなく電気絶縁性容器
あるいは電気絶縁性シールを施した容器9′となるのが
ある。Although the structure looks similar to that shown in FIG. 3 in appearance, the hydrogen permeable electrode film 2 is not formed on the hydrogen storage metal body 8 but is formed separately. The body 8 is only in close contact with the body 8 mechanically, and
Instead of being covered with an electrically insulating seal 9, it may be an electrically insulating container or a container 9' provided with an electrically insulating seal.
この構造体は水素貯蔵用金属体8が水素を吸蔵した時、
粉末状になり易いものの場合に用いて好適である。When the hydrogen storage metal body 8 occludes hydrogen, this structure
It is suitable for use in cases where the material tends to become powdery.
さらにこの場合は電極膜は第3図に示した構造のものを
用いた場合、水素貯蔵用金属体が水素を吸蔵して粉末に
なり電極膜2との密着性が低下しても、水素の吸蔵、放
出の能力の低下を少くすることができる。Furthermore, in this case, if the electrode film has the structure shown in Figure 3, even if the hydrogen storage metal body absorbs hydrogen and becomes powder, reducing its adhesion to the electrode film 2, the hydrogen storage metal body absorbs hydrogen and becomes powder. It is possible to reduce the decrease in storage and release capabilities.
このような容器型の構造体は水素貯蔵用金属材料の平衡
水素圧が1気圧よりかなり高い耐圧性の容器9′を用い
なければならない場合に用いられる。Such a container-type structure is used when it is necessary to use a pressure-resistant container 9' in which the equilibrium hydrogen pressure of the hydrogen storage metal material is considerably higher than 1 atm.
このようにしてなった本発明の構造体を第4図の説明図
のように取付け、電極膜だけが電解液と接するようにし
てカソードとして電気分解を行うと発生した水素の一部
は水素ガスとなって電極膜表面から泡出するが他部は水
素透過型電極を透過して、ガス状態を経過することなく
、水素貯蔵用金属に水素化物として結合して吸蔵される
。When the structure of the present invention thus obtained is attached as shown in the explanatory diagram of Fig. 4 and electrolysis is performed as a cathode with only the electrode film in contact with the electrolyte, some of the hydrogen generated becomes hydrogen gas. The hydrogen bubbles out from the surface of the electrode membrane, but the other part passes through the hydrogen-permeable electrode and is bonded to the hydrogen storage metal as a hydride and occluded without passing through the gas state.
適当な電解液(例えばアルカリ性の水)と電極膜面に加
工(例えばパラジウム−白金ブラックで被覆する)した
ものを用いれば電極表面から泡出する水素ガスは極めて
少くなり、電気分解の条件を適当にすればほとんど全く
泡出現象は見られなくなり、水素へのエネルギーの変換
効率は従来のものと変らなくなる。If a suitable electrolyte (e.g. alkaline water) and an electrode membrane surface treated (e.g. coated with palladium-platinum black) are used, the amount of hydrogen gas bubbling from the electrode surface will be extremely small, and the electrolysis conditions can be adjusted appropriately. If this is done, almost no bubbling phenomenon will be observed, and the efficiency of energy conversion into hydrogen will remain the same as in the conventional method.
第4図に示したこの電気分解装置は以下の点において第
1図に示した従来法による装置よりエネルギー効率がは
るかに優れている。This electrolyzer shown in FIG. 4 is much more energy efficient than the conventional device shown in FIG. 1 in the following respects.
水素透過型電極膜の透過効率は温度の上昇とともに高く
なることが知られており、一方、水素貯蔵用金属は水素
を吸蔵する際発熱する。It is known that the permeation efficiency of hydrogen-permeable electrode membranes increases as the temperature rises, while hydrogen storage metals generate heat when storing hydrogen.
従って電極膜や電解液が加熱され、透過効率が高くなる
。Therefore, the electrode membrane and electrolyte are heated, and the permeation efficiency is increased.
また電解液の温度の上昇と共に電力効率が向上する。Furthermore, power efficiency improves as the temperature of the electrolyte increases.
さらに水素貯蔵用金属は冷却されるために水素の貯蔵量
が増加する。Furthermore, since the hydrogen storage metal is cooled, the amount of hydrogen stored increases.
よって全体としてエネルギー効率が顕著に向上する。Therefore, overall energy efficiency is significantly improved.
従来法においては電解液を加熱し、水素貯蔵用金属を冷
却すれば電気エネルギーの変換効率を向上できるが、こ
の加熱、冷却のためのエネルギーを外部に求めれば、全
体としてのエネルギー効率を向上させることはできなか
った。In the conventional method, electrical energy conversion efficiency can be improved by heating the electrolyte and cooling the hydrogen storage metal, but if the energy for this heating and cooling is obtained externally, the overall energy efficiency can be improved. I couldn't do that.
水素貯蔵用金属は室温付近で平衡水素圧が1気圧以上の
ものと、それ以下のものとに大別されるが、前者につい
ては従来水素ガスを吸蔵させるには平衡水素圧以上に水
素ガスを加圧する必要があった。Hydrogen storage metals can be broadly classified into those with an equilibrium hydrogen pressure of 1 atm or higher near room temperature, and those with an equilibrium hydrogen pressure of 1 atm or less, and those with an equilibrium hydrogen pressure of less than 1 atm. Conventionally, in order to store hydrogen gas, it is necessary to store hydrogen gas above the equilibrium hydrogen pressure. It was necessary to pressurize.
本発明による構造体を用いれば10気圧程度までならば
効率は多少(10係程度)低下するが伺等加圧装置を必
要とせずに水素を平衡水素圧が1気圧以上である水素貯
蔵用金属材料に吸蔵させることが可能である。If the structure according to the present invention is used, the efficiency will decrease somewhat (about 10 factors) when the pressure is up to about 10 atm, but hydrogen storage metal with an equilibrium hydrogen pressure of 1 atm or more can store hydrogen without the need for a pressurizing device. It is possible to occlude it in the material.
本発明の構造体を用いた電気分解装置は電気分解の電源
として、太陽電池を用いた場合、特に良好である。The electrolyzer using the structure of the present invention is particularly good when a solar cell is used as the power source for electrolysis.
すなわち本発明における電気分解装置は、これまで述べ
たようにエネルギー変換効率が従来のものよりも良好で
あるが、水素と水素貯蔵用金属材の反応が律速になり勝
ちであるので、電流密度が低い場合に良好な結果を得る
からである。In other words, the electrolyzer of the present invention has better energy conversion efficiency than conventional ones as described above, but the reaction between hydrogen and hydrogen storage metal material tends to be rate-limiting, so the current density is low. This is because good results are obtained when the value is low.
次に本発明の電極部を有する水素貯蔵用構造体ノ燃料電
池への利用について述べる。Next, the use of the hydrogen storage structure having the electrode portion of the present invention in a fuel cell will be described.
第5図は従来の水素−酸素燃料電池の概念を示す説明図
であり、11は酸素極、12は水素極、5は電解液であ
る。FIG. 5 is an explanatory diagram showing the concept of a conventional hydrogen-oxygen fuel cell, where 11 is an oxygen electrode, 12 is a hydrogen electrode, and 5 is an electrolyte.
13は酸素または空気導入部、14は水素導入部である
。13 is an oxygen or air introduction section, and 14 is a hydrogen introduction section.
発生した電気は電力消費体15において利用される。The generated electricity is used in the power consumer 15.
本発明の電極部を有する水素貯蔵用構造体を燃料電池に
用いるに際しては、空気(空中の酸素)を用いる型の燃
料電池が最も利用価値が大きい。When using the hydrogen storage structure having the electrode part of the present invention in a fuel cell, a type of fuel cell that uses air (airborne oxygen) has the greatest utility value.
第6図は本発明の電極部を有する水素貯蔵用構造体を用
いた燃料電池の概略を示す説明図であって、水素供与機
構のみが従来例に示す第5図と比べて異っている。FIG. 6 is an explanatory diagram schematically showing a fuel cell using a hydrogen storage structure having an electrode portion of the present invention, and is different from FIG. 5 showing a conventional example only in the hydrogen donor mechanism. .
すなわち水素を吸蔵させた本発明の電極部を有する水素
貯蔵用構造体を水素極付き水素供与体として用いるもの
である。That is, the hydrogen storage structure having the electrode portion of the present invention that occludes hydrogen is used as a hydrogen donor with a hydrogen electrode.
このようにすると、従来法に比較してエネルギー効率の
点で以下述べるような利点が得られる。In this way, the following advantages can be obtained in terms of energy efficiency compared to the conventional method.
すなわち従来法においては作動させることによって温度
が上昇しすぎてしまうことを防ぐために燃料電池はある
程度冷却する必要があった。That is, in the conventional method, it was necessary to cool the fuel cell to some extent to prevent the temperature from rising too much during operation.
また水素ガスをボンベから供給する場合にはボンベに詰
めるためのエネルギーが必要である。Furthermore, when hydrogen gas is supplied from a cylinder, energy is required to fill the cylinder.
一方、本発明による燃料電池においては作動させた時に
発生する熱は水素貯蔵用金属体から水素を解離させるこ
とに利用される。On the other hand, in the fuel cell according to the present invention, the heat generated during operation is used to dissociate hydrogen from the hydrogen storage metal body.
すなわち、水素貯蔵用金属から水素が解離するときに吸
熱反応して燃料電池が作動するとき発熱反応によって発
生する熱が利用される。That is, when hydrogen is dissociated from the hydrogen storage metal, an endothermic reaction occurs, and the heat generated by the exothermic reaction when the fuel cell operates is utilized.
従って、エネルギー効率が従来のものより著しく向上す
る。Therefore, the energy efficiency is significantly improved compared to the conventional one.
また本発明の電極部を有する水素貯蔵用構造体は電気分
解による水素を貯蔵の際ばかりでなく、その他の方法に
よる水素を貯蔵、利用する際にも用いることができる。Furthermore, the hydrogen storage structure having the electrode portion of the present invention can be used not only for storing hydrogen by electrolysis, but also for storing and utilizing hydrogen by other methods.
すなわち前記本発明構造体を水素分圧が水素貯蔵用金属
材の平衡水素圧より高い雰囲気中に置けば、水素だけが
水素透過型電極膜を通過して貯蔵される。That is, if the structure of the present invention is placed in an atmosphere where the hydrogen partial pressure is higher than the equilibrium hydrogen pressure of the hydrogen storage metal material, only hydrogen will pass through the hydrogen permeable electrode membrane and be stored.
水素貯蔵用金属だけでも、このような作用はあるが、雰
囲気中の水素以外の成分例えば一酸化炭素、2000
p、p、 m以上の酸素などによって水素の吸蔵能力は
劣化する。Hydrogen storage metals alone have this effect, but components other than hydrogen in the atmosphere, such as carbon monoxide,
Hydrogen storage capacity deteriorates due to oxygen of more than p, p, or m.
本発明の構造体においては水素透過型電極は水素しか透
過しないのでこのような劣化は生じない。In the structure of the present invention, such deterioration does not occur because the hydrogen permeable electrode permeates only hydrogen.
以上述べたように本発明は水素と化学結合する金属材料
からなる水素貯蔵体の表面の一部に水素透過型電極を設
け、この水素透過型電極部を除く全表面を電気絶縁材料
でシールするか、または電気絶縁性容器で密封してなる
水素貯蔵用構造体であり、このものが電気分解装置にお
ける水素貯蔵部付きカソードとして使用でき、また水素
−酸素燃料電池の水素供与体として使用できるものであ
る。As described above, the present invention provides a hydrogen permeable electrode on a part of the surface of a hydrogen storage body made of a metal material that chemically bonds with hydrogen, and seals the entire surface except for this hydrogen permeable electrode part with an electrically insulating material. or a hydrogen storage structure sealed with an electrically insulating container, which can be used as a cathode with a hydrogen storage part in an electrolyzer or as a hydrogen donor in a hydrogen-oxygen fuel cell. It is.
第1図は電解液を電解して水素を貯蔵する従来方法の説
明図、第2図は従来例の方法における電極の説明図、第
3図は本発明の電極部を有する水素貯蔵用構造体の説明
図、第4図は本発明の構造体をとりつけた電解による水
素貯蔵法を示す説明図、第5図は従来法の燃料電池の作
用を示す説明図、第6図は本発明の構造体を燃料電池に
利用した場合の説明図である。
1・・・・・・対極、2・・・・・・水素透過型電極膜
、5・・・・・・電解液、6・・・・・・電解槽、7・
・・・・・電源、8・・・・・・水素吸蔵用(貯蔵用)
金属、9・・・・・・電気絶縁シール、9′・・・・・
・電気絶縁性密封容器、10・・・・・・コック、11
・・・・・・酸素極、12・・・・・・水素極、13・
・・・・・酸素導入部、14・・・・・・水素導入部、
15・・・・・・電力消費体、16・・・・・・水素貯
蔵用容器、A・・・・・・パラジウム−金−銀合金膜、
B・・・・・・パラジウムブラック(被覆層、C・・・
・・・白金ブラック被覆層。Fig. 1 is an explanatory diagram of a conventional method of electrolyzing an electrolyte to store hydrogen, Fig. 2 is an explanatory diagram of an electrode in the conventional method, and Fig. 3 is a hydrogen storage structure having an electrode part according to the present invention. FIG. 4 is an explanatory diagram showing a hydrogen storage method by electrolysis using the structure of the present invention, FIG. 5 is an explanatory diagram showing the operation of a conventional fuel cell, and FIG. 6 is an explanatory diagram showing the structure of the present invention. FIG. 2 is an explanatory diagram when the body is used in a fuel cell. DESCRIPTION OF SYMBOLS 1... Counter electrode, 2... Hydrogen permeable electrode membrane, 5... Electrolyte solution, 6... Electrolytic cell, 7.
...Power supply, 8...For hydrogen absorption (storage)
Metal, 9...Electrical insulation seal, 9'...
・Electrically insulating sealed container, 10... Cook, 11
...Oxygen electrode, 12...Hydrogen electrode, 13.
...Oxygen introduction part, 14...Hydrogen introduction part,
15... Power consumption body, 16... Hydrogen storage container, A... Palladium-gold-silver alloy membrane,
B... Palladium black (coating layer, C...
...Platinum black coating layer.
Claims (1)
透過型電極を除く該水素貯蔵体の全表面を電気絶縁性材
料でシールするか、または電気絶縁性容器で密封してな
る水素貯蔵用構造体において、上記水素貯蔵体は水素と
化学結合する金属材料からなり、上記水素透過型電極は
パラジウムまたはパラジウム合金よりなることを特徴と
する、電極部を有する水素貯蔵用構造体。 2 電気分解装置において水素貯蔵部付きカソードとし
て使用される特許請求の範囲第1項記載の水素貯蔵用構
造体。 3 水素−酸素燃料電池における水素供与体として使用
される特許請求の範囲第1項記載の水素貯蔵用構造体。[Scope of Claims] 1. A hydrogen permeable electrode is provided in a part of the hydrogen storage body, and the entire surface of the hydrogen storage body except for the hydrogen permeable electrode is sealed with an electrically insulating material, or an electrically insulating container is provided. A hydrogen storage structure having an electrode portion, wherein the hydrogen storage body is made of a metal material that chemically bonds with hydrogen, and the hydrogen permeable electrode is made of palladium or a palladium alloy. Storage structure. 2. The hydrogen storage structure according to claim 1, which is used as a cathode with a hydrogen storage section in an electrolyzer. 3. The hydrogen storage structure according to claim 1, which is used as a hydrogen donor in a hydrogen-oxygen fuel cell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53103514A JPS5846441B2 (en) | 1978-08-25 | 1978-08-25 | Hydrogen storage structure with electrode part |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53103514A JPS5846441B2 (en) | 1978-08-25 | 1978-08-25 | Hydrogen storage structure with electrode part |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5532729A JPS5532729A (en) | 1980-03-07 |
| JPS5846441B2 true JPS5846441B2 (en) | 1983-10-17 |
Family
ID=14356055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53103514A Expired JPS5846441B2 (en) | 1978-08-25 | 1978-08-25 | Hydrogen storage structure with electrode part |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5846441B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58163189A (en) * | 1982-03-23 | 1983-09-27 | Toshiba Corp | Metal oxide hydrogen cell |
| JPS6119063A (en) * | 1984-07-05 | 1986-01-27 | Sanyo Electric Co Ltd | Hydrogen occlusion electrode |
| DE3907084A1 (en) * | 1989-03-04 | 1990-09-13 | Battelle Institut E V | REVERSIBLE STORAGE FOR MEDIA AND USE OF THE STORAGE |
| JPH0990072A (en) * | 1995-09-26 | 1997-04-04 | Toichi Chikuma | Method and device for storing atomic hydrogen nucleus |
-
1978
- 1978-08-25 JP JP53103514A patent/JPS5846441B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5532729A (en) | 1980-03-07 |
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