JP4327687B2 - High temperature steam electrolyzer - Google Patents

High temperature steam electrolyzer Download PDF

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JP4327687B2
JP4327687B2 JP2004269198A JP2004269198A JP4327687B2 JP 4327687 B2 JP4327687 B2 JP 4327687B2 JP 2004269198 A JP2004269198 A JP 2004269198A JP 2004269198 A JP2004269198 A JP 2004269198A JP 4327687 B2 JP4327687 B2 JP 4327687B2
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oxygen
electrode
hydrogen
chamber
steam electrolysis
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JP2006083428A (en
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健太郎 松永
信和 鈴木
正人 吉野
清 小野
斗 小川
斉二 藤原
重夫 笠井
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Toshiba Corp
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Description

本発明は、高温水蒸気電解セルをモジュール化する高温水蒸気電解装置に関する。  The present invention relates to a high temperature steam electrolysis apparatus that modularizes a high temperature steam electrolysis cell.

この種の高温水蒸気電解法は、高温の水蒸気を電気分解し水素ガスと酸素ガスを得る方法で、その作動温度域の関連で固体電解質燃料電池の逆反応による電解法が知られている(例えば、特許文献1参照)。   This type of high-temperature steam electrolysis method is a method of electrolyzing high-temperature steam to obtain hydrogen gas and oxygen gas, and an electrolysis method based on a reverse reaction of a solid electrolyte fuel cell is known in relation to its operating temperature range (for example, , See Patent Document 1).

特許文献1に開示されているように、水蒸気電解装置の主要構成部は、円筒型の電解セル並びに水蒸気供給室、生成水素排出室及び酸素生成室から構成される。  As disclosed in Patent Document 1, the main components of the water vapor electrolysis apparatus are composed of a cylindrical electrolysis cell, a water vapor supply chamber, a generated hydrogen discharge chamber, and an oxygen generation chamber.

円筒型の電解セルの片端に電流リード用金属キャップを取り付け、この他端をシールキャップにより完全な閉構造としている。このため、円筒型の電解セルへの燃料の供給・排出は、一方の端部からのみ行う。また、生成水素排出室及び酸素生成室を区切る管板とのシール部において円筒型の電解セルを支持する構造となっている。  A metal cap for current leads is attached to one end of a cylindrical electrolytic cell, and the other end has a completely closed structure by a seal cap. For this reason, the supply / discharge of fuel to / from the cylindrical electrolysis cell is performed only from one end. In addition, a cylindrical electrolysis cell is supported at a seal portion with a tube plate that separates the product hydrogen discharge chamber and the oxygen production chamber.

給電方法について説明する。水素極側リード部は、テーパ型シーリングを経由して取り出される。酸素極側リード部は、電解セルの下端のセルリード部がシールキャップに固定されて電解セルの内部に導入され、還元雰囲気を通って集電用金属キャップから取り出される。   A power feeding method will be described. The hydrogen electrode side lead portion is taken out via a taper type ceiling. The oxygen electrode side lead portion is introduced into the electrolysis cell with the cell lead portion at the lower end of the electrolysis cell fixed to the seal cap, and taken out from the collecting metal cap through the reducing atmosphere.

このように構成された水蒸気電解装置においては、水素側/酸素側のガスシール部はセル上下の2箇所となり、かつ、このガスシール部は、いずれの場合でもセルリード部を含んだシール構造となっているため、確実で信頼性のあるシールの実現は困難である。
特許第2930326号公報
In the steam electrolysis apparatus configured as described above, the gas seal portion on the hydrogen side / oxygen side has two locations above and below the cell, and the gas seal portion has a seal structure including the cell lead portion in any case. Therefore, it is difficult to realize a reliable and reliable seal.
Japanese Patent No. 2930326

上述した従来の高温水蒸気電解装置においては、水素と酸素とを隔てる部分のガスシールに関し、水素側及び酸素側のガスシール部がセル上下の2箇所となり、かつ、このガスシール部は、いずれの場合でもセルリード部が介在するシール構造となっているため、確実で信頼性のあるシールの実現が困難であった。  In the conventional high-temperature steam electrolysis apparatus described above, the hydrogen-side and oxygen-side gas seal portions are located at two locations above and below the cell, and the gas seal portion is any of the gas seal portions that separate hydrogen and oxygen. Even in this case, since the cell lead portion is interposed, it is difficult to realize a reliable and reliable seal.

また、約900℃の作動温度および酸化/還元雰囲気という動作条件下で電解を行う円筒型の電解セルに均一に電解電流を供給する構造に関する課題、つまり、水素極及び酸素極のセルリード部の取り出しが近接するため、大電流供給を必要とする高効率な高温水蒸気電解装置を構成する場合、発熱による断線等、故障の要因となる、という解決すべき課題があった。  Also, a problem related to a structure for supplying an electrolytic current uniformly to a cylindrical electrolytic cell that performs electrolysis under an operating temperature of about 900 ° C. and an oxidizing / reducing atmosphere, that is, taking out cell lead portions of a hydrogen electrode and an oxygen electrode Therefore, when configuring a high-efficiency high-temperature steam electrolyzer that requires a large current supply, there has been a problem to be solved, such as disconnection due to heat generation, causing failure.

さらに、約900℃の作動温度および酸化/還元雰囲気という動作条件下で電解を行う円筒型の電解セル及び装置を構成する材料間の熱膨張率差を如何に吸収するかが、大きな課題である。  Furthermore, how to absorb the difference in coefficient of thermal expansion between the materials constituting the cylindrical electrolytic cell and apparatus that performs electrolysis under an operating temperature of about 900 ° C. and an oxidizing / reducing atmosphere is a major issue. .

本発明は上記課題を解決するためになされたもので、高温動作時の水素側及び酸素側のガスシール部を確実かつ信頼性の高い構造とし、さらに電解セルの電極に均一に電解電流を供給できる高温水蒸気電解装置を提供することを目的とする。   The present invention has been made to solve the above-described problems. The gas seals on the hydrogen side and oxygen side during high-temperature operation have a reliable and reliable structure, and the electrolytic current is uniformly supplied to the electrodes of the electrolysis cell. An object of the present invention is to provide a high-temperature steam electrolysis apparatus that can be used.

上記目的を達成するため、本発明の高温水蒸気電解装置においては、内側に水素極を有し外側に酸素極を有し少なくとも1個配設されて下端を閉じた筒状の水蒸気電解セルと、この水蒸気電解セルの上方に設けられ水蒸気が供給される水蒸気供給室と、この水蒸気供給室より垂下され前記水蒸気電解セルの内側に水蒸気を供給する水蒸気注入管と、前記水蒸気供給室の下部に設けられ前記水素極で生成した水素を系外に取り出す生成水素排出室と、この生成水素排出室の下部に設けられ前記酸素極の雰囲気を調整し生成した酸素を取り出す酸素生成室と、前記水蒸気電解セルの内側に配設され前記水素極に電解電流を供給する水素極弾性給電手段と、前記酸素生成室の内部に設けられ前記酸素極に電解電流を供給する酸素極弾性給電手段とを有し、前記水蒸気供給室と前記酸素生成室との間に絶縁層を介在させ、前記水蒸気供給室から前記水素極に電解電流を供給し、さらに前記酸素生成室の外壁から前記酸素極に電解電流を供給することを特徴とする。 In order to achieve the above object, in the high-temperature steam electrolysis apparatus of the present invention, a cylindrical steam electrolysis cell having a hydrogen electrode on the inside and an oxygen electrode on the outside and having at least one disposed closed bottom, A steam supply chamber provided above the steam electrolysis cell and supplied with steam, a steam injection pipe suspended from the steam supply chamber and supplying steam to the inside of the steam electrolysis cell, and provided below the steam supply chamber A generated hydrogen discharge chamber for extracting hydrogen generated at the hydrogen electrode out of the system, an oxygen generation chamber provided at a lower portion of the generated hydrogen discharge chamber for extracting oxygen generated by adjusting the atmosphere of the oxygen electrode, and the steam electrolysis a hydrogen electrode resilient power supply means for supplying an electrolytic current to the hydrogen electrode is disposed inside the cell, the oxygen electrode resilient power supply means for supplying an electrolytic current to the oxygen electrode provided inside the oxygen generating chamber An insulating layer is interposed between the water vapor supply chamber and the oxygen generation chamber, an electrolysis current is supplied from the water vapor supply chamber to the hydrogen electrode, and an electrolysis current is supplied from the outer wall of the oxygen generation chamber to the oxygen electrode. It is characterized by supplying .

また、上記目的を達成するため、本発明の高温水蒸気電解装置においては、内側に酸素極を有し外側に水素極を有し少なくとも1個配設されて下端を閉じた筒状の水蒸気電解セルと、この水蒸気電解セルの上方に設けられ空気を含む酸素極雰囲気が供給される酸素極雰囲気供給室と、この酸素極雰囲気供給室より垂下され前記水蒸気電解セルの内側に前記酸素極雰囲気を供給する酸素極雰囲気注入管と、前記酸素極雰囲気供給室の下部に設けられ前記酸素極雰囲気を調整し生成した酸素を系外に取り出す生成酸素排出室と、この生成酸素排出室の下部に設けられ水蒸気が供給されて、この水蒸気から前記水素極における電極反応によって水素を生成させ、この水素極で生成した水素を取り出す水素生成室と、前記水蒸気電解セルの内側に配設され前記酸素極に電解電流を供給する酸素極弾性給電手段と、前記水素生成室の内部に設けられ前記水素に電解電流を供給する水素極弾性給電手段とを有し、前記酸素雰囲気供給室と前記水素生成室との間に絶縁層を介在させ、前記酸素雰囲気供給室から前記酸素極に電解電流を供給し、さらに前記水素生成室の外壁から前記水素極に電解電流を供給すること、を特徴とするを特徴とする。 In order to achieve the above object, in the high-temperature steam electrolysis apparatus of the present invention, a cylindrical steam electrolysis cell having an oxygen electrode on the inside and at least one hydrogen electrode on the outside and having a closed lower end When the oxygen electrode atmosphere supply chamber oxygen electrode atmosphere containing air disposed above the steam electrolysis cell is supplied, the oxygen electrode atmosphere is suspended from the oxygen electrode atmosphere supply chamber inside the steam electrolysis cell fed An oxygen electrode atmosphere injection tube, a generated oxygen discharge chamber provided at a lower portion of the oxygen electrode atmosphere supply chamber, for adjusting the oxygen electrode atmosphere and taking out generated oxygen out of the system, and a lower portion of the generated oxygen discharge chamber. steam is supplied, to generate hydrogen by the electrode reaction in the hydrogen electrode from the water vapor, and hydrogen generating chamber to take out the hydrogen produced in the hydrogen electrode, disposed inside of the steam electrolysis cell Are the a and the oxygen electrode resilient power supply means for supplying the oxygen electrode to the electrolytic current, and a hydrogen electrode resilient power supply means for supplying an electrolytic current to the hydrogen electrode provided inside the hydrogen generator chamber, said oxygen electrode atmosphere supply An insulating layer is interposed between the oxygen generation chamber and the hydrogen generation chamber, an electrolysis current is supplied from the oxygen electrode atmosphere supply chamber to the oxygen electrode, and an electrolysis current is supplied from the outer wall of the hydrogen generation chamber to the hydrogen electrode. It is characterized by that.

本発明によれば、水素及び酸素のガスリークを防止すると共に、水蒸気電解セルの電極に均一に電解電流を供給し、さらに、水蒸気電解セル及び装置を構成する材料間の熱膨張率差を吸収することにより、ガスシールの信頼性が高く、強固な構造を持ち更に大電力供給を可能とする高温水蒸気電解装置を提供することができる。   According to the present invention, gas leakage of hydrogen and oxygen is prevented, an electrolysis current is uniformly supplied to the electrodes of the steam electrolysis cell, and further, the thermal expansion coefficient difference between the materials constituting the steam electrolysis cell and the apparatus is absorbed. As a result, it is possible to provide a high temperature steam electrolysis apparatus that has a highly reliable gas seal, has a strong structure, and can supply a large amount of power.

以下、本発明に係る高温水蒸気電解装置の実施の形態について、図1乃至図6を参照して説明する。ここで、同一又は類似の部分には共通の符号を付すことにより、重複説明を省略する。   Hereinafter, an embodiment of a high-temperature steam electrolysis apparatus according to the present invention will be described with reference to FIGS. 1 to 6. Here, the same or similar parts are denoted by common reference numerals, and redundant description is omitted.

まず、本発明の第1の実施の形態について説明する。   First, a first embodiment of the present invention will be described.

図1は、本発明による第1の実施の形態の高温水蒸気電解装置の構成を示す概略縦断面図である。   FIG. 1 is a schematic longitudinal sectional view showing a configuration of a high temperature steam electrolyzer according to a first embodiment of the present invention.

図1に示すように、高温水蒸気電解装置には、単数又は複数の筒状水蒸気電解セル1,1aが配設されている。ここでは、一例として、円筒型水蒸気電解セル1(以下「円筒セル」という。)について説明する。   As shown in FIG. 1, the high temperature steam electrolysis apparatus is provided with one or a plurality of cylindrical steam electrolysis cells 1 and 1a. Here, as an example, a cylindrical steam electrolysis cell 1 (hereinafter referred to as “cylindrical cell”) will be described.

円筒セル1,1aは、下端を閉じ、内側に水素極21、外側に酸素極31を有する。   The cylindrical cells 1 and 1a are closed at the lower end, and have a hydrogen electrode 21 on the inside and an oxygen electrode 31 on the outside.

高温水蒸気電解装置の上部には、水蒸気供給室2が構築されている。この水蒸気供給室2には、水蒸気41が供給され、この水蒸気41は、水蒸気注入管3を経由して円筒セル1の水素極21に供給される。   A steam supply chamber 2 is constructed in the upper part of the high-temperature steam electrolysis apparatus. The water vapor supply chamber 2 is supplied with water vapor 41, and the water vapor 41 is supplied to the hydrogen electrode 21 of the cylindrical cell 1 through the water vapor injection pipe 3.

直流電源45により、水素極21に負側、酸素極31に正側の電圧をかける。すると、水蒸気の電気分解によって、水素極21に水素、酸素極31に酸素が発生する。   A DC power supply 45 applies a negative voltage to the hydrogen electrode 21 and a positive voltage to the oxygen electrode 31. Then, hydrogen is generated at the hydrogen electrode 21 and oxygen is generated at the oxygen electrode 31 by electrolysis of water vapor.

円筒セル1、1aの水素極21において電極反応によりで生成した水素42は、水蒸気供給室2の下部に構成された生成水素排出室4に排出され、最終的に系外に取り出される。   The hydrogen 42 generated by the electrode reaction in the hydrogen electrode 21 of the cylindrical cell 1, 1 a is discharged to the generated hydrogen discharge chamber 4 formed at the lower part of the water vapor supply chamber 2 and finally taken out of the system.

この生成水素排出室4の下部には、酸素生成室5が構成され、空気等の酸素極雰囲気43が供給される。この酸素極雰囲気43は、円筒セル1の外側の酸素極31側の雰囲気を調整し、さらに、円筒セル1,1aの酸素極31において電極反応により生成した酸素44は系外に取り出される。   An oxygen generation chamber 5 is configured below the generated hydrogen discharge chamber 4, and an oxygen electrode atmosphere 43 such as air is supplied. The oxygen electrode atmosphere 43 adjusts the atmosphere on the oxygen electrode 31 side outside the cylindrical cell 1, and oxygen 44 generated by the electrode reaction in the oxygen electrode 31 of the cylindrical cells 1 and 1a is taken out of the system.

この円筒セル1は、全体を均一に形成したもので、図2に詳細を示す。内側は、水素極21からなる内壁より形成され、負極となる。この水素極21からなる内壁の外周面に、固体電解質型の電解質35からなる電解質層が形成される。   The cylindrical cell 1 is formed uniformly throughout, and details are shown in FIG. The inner side is formed from an inner wall made of the hydrogen electrode 21 and serves as a negative electrode. An electrolyte layer made of a solid electrolyte type electrolyte 35 is formed on the outer peripheral surface of the inner wall made of the hydrogen electrode 21.

この電解質35からなる電解質層の外周面に、酸素極31からなる正極が更に形成される。この酸素極31からなる酸素極層の外周面に、集電体23として機能するメッシュが外壁として形成される。すなわち、円筒セル1の外側にある酸素極31の表面に、金又は白金から形成されるメッシュを巻き付けることにより集電体23を形成し、酸素極31の電極面全体に電解電流を均一に供給することができる。ここで、このメッシュの代わりに、金又は白金の線をらせん状に巻き付けた構造やフェルト状の構造、あるいは多孔質状の導電性酸化物等の導電性でかつ弾性の部材を使用して集電体23を形成してもよい。   A positive electrode made of the oxygen electrode 31 is further formed on the outer peripheral surface of the electrolyte layer made of the electrolyte 35. A mesh functioning as a current collector 23 is formed as an outer wall on the outer peripheral surface of the oxygen electrode layer formed of the oxygen electrode 31. That is, the current collector 23 is formed by winding a mesh formed of gold or platinum around the surface of the oxygen electrode 31 outside the cylindrical cell 1, and the electrolytic current is uniformly supplied to the entire electrode surface of the oxygen electrode 31. can do. Here, instead of the mesh, a conductive and elastic member such as a structure in which a gold or platinum wire is spirally wound, a felt-like structure, or a porous conductive oxide is used. The electric body 23 may be formed.

このように、円筒型水蒸気電解セル1は、内側から水素極21、電解質35、酸素極31、集電体23から成る層が密着性良く形成されている。   As described above, the cylindrical steam electrolysis cell 1 has a layer composed of the hydrogen electrode 21, the electrolyte 35, the oxygen electrode 31, and the current collector 23 formed from the inside with good adhesion.

他の構成の円筒セル1aについて、図3に示す。図3は、図2の構成の変形例で、主に、図2と相違する構成について説明する。円筒セル1aは、図2に示す円筒セル1と同等の熱膨張率を有する支持管6を円筒セル1の上部に予め接合して形成したものである。支持管6を使用するときは、支持管6の内側と外側とは絶縁しておく必要がある。また、円筒セル1の外側の酸素極31と酸素生成室5の壁面とは、支持管6の外側表面に導電性を持たせるか又は別途設けるリード線等で両者を接続することにより、導通を保つことが必要である。   FIG. 3 shows a cylindrical cell 1a having another configuration. FIG. 3 is a modification of the configuration of FIG. 2 and mainly describes a configuration different from FIG. The cylindrical cell 1a is formed by previously joining a support tube 6 having a thermal expansion coefficient equivalent to that of the cylindrical cell 1 shown in FIG. When the support tube 6 is used, it is necessary to insulate the inside and the outside of the support tube 6. Further, the oxygen electrode 31 outside the cylindrical cell 1 and the wall surface of the oxygen generation chamber 5 are made conductive by giving conductivity to the outer surface of the support tube 6 or connecting them with a lead wire or the like separately provided. It is necessary to keep.

酸素生成室5の中には、ガイド板7が設けられている。このガイド板7は、導電性材料で形成され、酸素生成室5の壁から円筒セル1、1aの周辺まで伸びている。このガイド板7を設置しても、ガイド板7により形成された上下の部屋は開放されている。   A guide plate 7 is provided in the oxygen generation chamber 5. The guide plate 7 is made of a conductive material and extends from the wall of the oxygen generation chamber 5 to the periphery of the cylindrical cells 1 and 1a. Even when the guide plate 7 is installed, the upper and lower rooms formed by the guide plate 7 are open.

円筒セル1、1aは、一例として図1に示すように、ニッケル、金及び白金から選択された1種または2種以上の合金から形成されバネ状に加工した弾性給電端子32を介して側面から固定される。   As shown in FIG. 1 as an example, the cylindrical cells 1 and 1a are formed from one or more alloys selected from nickel, gold and platinum, and are formed from a side surface through an elastic power supply terminal 32 processed into a spring shape. Fixed.

また、円筒セル1の内側には、例えば、ニッケル、金及び白金から選択された1種又は2種以上の合金から形成されバネ状に加工した弾性給電端子22が配設される。この弾性給電端子22により、円筒セル1、1a内の水素極21と水蒸気注入管3とを接触させる。このバネ状の弾性給電端子22は、円筒セル1内側の水蒸気41の流れ又は温度変化に伴う円筒セル1と水蒸気供給管3との相対的な位置変化を妨げないよう、円筒セル1の中心から放射状に隙間を設けてもよい。また、このバネ状の弾性給電端子22の代わりに、メッシュやフェルト状の構造を持つ給電端子を使用してもよい。   Further, inside the cylindrical cell 1, for example, an elastic power supply terminal 22 formed of one or more alloys selected from nickel, gold, and platinum and processed into a spring shape is disposed. With this elastic power supply terminal 22, the hydrogen electrode 21 in the cylindrical cells 1, 1 a and the water vapor injection pipe 3 are brought into contact with each other. This spring-like elastic power supply terminal 22 is arranged from the center of the cylindrical cell 1 so as not to prevent a relative position change between the cylindrical cell 1 and the water vapor supply pipe 3 due to the flow of steam 41 inside the cylindrical cell 1 or a temperature change. You may provide a clearance radially. Further, instead of the spring-shaped elastic power supply terminal 22, a power supply terminal having a mesh or felt structure may be used.

本実施形態において、水蒸気導入管3及びガイド板7を導電性材料で形成しているので、この水蒸気導入管3及びガイド板7は、円筒セル1の内側にある水素極21及び円筒セル1の外側にある酸素極31に電解電流を供給するための電流リード端子として使用することができる。このとき、水蒸気供給室2と酸素生成室5との間に絶縁層8を介在させることにより、水素極21と酸素極31との短絡を防止する必要がある。   In the present embodiment, since the water vapor introducing tube 3 and the guide plate 7 are formed of a conductive material, the water vapor introducing tube 3 and the guide plate 7 are formed of the hydrogen electrode 21 and the cylindrical cell 1 inside the cylindrical cell 1. It can be used as a current lead terminal for supplying an electrolytic current to the oxygen electrode 31 on the outside. At this time, it is necessary to prevent a short circuit between the hydrogen electrode 21 and the oxygen electrode 31 by interposing the insulating layer 8 between the water vapor supply chamber 2 and the oxygen generation chamber 5.

また、水蒸気供給室2と水蒸気注入管3とを接続し、酸素生成室5とガイド板7とを電気的に接続することにより、水蒸気供給室2の容器外壁から円筒セル1の水素極21に電解電流を供給することができる。また、酸素生成室5の外壁から円筒セルの酸素極31に電解電流を供給することができる。   In addition, the steam supply chamber 2 and the steam injection pipe 3 are connected, and the oxygen generation chamber 5 and the guide plate 7 are electrically connected, so that the outer wall of the steam supply chamber 2 is connected to the hydrogen electrode 21 of the cylindrical cell 1. An electrolytic current can be supplied. In addition, an electrolytic current can be supplied from the outer wall of the oxygen generation chamber 5 to the oxygen electrode 31 of the cylindrical cell.

また、円筒セル1、1aの閉端部先端と酸素生成室5の内壁との間に、例えば、フェルト状の白金から形成される弾性給電端子52を設置し、電気的接触を確保すると共に、円筒セル1、1aの固定を先端及び根元の2点で行うことにより、さらに構造的安定性を向上させることができる。   Further, between the closed end of the cylindrical cells 1 and 1a and the inner wall of the oxygen generation chamber 5, for example, an elastic power supply terminal 52 formed of felt-like platinum is installed to ensure electrical contact, The structural stability can be further improved by fixing the cylindrical cells 1 and 1a at the two points of the tip and the base.

また、円筒セル1、1aの開放部は、生成水素排出室4の壁面にガラス及びセラミックス複合材等から形成されるシール材9を介して固定される。このシール材9に接する円筒セル1の接続部10及び生成水素排出室4のセル接続部11には、予め円環状又はらせん状の刻み目を設けることにより、ガスリークを効果的に防止すると共に円筒セル1、1aを生成水素排出室4の壁面により強固に固定することが可能である。   The open portions of the cylindrical cells 1, 1 a are fixed to the wall surface of the generated hydrogen discharge chamber 4 via a seal material 9 formed of glass and a ceramic composite material. The connecting portion 10 of the cylindrical cell 1 in contact with the sealing material 9 and the cell connecting portion 11 of the generated hydrogen discharge chamber 4 are provided with an annular or spiral notch in advance, thereby effectively preventing gas leakage and the cylindrical cell. 1, 1a can be firmly fixed to the wall surface of the product hydrogen discharge chamber 4.

本実施形態によれば、水素及び酸素のガスリークを防止すると共に、円筒セル1の電極に均一に電解電流を供給し、さらに、円筒セル1及び装置を構成する材料間の熱膨張率差を吸収することにより、ガスシールの信頼性が高く、強固な構造を持ち更に大電力供給を可能とする高温水蒸気電解装置を製造することができる。   According to this embodiment, hydrogen and oxygen gas leaks are prevented, an electrolytic current is supplied uniformly to the electrodes of the cylindrical cell 1, and further, the thermal expansion coefficient difference between the cylindrical cell 1 and the material constituting the apparatus is absorbed. By doing so, it is possible to manufacture a high-temperature steam electrolysis apparatus that has a highly reliable gas seal, has a strong structure, and can supply a large amount of power.

なお、図1では、一つの高温水蒸気電解装置に2種類の円筒セル1及び1aを並列に配置した例を示すが、円筒セル1または1aの一方のみを1個だけ又は複数個配置してもよい。   Although FIG. 1 shows an example in which two types of cylindrical cells 1 and 1a are arranged in parallel in one high-temperature steam electrolysis apparatus, only one or a plurality of cylindrical cells 1 or 1a may be arranged. Good.

次に、本発明の第2の実施の形態について説明する。   Next, a second embodiment of the present invention will be described.

図4は、本発明による第2の実施の形態の高温水蒸気電解装置の構成を示す概略縦断面図である。   FIG. 4 is a schematic longitudinal sectional view showing the configuration of the high-temperature steam electrolyzer according to the second embodiment of the present invention.

図4に示すように、高温水蒸気電解装置には、単数又は複数の円筒セル51、51aが配設されている。この円筒セル51、51aは、一端を閉じ、内側に酸素極31、外側に水素極21を有する。   As shown in FIG. 4, the high temperature steam electrolysis apparatus is provided with one or a plurality of cylindrical cells 51, 51a. The cylindrical cells 51 and 51a are closed at one end, and have an oxygen electrode 31 on the inner side and a hydrogen electrode 21 on the outer side.

すなわち、この円筒セル51、51aは、図1記載の円筒セル1、1aと比較して、酸素極31、水素極21が、内側と外側とが逆に配設されている。   That is, in the cylindrical cells 51 and 51a, the oxygen electrode 31 and the hydrogen electrode 21 are arranged oppositely on the inner side and the outer side as compared with the cylindrical cells 1 and 1a shown in FIG.

高温水蒸気電解装置の上部には、酸素極雰囲気供給室12が構築されている。この酸素極雰囲気供給室12には、円筒セル51、51aの内側の酸素極31側の雰囲気を調整するために、空気等の酸素極雰囲気43が供給される。   In the upper part of the high-temperature steam electrolysis apparatus, an oxygen electrode atmosphere supply chamber 12 is constructed. The oxygen electrode atmosphere supply chamber 12 is supplied with an oxygen electrode atmosphere 43 such as air in order to adjust the atmosphere on the oxygen electrode 31 side inside the cylindrical cells 51 and 51a.

この酸素極雰囲気供給室12に供給された空気等の酸素極雰囲気43は、酸素極雰囲気管13を経由して円筒セル51、51aの内側の酸素極31に供給される。   The oxygen electrode atmosphere 43 such as air supplied to the oxygen electrode atmosphere supply chamber 12 is supplied to the oxygen electrode 31 inside the cylindrical cells 51, 51 a via the oxygen electrode atmosphere tube 13.

この酸素極雰囲気供給室12の下部には、生成酸素排出室14が構築される。円筒セル51、51aの酸素極31において電極反応により生成した酸素44は、生成酸素排出室14に排出され、最終的に系外に取り出される。   A generated oxygen discharge chamber 14 is constructed below the oxygen electrode atmosphere supply chamber 12. Oxygen 44 generated by the electrode reaction in the oxygen electrode 31 of the cylindrical cells 51 and 51a is discharged to the generated oxygen discharge chamber 14 and finally taken out of the system.

生成酸素排出室14の下部には、水素生成室15が配設されている。この水素生成室15には、水蒸気41が供給される。この供給された水蒸気41は、円筒セル51、51a外側の水素極21において電極反応する。この電極反応により生成した水素42は、水素生成室15に排出され、最終的に生成水素42の取出口より回収される。   A hydrogen generation chamber 15 is disposed below the generated oxygen discharge chamber 14. Steam 41 is supplied to the hydrogen generation chamber 15. The supplied water vapor 41 undergoes an electrode reaction at the hydrogen electrode 21 outside the cylindrical cells 51 and 51a. Hydrogen 42 generated by this electrode reaction is discharged into the hydrogen generation chamber 15 and finally recovered from the outlet of the generated hydrogen 42.

この円筒セル51は、全体を均一に形成したもので、図5に詳細を示す。内側は、酸素極31からなる内壁より形成され、正極を示す。この酸素極31からなる内壁の外周面に、固体電解質型の電解質35からなる電解質層が形成される。   The cylindrical cell 51 is formed uniformly throughout, and details are shown in FIG. The inner side is formed from the inner wall made of the oxygen electrode 31 and represents the positive electrode. An electrolyte layer made of a solid electrolyte type electrolyte 35 is formed on the outer peripheral surface of the inner wall made of the oxygen electrode 31.

この電解質35からなる電解質層の外周面に、水素極21からなる負極が更に形成される。この水素極21からなる水素極層の外周面に、集電体23として機能するメッシュが外壁として形成される。この集電体23は、円筒セル51の外側の水素極21の表面に、ニッケル、金及び白金から選択された1種または2種以上の合金から形成されるメッシュを巻き付けることにより形成され、水素極21の電極面全体に電解電流を均一に供給することができる。ここで、メッシュの代わりに、金又は白金製の線をらせん状に巻きつけた構造やフェルト状の構造又は多孔質状の導電性酸化物を使用して集電体23を形成することができる。   On the outer peripheral surface of the electrolyte layer made of the electrolyte 35, a negative electrode made of the hydrogen electrode 21 is further formed. A mesh functioning as a current collector 23 is formed as an outer wall on the outer peripheral surface of the hydrogen electrode layer composed of the hydrogen electrode 21. The current collector 23 is formed by winding a mesh formed of one or more alloys selected from nickel, gold and platinum around the surface of the hydrogen electrode 21 outside the cylindrical cell 51, The electrolytic current can be uniformly supplied to the entire electrode surface of the electrode 21. Here, the current collector 23 can be formed using a structure in which a wire made of gold or platinum is spirally wound, a felt-like structure, or a porous conductive oxide instead of a mesh. .

このように、円筒セル51は、内側から酸素極31、電解質35、水素極21、集電体23から成る層が密着性良く形成されている。   Thus, the cylindrical cell 51 has a layer composed of the oxygen electrode 31, the electrolyte 35, the hydrogen electrode 21, and the current collector 23 formed from the inside with good adhesion.

他の構成の円筒セル51aについて、図6に示す。図6は、図5の構成に追加するものであり、主に、図5と相違する構成について説明する。円筒セル51aは、図5に示す円筒セル51と同等の熱膨張率を有する支持管6を円筒セル51の上部に予め接合して形成したものである。支持管6を使用するときは、支持管6の内側と外側とは絶縁しておく必要がある。また、円筒セル51aの外側の水素極21と水素生成室15の壁面とは、支持管6の外側表面に導電性を持たせるか、又は別途設けるリード線等で両者を接続することにより、導通を保つことが必要である。   FIG. 6 shows a cylindrical cell 51a having another configuration. FIG. 6 is added to the configuration of FIG. 5 and mainly describes a configuration different from FIG. The cylindrical cell 51a is formed by previously joining a support tube 6 having a thermal expansion coefficient equivalent to that of the cylindrical cell 51 shown in FIG. When the support tube 6 is used, it is necessary to insulate the inside and the outside of the support tube 6. In addition, the hydrogen electrode 21 outside the cylindrical cell 51a and the wall surface of the hydrogen generation chamber 15 are made conductive by giving conductivity to the outer surface of the support tube 6 or by connecting them with a separately provided lead wire or the like. It is necessary to keep

水素生成室15の中にはガイド板7が設けられている。このガイド板7と円筒セル51aの側面とは、例えば、ニッケル、金及び白金から選択された1種又は2種以上の合金から形成されバネ状に加工した弾性給電端子32aを介して固定される。 円筒セル51、51aの内側には、例えば、ニッケル、金及び白金から選択された1種又は2種以上の合金から形成されバネ状に加工した弾性給電端子22aを設け、円筒セル51の酸素極31と酸素極雰囲気注入管13とを接触させる。このバネ状弾性給電端子22aは、円筒セル51、51aの内側の水蒸気ガスの流れや温度変化に伴う円筒セル51、51aと酸素極雰囲気注入管13との相対的な位置変化を妨げないよう、円筒セル51、51aの中心から放射状に隙間を設けてもよい。また、これらのバネ状弾性給電端子22aの代わりに、メッシュやフェルト状の構造を持つ給電端子を使用してもよい。   A guide plate 7 is provided in the hydrogen generation chamber 15. The guide plate 7 and the side surface of the cylindrical cell 51a are fixed via an elastic power supply terminal 32a formed of, for example, one or more alloys selected from nickel, gold, and platinum and processed into a spring shape. . Inside the cylindrical cells 51, 51a, for example, an elastic power supply terminal 22a formed of one or more alloys selected from nickel, gold and platinum and processed into a spring shape is provided, and the oxygen electrode of the cylindrical cell 51 is provided. 31 and the oxygen electrode atmosphere injection tube 13 are brought into contact with each other. This spring-like elastic power supply terminal 22a does not hinder the relative position change between the cylindrical cells 51, 51a and the oxygen electrode atmosphere injection tube 13 due to the flow of steam gas or the temperature change inside the cylindrical cells 51, 51a. You may provide a clearance radially from the center of the cylindrical cells 51 and 51a. Further, instead of these spring-like elastic power supply terminals 22a, power supply terminals having a mesh or felt-like structure may be used.

本実施の形態おいて、酸素極雰囲気注入管13及びガイド板7を導電性材料より形成しているので、円筒セル51,51aの内側に存在する酸素極31及び円筒セル51の外側に存在する水素極21に電解電流を供給するための電流リード端子として用いることが可能である。このとき、酸素極雰囲気供給室12と水素生成室15とは、絶縁層8を介在させることにより、水素極21と酸素極31との短絡を防止する必要がある。   In the present embodiment, since the oxygen electrode atmosphere injection tube 13 and the guide plate 7 are made of a conductive material, the oxygen electrode 31 existing inside the cylindrical cells 51, 51a and the outside of the cylindrical cell 51 exist. It can be used as a current lead terminal for supplying an electrolytic current to the hydrogen electrode 21. At this time, the oxygen electrode atmosphere supply chamber 12 and the hydrogen generation chamber 15 need to prevent a short circuit between the hydrogen electrode 21 and the oxygen electrode 31 by interposing the insulating layer 8.

また、酸素極雰囲気供給室12と酸素極雰囲気注入管13とを電気的に接続し、酸素極雰囲気供給室12の容器外壁から円筒セル1の酸素極雰囲気供給室12に電解電流を供給することができる。また、水素生成室15とガイド板7とを電気的に接続することにより、水素生成室15の外壁から円筒セルの水素極21に電解電流を供給することができる。   Further, the oxygen electrode atmosphere supply chamber 12 and the oxygen electrode atmosphere injection tube 13 are electrically connected to supply an electrolytic current from the outer wall of the oxygen electrode atmosphere supply chamber 12 to the oxygen electrode atmosphere supply chamber 12 of the cylindrical cell 1. Can do. Further, by electrically connecting the hydrogen generation chamber 15 and the guide plate 7, an electrolytic current can be supplied from the outer wall of the hydrogen generation chamber 15 to the hydrogen electrode 21 of the cylindrical cell.

また、円筒セル51、51aの閉端部先端と水素生成室15の内壁との間に、例えば、フェルト状のニッケル又は白金からなる弾性給電端子52aを設置し、電気的接触を確保すると共に円筒セル51、51aの固定を先端と根元の2点で行うことにより、構造的安定性を向上させることができる。   Also, an elastic power supply terminal 52a made of, for example, felt-like nickel or platinum is installed between the closed end tips of the cylindrical cells 51 and 51a and the inner wall of the hydrogen generation chamber 15 to ensure electrical contact and the cylinder. The structural stability can be improved by fixing the cells 51 and 51a at two points of the tip and the base.

また円筒セル51、51aの開端部は、生成酸素排出室14の壁面にガラス及びセラミックス複合材等から形成されるシール材9を介して固定される。このシール材9に接する円筒セル51、51aの接続部10及び生成酸素排出室14のセル接続部16に、予め円環状又はらせん状の刻み目を設けることにより、ガスリークを効果的に防止すると共に、円筒セル51、51aを生成酸素排出室14の壁面により強固に固定することが可能である。   The open ends of the cylindrical cells 51 and 51a are fixed to the wall surface of the product oxygen discharge chamber 14 via a sealing material 9 formed of glass and a ceramic composite material. By providing an annular or spiral notch in advance in the connecting portion 10 of the cylindrical cells 51 and 51a in contact with the sealing material 9 and the cell connecting portion 16 of the generated oxygen discharge chamber 14, gas leakage is effectively prevented, The cylindrical cells 51 and 51a can be firmly fixed to the wall surface of the product oxygen discharge chamber 14.

本実施の形態により、水素と酸素とのガスリークを防止すると共に、セル電極に均一に電解電流を供給し、さらに、円筒セルと装置を構成する材料間との熱膨張率差を吸収することにより、ガスシールの信頼性が高く、強固な構造を持ち更に大電力供給を可能とする高温水蒸気電解装置を製造することができる。   According to the present embodiment, gas leakage between hydrogen and oxygen is prevented, an electrolytic current is uniformly supplied to the cell electrode, and further, a difference in thermal expansion coefficient between the cylindrical cell and the material constituting the device is absorbed. A high-temperature steam electrolysis apparatus that has a highly reliable gas seal, has a strong structure, and can supply a large amount of power can be manufactured.

本発明による第1の実施の形態の高温水蒸気電解装置の構成を示す概略縦断面図。BRIEF DESCRIPTION OF THE DRAWINGS The schematic longitudinal cross-sectional view which shows the structure of the high temperature steam electrolysis apparatus of 1st Embodiment by this invention. 図1の円筒型水蒸気電解セルの構成を示す縦断面図。The longitudinal cross-sectional view which shows the structure of the cylindrical steam electrolysis cell of FIG. 図1の円筒型水蒸気電解セルの他の構成を示す縦断面図。The longitudinal cross-sectional view which shows the other structure of the cylindrical steam electrolysis cell of FIG. 本発明による第2の実施の形態の高温水蒸気電解装置の構成を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the structure of the high temperature steam electrolyzer of 2nd Embodiment by this invention. 図4の円筒型水蒸気電解セルの構成を示す縦断面図。The longitudinal cross-sectional view which shows the structure of the cylindrical steam electrolysis cell of FIG. 図4の円筒型水蒸気電解セルの他の構成を示す縦断面図。The longitudinal cross-sectional view which shows the other structure of the cylindrical steam electrolysis cell of FIG.

符号の説明Explanation of symbols

1,1a、51,51a…円筒型水蒸気電解セル、2…水蒸気供給室、3…水蒸気注入管、4…生成水素排出室、5…酸素生成室、6…支持管、7…ガイド板、8…絶縁層、9…シール材、10…円筒セルの接続部、11…生成水素排出室のセル接続部、12…酸素極雰囲気供給室、13…酸素極雰囲気注入管、14…生成酸素排出室、15…水素生成室、16…生成酸素排出室のセル接続部、21…水素極、22、22a,32,32a,52,52a…弾性給電端子、23…集電体、31…酸素極、35…電解質、41…水蒸気、42…生成水素、43…酸素極雰囲気、44…生成酸素、45…直流電源。   DESCRIPTION OF SYMBOLS 1,1a, 51,51a ... Cylindrical steam electrolysis cell, 2 ... Steam supply chamber, 3 ... Steam injection tube, 4 ... Production hydrogen discharge chamber, 5 ... Oxygen production chamber, 6 ... Support tube, 7 ... Guide plate, 8 DESCRIPTION OF SYMBOLS ... Insulating layer, 9 ... Sealing material, 10 ... Connection part of cylindrical cell, 11 ... Cell connection part of product hydrogen discharge chamber, 12 ... Oxygen electrode atmosphere supply chamber, 13 ... Oxygen electrode atmosphere injection tube, 14 ... Product oxygen discharge chamber 15 ... hydrogen generation chamber, 16 ... cell connection part of the generated oxygen discharge chamber, 21 ... hydrogen electrode, 22, 22a, 32, 32a, 52, 52a ... elastic power supply terminal, 23 ... current collector, 31 ... oxygen electrode, 35 ... electrolyte, 41 ... water vapor, 42 ... generated hydrogen, 43 ... oxygen atmosphere, 44 ... generated oxygen, 45 ... direct current power source.

Claims (11)

内側に水素極を有し外側に酸素極を有し少なくとも1個配設されて下端を閉じた筒状の水蒸気電解セルと、
この水蒸気電解セルの上方に設けられ水蒸気が供給される水蒸気供給室と、
この水蒸気供給室より垂下され前記水蒸気電解セルの内側に水蒸気を供給する水蒸気注入管と、
前記水蒸気供給室の下部に設けられ前記水素極で生成した水素を系外に取り出す生成水素排出室と、
この生成水素排出室の下部に設けられ前記酸素極の雰囲気を調整し生成した酸素を取り出す酸素生成室と、
前記水蒸気電解セルの内側に配設され前記水素極に電解電流を供給する水素極弾性給電手段と、
前記酸素生成室の内部に設けられ前記酸素極に電解電流を供給する酸素極弾性給電手段とを有し、
前記水蒸気供給室と前記酸素生成室との間に絶縁層を介在させ、
前記水蒸気供給室から前記水素極に電解電流を供給し、さらに前記酸素生成室の外壁から前記酸素極に電解電流を供給すること、を特徴とする高温水蒸気電解装置。
A cylindrical steam electrolysis cell having a hydrogen electrode on the inside and an oxygen electrode on the outside and having a lower end closed,
A steam supply chamber provided above the steam electrolysis cell and supplied with steam;
A water vapor injection pipe that hangs down from the water vapor supply chamber and supplies water vapor to the inside of the water vapor electrolysis cell;
A generated hydrogen discharge chamber provided at a lower portion of the water vapor supply chamber to extract hydrogen generated at the hydrogen electrode out of the system;
An oxygen generation chamber provided at a lower portion of the generated hydrogen discharge chamber to take out oxygen generated by adjusting the atmosphere of the oxygen electrode;
Hydrogen polar elastic power supply means disposed inside the steam electrolysis cell and supplying an electrolytic current to the hydrogen electrode;
An oxygen polar elastic power supply means provided inside the oxygen generation chamber for supplying an electrolytic current to the oxygen electrode ;
An insulating layer is interposed between the water vapor supply chamber and the oxygen generation chamber;
An electrolysis current is supplied from the steam supply chamber to the hydrogen electrode, and an electrolysis current is supplied from the outer wall of the oxygen generation chamber to the oxygen electrode .
前記水素極弾性給電手段は、導電性材料から形成される水蒸気注入管と前記水素極との間に設けられたニッケル、金及び白金から選択された1種または2種以上の合金から形成されたメッシュ又はバネを具備すること、を特徴とする請求項1記載の高温水蒸気電解装置。   The hydrogen electrode elastic power feeding means is formed of one or more alloys selected from nickel, gold and platinum provided between a water vapor injection tube formed of a conductive material and the hydrogen electrode. The high-temperature steam electrolysis apparatus according to claim 1, further comprising a mesh or a spring. 前記酸素弾性極給電手段は、前記水蒸気電解セルの外表面に、ニッケル、金及び白金から選択された1種または2種以上の合金から成る線材をらせん状に若しくはメッシュとして巻き付けて形成される集電体又は多孔質状の導電性酸化物から形成される集電体を具備すること、を特徴とする請求項1又は2記載の高温水蒸気電解装置。   The oxygen elastic electrode power feeding means is formed by winding a wire made of one or more alloys selected from nickel, gold and platinum around the outer surface of the steam electrolysis cell in a spiral shape or as a mesh. The high-temperature steam electrolysis apparatus according to claim 1 or 2, further comprising a current collector formed of an electric conductor or a porous conductive oxide. 前記酸素弾性極給電手段は、前記水蒸気電解セルの外周面と前記酸素生成室の内部に設けられたガイド板との間に設けられた給電端子を具備すること、を特徴とする請求項1乃至3のいずれかに記載の高温水蒸気電解装置。   The said oxygen elastic electrode electric power feeding means comprises the electric power feeding terminal provided between the outer peripheral surface of the said steam electrolysis cell, and the guide plate provided in the inside of the said oxygen production | generation chamber, The 1 thru | or characterized by the above-mentioned. 4. The high temperature steam electrolyzer according to any one of 3 above. 前記水蒸気電解セルの下端と前記酸素生成室の内壁との間に、ニッケル、金及び白金から選択された1種または2種以上の合金から形成されたメッシュ又はバネを設けること、を特徴とする請求項1乃至4のいずれかに記載の高温水蒸気電解装置。 A mesh or spring formed of one or more alloys selected from nickel, gold and platinum is provided between the lower end of the steam electrolysis cell and the inner wall of the oxygen generation chamber. The high temperature steam electrolyzer according to any one of claims 1 to 4 . 前記生成水素排出室の壁面に固定するシール部に接する前記水蒸気電解セルの上部外側面及び前記生成水素排出室の壁面に円環状又はらせん状の刻み目を設けること、を特徴とする請求項1乃至5のいずれかに記載の高温水蒸気電解装置。 2. An annular or spiral notch is provided on the upper outer surface of the steam electrolysis cell in contact with a seal portion fixed to the wall surface of the product hydrogen discharge chamber and the wall surface of the product hydrogen discharge chamber. The high-temperature steam electrolysis apparatus according to any one of 5 . 内側に酸素極を有し外側に水素極を有し少なくとも1個配設されて下端を閉じた筒状の水蒸気電解セルと、
この水蒸気電解セルの上方に設けられ空気を含む酸素極雰囲気が供給される酸素極雰囲気供給室と、
この酸素極雰囲気供給室より垂下され前記水蒸気電解セルの内側に前記酸素極雰囲気を供給する酸素極雰囲気注入管と、
前記酸素極雰囲気供給室の下部に設けられ前記酸素極雰囲気を調整し生成した酸素を系外に取り出す生成酸素排出室と、
この生成酸素排出室の下部に設けられ水蒸気が供給されて、この水蒸気から前記水素極における電極反応によって水素を生成させ、この水素極で生成した水素を取り出す水素生成室と、
前記水蒸気電解セルの内側に配設され前記酸素極に電解電流を供給する酸素極弾性給電手段と、
前記水素生成室の内部に設けられ前記水素に電解電流を供給する水素極弾性給電手段とを有し、
前記酸素雰囲気供給室と前記水素生成室との間に絶縁層を介在させ、
前記酸素雰囲気供給室から前記酸素極に電解電流を供給し、さらに前記水素生成室の外壁から前記水素極に電解電流を供給すること、を特徴とする高温水蒸気電解装置。
A cylindrical steam electrolysis cell having an oxygen electrode on the inside and a hydrogen electrode on the outside and having a closed lower end,
An oxygen electrode atmosphere supply chamber provided above the steam electrolysis cell and supplied with an oxygen electrode atmosphere containing air ;
And inside it said oxygen supplying electrode atmosphere oxygen electrode atmosphere inlet tube of the steam electrolysis cell is suspended from the oxygen electrode atmosphere supply chamber,
A generated oxygen discharge chamber provided in a lower part of the oxygen electrode atmosphere supply chamber to extract oxygen generated by adjusting the oxygen electrode atmosphere ;
A hydrogen generation chamber provided in a lower portion of the generated oxygen discharge chamber, supplied with water vapor, generates hydrogen by an electrode reaction at the hydrogen electrode from the water vapor, and takes out the hydrogen generated at the hydrogen electrode;
An oxygen polar elastic power supply means that is disposed inside the steam electrolysis cell and supplies an electrolysis current to the oxygen electrode;
And a hydrogen electrode resilient power supply means for supplying an electrolytic current to the hydrogen electrode provided inside the hydrogen generator chamber,
Interposing an insulating layer between the oxygen electrode atmosphere supply chamber and the hydrogen generation chamber;
An electrolysis current is supplied from the oxygen electrode atmosphere supply chamber to the oxygen electrode, and further an electrolysis current is supplied from the outer wall of the hydrogen generation chamber to the hydrogen electrode.
前記酸素極給弾性電手段は、導電性材料から形成される酸素極雰囲気注入管と前記酸素極との間に設けられたニッケル、金及び白金から選択された1種または2種以上の合金から形成されたメッシュ又はバネを具備すること、を特徴とする請求項7記載の高温水蒸気電解装置。 The oxygen electrode supply elastic electric means is made of one or more alloys selected from nickel, gold and platinum provided between an oxygen electrode atmosphere injection tube formed of a conductive material and the oxygen electrode. The high-temperature steam electrolysis apparatus according to claim 7, further comprising a formed mesh or spring . 前記水素極弾性給電手段は、前記水蒸気電解セルの外表面に、ニッケル、金及び白金から選択された1種または2種以上の合金から成る線材をらせん状に若しくはメッシュとして巻き付けて形成される集電体又は多孔質状の導電性酸化物から形成される集電体を具備すること、を特徴とする請求項7又は8記載の高温水蒸気電解装置。 The hydrogen polar elastic power supply means is formed by winding a wire made of one or two or more alloys selected from nickel, gold and platinum around the outer surface of the steam electrolysis cell in a spiral shape or as a mesh. The high-temperature steam electrolysis apparatus according to claim 7 or 8, further comprising a current collector formed of an electric body or a porous conductive oxide . 前記酸素極弾性給電手段は、前記水蒸気電解セルの外周面と前記水素生成室の内部に設けられたガイド板との間に設けられた給電端子を具備すること、を特徴とする請求項7乃至9のいずれかに記載の高温水蒸気電解装置。 The oxygen oxygen elastic power supply means includes a power supply terminal provided between an outer peripheral surface of the steam electrolysis cell and a guide plate provided in the hydrogen generation chamber. The high temperature steam electrolysis apparatus according to any one of 9 . 前記水蒸気電解セルの下端と前記水素生成室の内壁との間に、ニッケル、金及び白金から選択された1種または2種以上の合金から形成されたメッシュ又はバネを設けること、を特徴とする請求項7乃至10のいずれかに記載の高温水蒸気電解装置。 A mesh or spring formed of one or more alloys selected from nickel, gold, and platinum is provided between the lower end of the steam electrolysis cell and the inner wall of the hydrogen generation chamber. The high temperature steam electrolyzer according to any one of claims 7 to 10 .
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