JP3511608B1 - Steam electrolyzer - Google Patents
Steam electrolyzerInfo
- Publication number
- JP3511608B1 JP3511608B1 JP2003325438A JP2003325438A JP3511608B1 JP 3511608 B1 JP3511608 B1 JP 3511608B1 JP 2003325438 A JP2003325438 A JP 2003325438A JP 2003325438 A JP2003325438 A JP 2003325438A JP 3511608 B1 JP3511608 B1 JP 3511608B1
- Authority
- JP
- Japan
- Prior art keywords
- ion exchange
- exchange membrane
- steam
- water vapor
- compartment
- 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 - Fee Related
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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
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Fuel Cell (AREA)
Abstract
【要約】
【課題】水蒸気電解装置に関するものであって、気液分
離タンクや浄化手段や水蒸気冷却手段が不要で、無重力
下でも、水蒸気から、高純度の酸素と水素を、液体の水
と混じらないように取り出すことができる水蒸気電解装
置を提供すること。
【解決手段】圧力調整手段、温度調整手段、及び安全弁
を有する水蒸気発生器を付設し、かつ、(ア)前記水蒸
気発生器から水蒸気を導入する手段を有する隔室A、
(イ)フッ素樹脂系イオン交換膜、(ウ)水素排出手段
を有し、かつ、スポンジ状陰極を充填した隔室B、
(エ)白金、イリジウム、ロジウム又はイリジウム−ロ
ジウム合金をメッキしたフッ素樹脂系イオン交換膜、
(オ)多孔質チタンに白金メッキした陽極、(カ)酸素
排出手段を有する隔室Cを(ア)から(カ)の順にサン
ドイッチした電解槽を有する。Kind Code: A1 The present invention relates to a steam electrolysis apparatus, which does not require a gas-liquid separation tank, a purifying means, or a steam cooling means, and mixes high-purity oxygen and hydrogen from water vapor with liquid water even under zero gravity. To provide a steam electrolyzer that can be taken out without any trouble. A compartment A is provided with a steam generator having a pressure adjusting means, a temperature adjusting means, and a safety valve, and (A) means for introducing steam from the steam generator.
(A) a fluororesin-based ion exchange membrane, (c) a compartment B having hydrogen discharging means and filled with a sponge-shaped cathode,
(D) platinum, iridium, rhodium or iridium-rhodium alloy plated fluororesin-based ion exchange membrane,
(E) An electrolytic cell having an anode formed by plating platinum on porous titanium and (F) sandwiching the compartment C having an oxygen discharging means in the order of (A) to (F).
Description
【技術分野】【Technical field】
【0001】本発明は、重力の有無に関係なく、水蒸気
を電気分解して酸素と水素を取り出す水蒸気電解装置に
関する。より詳細には、航空機内で酸素を供給したり、
燃料電池にエネルギー源として酸素・水素を供給した
り、宇宙空間や宇宙船で生命を維持するための酸素や燃
料としての水素を供給したり、或いは宝飾加工の酸素バ
ーナーに酸素を供給したりすることに利用可能な水蒸気
電解装置に関するものである。The present invention relates to a steam electrolyzer for electrolyzing steam to extract oxygen and hydrogen regardless of the presence or absence of gravity. More specifically, you can supply oxygen onboard the aircraft,
Supplying oxygen and hydrogen as energy sources to fuel cells, supplying oxygen and hydrogen as fuel to maintain life in outer space and spacecraft, or supplying oxygen to jewelery processing oxygen burners In particular, it relates to a steam electrolyzer that can be used.
【0002】従来より、液体の水や電解質溶液を陰極及
び陽極に接触させて電解して、酸素又は水素を得る水の
電解装置が知られている(例えば、特許文献1参照)。2. Description of the Related Art Conventionally, there has been known a water electrolysis device for obtaining oxygen or hydrogen by bringing liquid water or an electrolyte solution into contact with a cathode and an anode to electrolyze it (see, for example, Patent Document 1).
【特許文献1】特開平9−67689号公報(図1)[Patent Document 1] Japanese Patent Laid-Open No. 9-67689 (FIG. 1)
【0003】また、搭載した水から、酸素と水素を8:
1の質量比で発生させる電解槽を備えた宇宙船が知られ
ている(例えば、特許文献2参照)。また、燃料電池と
組み合わせた閉鎖居住空間システムが知られている(例
えば、特許文献3参照)。In addition, oxygen and hydrogen are supplied from the loaded water to 8:
A spacecraft provided with an electrolytic cell that is generated at a mass ratio of 1 is known (for example, see Patent Document 2). Further, a closed living space system combined with a fuel cell is known (see, for example, Patent Document 3).
【特許文献2】特開平6−8893号公報(0006段
落)[Patent Document 2] Japanese Patent Laid-Open No. 6-8893 (paragraph 0006)
【特許文献3】特開平5−262300号公報(002
0段落)[Patent Document 3] Japanese Patent Application Laid-Open No. 5-262300 (002)
(0 paragraph)
【0004】本出願人らは、上記背景を鑑み、水電解装
置を開発した(例えば、特許文献4参照)。さらに、環
境浄化型水電解装置を開発した(例えば、特許文献5参
照)。In view of the above background, the present applicants have developed a water electrolysis device (see, for example, Patent Document 4). Furthermore, an environmental purification type water electrolysis device has been developed (for example, see Patent Document 5).
【特許文献4】特願2003−001862号[Patent Document 4] Japanese Patent Application No. 2003-001862
【特許文献5】特願2003−056632号[Patent Document 5] Japanese Patent Application No. 2003-056632
【0005】従来は、水蒸気を電解する際に、一度冷却
して液体の水にしてから水電解装置に導入するため、冷
却装置を必要とした。Conventionally, when electrolyzing steam, a cooling device is required because it is once cooled to form liquid water and then introduced into a water electrolysis device.
【0006】しかも、電極に電解液である液体の水を接
触させて電解すると、それぞれの電極から泡となって酸
素及び水素が発生するために気体と液体を分離するため
の気液分離タンクが必要であるという問題があった。特
に、無重力状態では液体の中にガスが泡となってとどま
り、分離することができないという問題があった。Further, when liquid water as an electrolytic solution is brought into contact with the electrodes for electrolysis, bubbles are generated from the respective electrodes to generate oxygen and hydrogen, so that a gas-liquid separation tank for separating gas and liquid is provided. There was a problem that it was necessary. In particular, in the zero-gravity state, there is a problem that gas remains as bubbles in the liquid and cannot be separated.
【0007】また、電解質となるイオン交換膜の電気抵
抗を常に低く保つためには、不純物のない高純度の水蒸
気を必要とするという問題があった。Further, there is a problem that high-purity water vapor without impurities is required in order to always keep the electric resistance of the ion-exchange membrane as an electrolyte low.
【0008】さらに、陽極で発生したH+イオンは水と
共に陰極に移動し、その水を回収して陽極に戻すため、
水循環回路が複雑になるという問題があった。Further, H + ions generated at the anode move to the cathode together with water, and the water is recovered and returned to the anode.
There was a problem that the water circulation circuit became complicated.
【0009】したがって、宇宙環境等の閉鎖空間におい
て、人間等の排出する空気に含まれる水蒸気を電解して
利用したい場合でも、混入する二酸化炭素やメタンを取
り除く浄化手段や、冷却して液体の水にする手段が必要
となるという問題があった。Therefore, in a closed space such as a space environment, even when it is desired to electrolyze and utilize steam contained in air discharged by humans or the like, a purifying means for removing carbon dioxide and methane mixed in, and liquid water cooled. There was a problem that a means to
【0010】本発明は、かかる問題を鑑みてなされたも
のであり、したがって、本発明の目的は、気液分離タン
クや浄化手段や水蒸気冷却手段が不要で、無重力下で
も、水蒸気から、高純度の酸素と水素を、液体の水と混
じらないように取り出すことができる水蒸気電解装置を
提供することにある。本発明者らは、上記の目的を達成
するために鋭意研究を重ねた結果、試行錯誤の上、本発
明を完成するに至った。The present invention has been made in view of the above problems. Therefore, the object of the present invention is to eliminate the need for a gas-liquid separation tank, a purifying means and a steam cooling means, and to obtain high purity from steam even under zero gravity. An object of the present invention is to provide a steam electrolyzer capable of taking out the oxygen and hydrogen of the above-mentioned without being mixed with liquid water. The present inventors have conducted intensive studies to achieve the above object, and as a result, completed the present invention through trial and error.
【0011】上記目的を達成するために、本発明の水蒸
気電解装置は、水蒸気を電解槽内へ導入する手段を有
し、水蒸気透過性を有する陰極をフッ素樹脂系のイオン
交換膜Aと触媒つきフッ素樹脂系のイオン交換膜Bの間
に挟みこみ、イオン交換膜Aの外側に水蒸気導入相を配
し、イオン交換膜Bの外側には陽極を配した電解槽で、
前記水蒸気導入相内に導入された水蒸気が、イオン交換
膜Aと前記陰極内を通過して、イオン交換膜Bに吸水さ
れ、両電極への電圧印加により、電解され、イオン交換
膜B内をプロトンが陽極側から陰極側に移動して、陰極
表面に水素が発生し、陽極表面に酸素が発生することに
より、発生した酸素と水素に水を混入させないものであ
る。In order to achieve the above object, the steam electrolysis apparatus of the present invention has means for introducing steam into the electrolytic cell, and a cathode having steam permeability is provided with a fluororesin ion exchange membrane A and a catalyst. It is sandwiched between fluororesin type ion exchange membranes B, a steam introduction phase is placed outside the ion exchange membrane A, and an anode is placed outside the ion exchange membrane B.
The water vapor introduced into the water vapor introduction phase passes through the ion exchange membrane A and the cathode, is absorbed by the ion exchange membrane B, is electrolyzed by applying a voltage to both electrodes, Protons move from the anode side to the cathode side, hydrogen is generated on the cathode surface, and oxygen is generated on the anode surface, so that the generated oxygen and hydrogen are not mixed with water.
【0012】本発明の水蒸気電解装置は、圧力調整手
段、温度調整手段、及び安全弁を有する水蒸気発生器を
付設し、かつ、(ア)前記水蒸気発生器から水蒸気を導
入する手段を有する隔室A、(イ)フッ素樹脂系イオン
交換膜、(ウ)水素排出手段を有し、かつ、スポンジ状
陰極を充填した隔室B、(エ)白金、イリジウム、ロジ
ウム又はイリジウム−ロジウム合金をメッキしたフッ素
樹脂系イオン交換膜、(オ)多孔質チタンに白金メッキ
した陽極、(カ)酸素排出手段を有する隔室Cを(ア)
から(カ)の順にサンドイッチした電解槽を有するもの
である。The steam electrolysis apparatus of the present invention is provided with a steam generator having a pressure adjusting means, a temperature adjusting means, and a safety valve, and (a) a compartment A having a means for introducing steam from the steam generator. , (A) Fluororesin-based ion exchange membrane, (c) compartment B having hydrogen discharge means and filled with a sponge-like cathode, (d) platinum, iridium, rhodium or fluorine plated with iridium-rhodium alloy A compartment C having a resin-based ion exchange membrane, (e) an anode formed by plating platinum on porous titanium, and (f) an oxygen exhausting means (a).
From (a) to (f), the electrolytic cell is sandwiched.
【0013】本発明の水蒸気電解装置は、気液分離タン
クや浄化手段や水蒸気冷却手段が不要で、無重力下で
も、水蒸気から、高純度の酸素と水素を、液体の水と混
じらないように取り出すことができる。また、宇宙環境
等の閉鎖空間において、人間等の排出する空気に含まれ
る水蒸気を容易に電解利用できる。The steam electrolyzer of the present invention does not require a gas-liquid separation tank, a purifying means or a steam cooling means, and takes out high-purity oxygen and hydrogen from the steam without mixing with liquid water even under zero gravity. be able to. Further, in a closed space such as a space environment, water vapor contained in air discharged by humans can be easily electrolyzed.
【0014】本発明によれば、酸素や水素が水の中に気
泡として発生しないので、気液分離タンクがいらない。
これは、コスト面のメリットのみならず、コンパクトで
軽量であるというメリットがある。また、本発明によれ
ば、無重力下において水蒸気を電気分解する場合におい
ても、水素排出口及び酸素排出口からは気体のみ取り出
すことができるので、取り出し時に気体に水が混入する
恐れがない。宇宙船においてはコンパクトであることが
非常に重要なポイントとなる。According to the present invention, since oxygen and hydrogen are not generated as bubbles in water, a gas-liquid separation tank is unnecessary.
This has not only the merit in terms of cost but also the merit of being compact and lightweight. Further, according to the present invention, even in the case of electrolyzing water vapor under zero gravity, only the gas can be taken out from the hydrogen outlet and the oxygen outlet, so that there is no fear that water is mixed into the gas at the time of taking out. Compactness is a very important point in spacecraft.
【発明を実施するための最良の形態】BEST MODE FOR CARRYING OUT THE INVENTION
【0015】本発明の特長は、水蒸気を電解槽内へ導入
する手段を有し、水蒸気透過性を有する陰極をフッ素樹
脂系のイオン交換膜Aと触媒つきフッ素樹脂系のイオン
交換膜Bの間に挟みこみ、イオン交換膜Aの外側に水蒸
気導入相を配し、イオン交換膜Bの外側には陽極を配し
た電解槽で、前記水蒸気導入相内に導入された水蒸気
が、イオン交換膜Aと前記陰極内を通過して、イオン交
換膜Bに吸水され、両電極への電圧印加により、電解さ
れ、イオン交換膜B内をプロトンが陽極側から陰極側に
移動して、陰極表面に水素が発生し、陽極表面に酸素が
発生することにより、発生した酸素と水素に水を混入さ
せないことである。The feature of the present invention is that it has a means for introducing water vapor into the electrolytic cell, and the water vapor permeable cathode is between the fluororesin ion exchange membrane A and the catalyst-containing fluororesin ion exchange membrane B. The water vapor introduced into the ion exchange membrane A is placed in an electrolytic cell having a water vapor introduction phase outside the ion exchange membrane A and an anode outside the ion exchange membrane B. Water is absorbed by the ion exchange membrane B after passing through the cathode, and electrolyzed by applying a voltage to both electrodes. Protons move in the ion exchange membrane B from the anode side to the cathode side, and hydrogen is deposited on the cathode surface. Is generated, and oxygen is generated on the surface of the anode, so that water is not mixed with the generated oxygen and hydrogen.
【0016】電解槽内は、室温であるため、水蒸気は、
導入された電解槽内で、一部液体の水になるが、水蒸気
導入相と電極がフッ素樹脂系イオン交換膜で仕切られて
いるため、電極に直接液体が接触することなく、水分が
イオン交換膜を水蒸気圧の高い方から低い電極側に水蒸
気として移動して電解される。Since the inside of the electrolytic cell is at room temperature, water vapor is
In the introduced electrolytic cell, part of the water becomes liquid, but since the water vapor introduction phase and the electrode are separated by the fluororesin ion exchange membrane, the liquid does not come into direct contact with the electrode and the water is ion-exchanged. The film moves from the side having a higher water vapor pressure to the electrode side having a lower water vapor pressure as water vapor for electrolysis.
【実施例1】[Example 1]
【0017】図1は、本発明の実施例1の構成図であ
る。図1に示した本発明の実施例1において、水蒸気電
解装置(1)は、水蒸気導入相である隔室A(3)、イ
オン交換膜A(4)、隔室B(8)、イオン交換膜B
(5)、陽極(9)、隔室C(11)の順にサンドイッ
チした電解槽(12)から構成される。気液分離タンク
は設けない。FIG. 1 is a block diagram of the first embodiment of the present invention. In Example 1 of the present invention shown in FIG. 1, the steam electrolysis apparatus (1) includes a compartment A (3), an ion exchange membrane A (4), a compartment B (8), an ion exchange which are phases for introducing steam. Membrane B
(5), the anode (9) and the compartment C (11) are sandwiched in this order from the electrolytic cell (12). No gas-liquid separation tank is provided.
【0018】隔室A(3)には、水蒸気流入口(2)が
設けてある。隔室B(8)には、水素排出口(6)が設
けてあり、かつ、スポンジ状の陰極(7)を充填してあ
る。隔室C(11)には、酸素排出口(10)が設けて
ある。隔室C(11)には、陽極(9)とイオン交換膜
B(5)の接触性向上のために、スポンジ状のNi−C
r合金が充填してある。The compartment A (3) is provided with a water vapor inlet (2). The compartment B (8) is provided with a hydrogen discharge port (6) and is filled with a sponge-like cathode (7). An oxygen outlet (10) is provided in the compartment C (11). In the compartment C (11), a sponge-like Ni-C is formed in order to improve the contact property between the anode (9) and the ion exchange membrane B (5).
r alloy is filled.
【0019】図1に示した本発明の実施例1において
は、陽極(9)には、多孔質チタンに白金をメッキした
電極を用いた。陰極(7)には、白金をメッキした、ス
ポンジ状の、ニッケル・クロム合金の多孔質電極を用い
た。In Example 1 of the present invention shown in FIG. 1, an electrode obtained by plating porous titanium with platinum was used as the anode (9). As the cathode (7), a sponge-like porous electrode of nickel-chromium alloy plated with platinum was used.
【0020】本発明の実施例1においては、イオン交換
膜A(4)として、フッ素樹脂系のイオン交換膜(例え
ば、デュポン社製のフッ素化ポリオレフィンのスルホン
化合物であるNAFION(R))を用いた。イオン交
換膜B(5)は、フッ素樹脂系のイオン交換膜に、触媒
の白金を4〜5mg/cm2担持させた。その有効膜面
積は、約200cm2である。本発明の実施例1におい
ては、フッ素樹脂系のイオン交換膜として、NAFIO
N(R) 117(デュポン社製)を用いた。イオン交
換膜にメッキする金属は、白金以外に、イリジウム、ロ
ジウム又はイリジウム−ロジウム合金が適する。In Example 1 of the present invention, as the ion exchange membrane A (4), a fluororesin type ion exchange membrane (for example, NAFION (R) which is a sulfone compound of fluorinated polyolefin manufactured by DuPont) is used. I was there. As the ion exchange membrane B (5), 4 to 5 mg / cm 2 of platinum as a catalyst was supported on a fluororesin-based ion exchange membrane. Its effective membrane area is about 200 cm 2 . In Example 1 of the present invention, NAFIO was used as the ion exchange membrane of fluororesin.
N (R) 117 (manufactured by DuPont) was used. In addition to platinum, iridium, rhodium, or an iridium-rhodium alloy is suitable as the metal to be plated on the ion exchange membrane.
【0021】本発明に実施例1においては、隔室A
(3)に供給された水蒸気は、飽和状態となっており、
温度調節をしていないため、一部、液体の水になるが、
イオン交換膜A(4)でブロックされる。本発明に用い
るイオン交換膜A(4)は液体を通過させず、水分のみ
通過させるものである。したがって、隔室A(3)にで
きた水や供給された水蒸気は、イオン交換膜A(4)を
飽和水蒸気として通過し、さらに、スポンジ状の陰極
(7)を通過して移動する。すなわち、イオン交換膜A
(4)が水蒸気のみを蒸気圧の高い方から低い方に移動
させる性質を利用し、気体のH2Oをイオン交換膜A
(4)を隔てた陰極側に供給して電気分解を起こさせて
水素と酸素を取り出す。In the first embodiment of the present invention, the compartment A
The water vapor supplied to (3) is saturated,
Because it does not control the temperature, it becomes liquid water,
It is blocked by the ion exchange membrane A (4). The ion exchange membrane A (4) used in the present invention does not allow liquid to pass therethrough but allows only water to pass through. Therefore, the water formed in the compartment A (3) and the supplied water vapor pass through the ion exchange membrane A (4) as saturated water vapor and further move through the sponge-like cathode (7). That is, the ion exchange membrane A
Utilizing the property that (4) moves only water vapor from the higher vapor pressure side to the lower vapor pressure side, the gaseous H 2 O is transferred to the ion exchange membrane A.
(4) is supplied to the separated cathode side to cause electrolysis to take out hydrogen and oxygen.
【0022】本発明の実施例1においては、水蒸気導入
相と電極がフッ素樹脂系イオン交換膜で仕切られ、電極
に直接液体が接触することがない。本発明の実施例1に
おいては、水分が、イオン交換膜を、水蒸気圧の高い方
から低い電極側に水蒸気として移動し、その水蒸気が触
媒を担持したもう一方のイオン交換膜に吸水され、両電
極への電圧の印加によって電解される。したがって、本
発明の実施例1においては、液体状態の水が、発生気体
である酸素や水素に混入することがない。In Example 1 of the present invention, the water vapor introduction phase and the electrode are partitioned by the fluororesin ion exchange membrane, and the liquid does not come into direct contact with the electrode. In Example 1 of the present invention, water migrates through the ion exchange membrane from the side having a higher water vapor pressure to the electrode side having a lower vapor pressure as water vapor, and the water vapor is absorbed by the other ion exchange membrane carrying the catalyst. It is electrolyzed by applying a voltage to the electrodes. Therefore, in the first embodiment of the present invention, liquid water is not mixed with oxygen or hydrogen that is the generated gas.
【0023】また、本発明の実施例1においては、水蒸
気を陽極側から供給せず、またイオン交換膜が液体の水
を透過するということがないので、陽極から水素イオン
と共に移動する液体の水の処理が不要である。また、気
体である水素・酸素と液体状態の水を分離させるための
装置も不要である。Further, in Example 1 of the present invention, since water vapor is not supplied from the anode side and the ion exchange membrane does not permeate liquid water, liquid water that moves together with hydrogen ions from the anode is used. Is unnecessary. Further, a device for separating hydrogen / oxygen as a gas and water in a liquid state is not necessary.
【0024】また、本発明の実施例1においては、水蒸
気をそのまま水蒸気導入相である隔室Aに導入して電解
できるので、水蒸気を冷却する手段も不要である。さら
に、水蒸気に二酸化炭素等のガスが混入していても水蒸
気の電解ができるので、浄化手段がいらない。Further, in Example 1 of the present invention, since steam can be introduced as it is into the compartment A, which is the steam introduction phase, for electrolysis, no means for cooling the steam is required. Further, even if a gas such as carbon dioxide is mixed in the steam, the steam can be electrolyzed, so that no purification means is required.
【0025】本発明は、実施例1で用いた陰極をスポン
ジ状でなく多孔質にしたり、イオン交換膜に水蒸気透過
性の高い他のイオン交換膜を用いる等による実施も可能
である。The present invention can also be carried out by making the cathode used in Example 1 porous instead of sponge, or using another ion exchange membrane having high water vapor permeability as the ion exchange membrane.
【実施例2】Example 2
【0026】図2は、本発明の実施例2の構成図であ
る。本発明の実施例2においては、水蒸気電解装置
(1)は、さらに、水蒸気発生装置(18)が付設され
ている。その他の点は本発明の実施例1と同じである。
水蒸気発生装置(18)には、圧力調整手段としての圧
力センサ(19)と圧力調節器(20)、温度調整手段
としての温度センサ(23)、及び安全弁(22)を有
する水タンク(16)からなる。また、モニター用とし
て圧力計(21)と水位計(24)を有する。水タンク
(16)内には水が一定量満たしてあり、水位センサ
(25)による制御で水位調節を行う。水はヒータ(1
3)で温度調整されている。ヒータ(13)は、圧力調
節器(20)とつながれていて、水蒸気圧が一定値にな
るように制御する。温度センサ(23)は水蒸気の温度
を測定する。水蒸気電解装置(1)と水蒸気発生装置
(18)は、水蒸気用パイプ(17)でつながれてい
る。水蒸気用パイプ(17)には、結露防止のためのヒ
ータが巻きつけてある。FIG. 2 is a block diagram of the second embodiment of the present invention. In Example 2 of the present invention, the steam electrolyzer (1) is further provided with a steam generator (18). Other points are the same as the first embodiment of the present invention.
A water tank (16) having a pressure sensor (19) and a pressure controller (20) as pressure adjusting means, a temperature sensor (23) as temperature adjusting means, and a safety valve (22) in the steam generator (18). Consists of. Further, it has a pressure gauge (21) and a water level gauge (24) for monitoring. The water tank (16) is filled with a certain amount of water, and the water level is adjusted by the control of the water level sensor (25). Water is heater (1
The temperature is adjusted in 3). The heater (13) is connected to the pressure regulator (20) and controls the water vapor pressure to a constant value. The temperature sensor (23) measures the temperature of water vapor. The steam electrolyzer (1) and the steam generator (18) are connected by a steam pipe (17). A heater for preventing dew condensation is wound around the steam pipe (17).
【0027】図3は、本発明の実施例3の構成図であ
る。本発明の実施例3の水蒸気電解装置(1)において
は、本発明の実施例2に、さらに、逆止弁(26)とバ
ルブ(27)を有するガス送入口(14)が設けてあ
り、任意のガスを水蒸気に混入できる。また、電解槽
(12)を複数個並列で並べてあり、高効率で酸素と水
素を発生させることができる。FIG. 3 is a block diagram of the third embodiment of the present invention. In the steam electrolysis apparatus (1) of Example 3 of the present invention, the gas inlet (14) having the check valve (26) and the valve (27) is further provided in Example 2 of the present invention, Any gas can be mixed with steam. Further, a plurality of electrolytic cells (12) are arranged in parallel, and oxygen and hydrogen can be generated with high efficiency.
【0028】本発明の実施例3においては、宇宙の閉鎖
空間において二酸化炭素やメタン等の混入した水蒸気を
電解した場合の模擬テストを行うことができる。In the third embodiment of the present invention, a simulated test can be conducted in the case where electrolysis of steam mixed with carbon dioxide, methane and the like is performed in a closed space of the universe.
【0029】本発明の水蒸気電解装置の利用は、航空機
内での酸素を供給したり、燃料電池にエネルギー源とし
て酸素・水素を供給したり、宇宙空間や宇宙船で生命を
維持するための酸素や燃料としての水素を供給したり、
或いは宝飾加工の酸素バーナーに酸素を供給したりする
ことに役立つ。したがって、本発明の水蒸気電解装置の
利用により、宇宙開発等の発展に寄与する。The steam electrolyzer of the present invention is used to supply oxygen in an aircraft, to supply oxygen / hydrogen as an energy source to a fuel cell, and to maintain life in outer space or spacecraft. Or supply hydrogen as fuel,
Alternatively, it is useful for supplying oxygen to a jewelry processing oxygen burner. Therefore, the use of the steam electrolyzer of the present invention contributes to the progress of space development and the like.
【0030】[0030]
【図1】本発明の実施例1の構成図である。FIG. 1 is a configuration diagram of a first embodiment of the present invention.
【図2】本発明の実施例2の構成図である。FIG. 2 is a configuration diagram of a second embodiment of the present invention.
【図3】本発明の実施例3の構成図である。FIG. 3 is a configuration diagram of a third embodiment of the present invention.
【0031】 1 水蒸気電解装置 2 水蒸気流入口 3 隔室A 4 イオン交換膜A 5 イオン交換膜B 6 水素排出口 7 陰極 8 隔室B 9 陽極 10 酸素排出口 11 隔室C 12 電解槽 13 ヒータ 14 ガス送入口 15 水排出口 16 水タンク 17 水蒸気用パイプ 18 水蒸気発生装置 19 圧力センサ 20 圧力調節器 21 圧力計 22 安全弁 23 温度センサ 24 水位計 25 水位センサ 26 逆止弁 27 バルブ[0031] 1 Steam electrolyzer 2 Steam inlet 3 compartment A 4 Ion exchange membrane A 5 Ion exchange membrane B 6 Hydrogen outlet 7 cathode 8 compartment B 9 Anode 10 oxygen outlet 11 compartment C 12 Electrolyzer 13 heater 14 gas inlet 15 Water outlet 16 water tank 17 Water vapor pipe 18 Steam generator 19 Pressure sensor 20 Pressure regulator 21 pressure gauge 22 Safety valve 23 Temperature sensor 24 Water gauge 25 Water level sensor 26 Check valve 27 valves
───────────────────────────────────────────────────── フロントページの続き (72)発明者 渡辺 洋二 東京都新宿区新宿5丁目4番14号 スガ 試験機株式会社内 (56)参考文献 実開 平4−21563(JP,U) 特許3452140(JP,B1) (58)調査した分野(Int.Cl.7,DB名) C25B 1/04 C25B 9/00 H01M 8/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoji Watanabe 5-4-14 Shinjuku, Shinjuku-ku, Tokyo Suga Test Machine Co., Ltd. (56) References: Kaihei 4-21563 (JP, U) Patent 3452140 ( JP, B1) (58) Fields investigated (Int.Cl. 7 , DB name) C25B 1/04 C25B 9/00 H01M 8/00
Claims (2)
膜Aと触媒つきフッ素樹脂系のイオン交換膜Bの間に挟
みこみ、イオン交換膜Aの外側に水蒸気導入相を配し、
イオン交換膜Bの外側には陽極を配した電解槽で、 前記水蒸気導入相内に導入された水蒸気が、イオン交換
膜Aと前記陰極内を通過して、イオン交換膜Bに吸水さ
れ、両電極への電圧印加により、電解され、 イオン交換膜B内をプロトンが陽極側から陰極側に移動
して、陰極表面に水素が発生し、 陽極表面に酸素が発生することにより、 発生した酸素と水素に水を混入させないことを特徴とす
る水蒸気電解装置。1. A means for introducing water vapor into an electrolytic cell, wherein a water vapor permeable cathode is sandwiched between a fluororesin-based ion exchange membrane A and a catalyst-containing fluororesin-based ion exchange membrane B, A water vapor introduction phase is arranged outside the ion exchange membrane A,
In an electrolytic cell having an anode arranged outside the ion exchange membrane B, the water vapor introduced into the water vapor introduction phase passes through the ion exchange membrane A and the cathode and is absorbed by the ion exchange membrane B. When a voltage is applied to the electrode, it is electrolyzed, protons move from the anode side to the cathode side in the ion exchange membrane B, hydrogen is generated on the cathode surface, and oxygen is generated on the anode surface. A steam electrolysis device characterized in that hydrogen is not mixed with water.
を有する水蒸気発生器を付設し、 かつ、 (ア)前記水蒸気発生器から水蒸気を導入する手段を有
する隔室A、 (イ)フッ素樹脂系イオン交換膜、 (ウ)水素排出手段を有し、かつ、スポンジ状陰極を充
填した隔室B、 (エ)白金、イリジウム、ロジウム又はイリジウム−ロ
ジウム合金をメッキしたフッ素樹脂系イオン交換膜、 (オ)多孔質チタンに白金メッキした陽極、 (カ)酸素排出手段を有する隔室C を(ア)から(カ)の順にサンドイッチした電解槽を有
することを特徴とする水蒸気電解装置。2. A compartment A provided with a steam generator having a pressure adjusting means, a temperature adjusting means, and a safety valve, and (a) having a means for introducing steam from the steam generator, and (b) a fluororesin. -Based ion exchange membrane, (c) compartment B having hydrogen discharging means and filled with a sponge-like cathode, (d) platinum, iridium, rhodium or iridium-rhodium alloy-plated fluororesin ion exchange membrane, (E) A steam electrolyzing device comprising an electrolytic cell in which an anode made by plating platinum on porous titanium and (f) a compartment C having an oxygen discharging means are sandwiched in the order of (a) to (f).
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