JPH0533179A - Production of cell for steam electrolysis - Google Patents
Production of cell for steam electrolysisInfo
- Publication number
- JPH0533179A JPH0533179A JP3216132A JP21613291A JPH0533179A JP H0533179 A JPH0533179 A JP H0533179A JP 3216132 A JP3216132 A JP 3216132A JP 21613291 A JP21613291 A JP 21613291A JP H0533179 A JPH0533179 A JP H0533179A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen electrode
- cell
- molding
- electrolyte
- solid electrolyte
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、水蒸気電解用セルの製
造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a cell for steam electrolysis.
【0002】[0002]
【従来の技術】水蒸気電解用セルとしては、電解質にア
ルカリ水溶液を用いるアルカリ型、高分子固体電解質膜
を用いる高分子膜型の一部が実用化され、室温から10
0℃程度までの温度下での電解に用いられている。2. Description of the Related Art As a cell for steam electrolysis, a part of an alkaline type using an aqueous alkaline solution as an electrolyte and a polymer membrane type using a polymer solid electrolyte membrane has been put into practical use.
It is used for electrolysis at temperatures up to about 0 ° C.
【0003】このような水蒸気電解用セルでは、電極反
応に伴う分極を抑制するために白金やパラジウムのよう
な貴金属の触媒を必要とし、また電解に要する分解電圧
が高いためにエネルギーロスが大きいという問題があっ
た。In such a steam electrolysis cell, a catalyst of a noble metal such as platinum or palladium is required to suppress polarization associated with an electrode reaction, and the decomposition voltage required for electrolysis is high, resulting in a large energy loss. There was a problem.
【0004】上記のような問題を解消しうるものとし
て、安定化ジルコニアを電解質として用い1000℃程
度の温度下で電解を行うものが独国のドルニエ社、米国
のウェスティングハウス社等で開発されているが、緻密
な固体電解質膜を必要とし、その方法として、押し出し
成形法、プレズマ溶射法、電気化学蒸着法(EVD)が
用いられていた。In order to solve the above-mentioned problems, a method of using stabilized zirconia as an electrolyte and performing electrolysis at a temperature of about 1000 ° C. was developed by Dornier in Germany and Westinghouse in the United States. However, a dense solid electrolyte membrane is required, and as a method therefor, an extrusion molding method, a plasma spraying method, and an electrochemical vapor deposition method (EVD) have been used.
【0005】さらに、上記のような緻密な固体電解質膜
を作成する方法としては、図8のように安定化ジルコニ
ア粉末3をスラリーにし、基材1上に塗布して焼成する
試みもなされている。Further, as a method of forming the dense solid electrolyte membrane as described above, it has been attempted to make the stabilized zirconia powder 3 into a slurry, apply it to the base material 1 and fire it as shown in FIG. .
【0006】[0006]
【発明が解決しようとする課題】上記した前者の製造方
法では、高価な製造装置を必要とするうえに、固体電解
質膜を必要とする部分と必要としない部分とを構成する
マスキングに時間がかかるため、電池の量産性に問題が
あった。In the former manufacturing method described above, an expensive manufacturing apparatus is required, and it takes a long time to perform masking for forming a portion requiring the solid electrolyte membrane and a portion not requiring the solid electrolyte membrane. Therefore, there was a problem in mass productivity of the battery.
【0007】また、後者の製造方法では、焼成時に安定
化ジルコニア粉末3が収縮するため、基材1の上に構成
された固体電解質膜8に割れ2を生じたり、固体電解質
膜8が剥離するという問題があった。Further, in the latter manufacturing method, the stabilized zirconia powder 3 shrinks during firing, so that cracks 2 occur in the solid electrolyte membrane 8 formed on the base material 1 or the solid electrolyte membrane 8 peels off. There was a problem.
【0008】[0008]
【課題を解決するための手段】上記課題を解決するた
め、本発明は、安定化剤を添加したジルコニアを含有す
るスラリーを成形して電解質成形体とする工程と、前記
電解質成形体の一方の面に、金属もしくは金属酸化物を
含有するスラリーを成形して水素極成形体を構成し、電
解質成形体と水素極成形体とを一体化した複合成形体を
得る工程と、この複合成形体を焼成して固体電解質−水
素極複合体を得る工程と、この固体電解質−水素極複合
体の固体電解質側に空気極を形成することを特徴とする
ものである。In order to solve the above-mentioned problems, the present invention provides a step of forming a slurry containing a zirconia to which a stabilizer is added to form an electrolyte molded body, and one of the above-mentioned electrolyte molded bodies. A step of forming a slurry containing a metal or a metal oxide on the surface to form a hydrogen electrode formed body, and obtaining a composite formed body in which an electrolyte formed body and a hydrogen electrode formed body are integrated; The method is characterized by comprising a step of firing to obtain a solid electrolyte-hydrogen electrode composite, and forming an air electrode on the solid electrolyte side of the solid electrolyte-hydrogen electrode composite.
【0009】[0009]
【作用】上記のように、本発明は、スラリーを成形して
電解質成形体と水素極成形体とを構成してこれらを同時
に焼成しているので、緻密な固体電解質膜と多孔性の水
素極とを容易に形成することができ、その厚みもスラリ
ーを流す時間によって任意にコントロールすることがで
きる。As described above, according to the present invention, a slurry is formed to form an electrolyte formed body and a hydrogen electrode formed body, and these are fired at the same time. Therefore, a dense solid electrolyte membrane and a porous hydrogen electrode are formed. And can be easily formed, and the thickness thereof can be arbitrarily controlled by the time during which the slurry flows.
【0010】一方、スラリー中に添加された金属酸化物
は、水素と接触して還元され、水素極としての作用をす
る。また前記スラリーから構成される水素極成形体は、
焼成することによって水素極の強度が高まり基材として
の作用もする。On the other hand, the metal oxide added to the slurry comes into contact with hydrogen to be reduced and acts as a hydrogen electrode. Further, the hydrogen electrode molded body composed of the slurry,
The firing increases the strength of the hydrogen electrode and also acts as a base material.
【0011】[0011]
【実施例】図1は、本発明の水蒸気電解用セルの製造方
法に使用するスラリーを成形するための型4の断面図
で、石膏のような吸水性を有する材料からなる。EXAMPLE FIG. 1 is a cross-sectional view of a mold 4 for molding a slurry used in the method for producing a cell for steam electrolysis according to the present invention, which is made of a material having a water absorbing property such as gypsum.
【0012】図2は、前記型4に安定化剤としてのイッ
トリアを添加したジルコニア粉末、水、分散材、バイン
ダー、消泡剤からなるスラリーを流し込んで一定時間放
置して電解質成形体5とした後、余剰のスラリーを除去
した状態の断面図である。In FIG. 2, a slurry comprising zirconia powder containing yttria as a stabilizer, water, a dispersant, a binder and a defoaming agent is poured into the mold 4 and left for a certain period of time to prepare an electrolyte molded body 5. After that, it is a cross-sectional view of a state in which excess slurry is removed.
【0013】図3は、前記スラリーに金属酸化物として
の酸化ニッケルを添加したスラリーを、前記電解質成形
体5が乾燥するまでに、その上に流し込んで一定時間放
置して水素極成形体6とした後、余剰のスラリーを除去
した状態の断面図である。なお、この水素極成形体6を
形成するためのスラリーと電解質成形体5を形成するた
めのスラリーとは同一のものでなくてもよいことは言う
までもない。In FIG. 3, a slurry prepared by adding nickel oxide as a metal oxide to the slurry is poured onto the electrolyte molded body 5 and left for a certain period of time until the electrolyte molded body 5 dries, and a hydrogen electrode molded body 6 is formed. FIG. 4 is a cross-sectional view of a state in which a surplus slurry has been removed after the process. It goes without saying that the slurry for forming the hydrogen electrode molded body 6 and the slurry for forming the electrolyte molded body 5 do not have to be the same.
【0014】図4は、図3の状態のものを乾燥させて型
4を除去した後焼成して得た固体電解質−水素極複合体
の断面図で、内側に多孔性の水素極7が形成され、外側
に緻密な固体電解質膜8が形成される。FIG. 4 is a sectional view of a solid electrolyte-hydrogen electrode composite obtained by drying the state of FIG. 3 to remove the mold 4 and then firing it. A porous hydrogen electrode 7 is formed inside. As a result, a dense solid electrolyte membrane 8 is formed on the outside.
【0015】図5は、前記固体電解質−水素極複合体の
固体電解質膜8の外側に空気極9として、ストロンチウ
ムをドープしたLaMnO3 をデイッピング法によって
形成した状態の断面図、すなわち本発明の製造方法によ
って得られた水蒸気電解用セルの断面図である。なお、
空気極9の形成方法としては、デイッピング法以外にス
ラリー塗布法、溶射法等がある。FIG. 5 is a cross-sectional view of a state in which strontium-doped LaMnO 3 is formed by the dipping method as an air electrode 9 on the outside of the solid electrolyte membrane 8 of the solid electrolyte-hydrogen electrode composite, that is, the production of the present invention. FIG. 3 is a cross-sectional view of a steam electrolysis cell obtained by the method. In addition,
As a method for forming the air electrode 9, there are a slurry coating method, a thermal spraying method and the like other than the dipping method.
【0016】こうして得られた図5のような水蒸気電解
用セルを作動温度である700℃から1000℃に昇温
し、水素極7側に水素を、空気極9側に空気を供給する
と、水素によって水素極7中の酸化ニッケルが還元され
る。When the thus obtained cell for steam electrolysis as shown in FIG. 5 is heated from the operating temperature of 700 ° C. to 1000 ° C. and hydrogen is supplied to the hydrogen electrode 7 side and air to the air electrode 9 side, hydrogen is supplied. Thereby, nickel oxide in the hydrogen electrode 7 is reduced.
【0017】そして、図5の水素極7に水蒸気を供給
し、この水素極7を負極、空気極9を正極にして約1V
の電圧を印加すると、水素極7で水蒸気が電解され、外
部回路から供給される電子を取り込んで酸素イオンと水
素とを生成し、この酸素イオンは固体電解質膜8を通っ
て固体電解質膜8と空気極9との界面に到達し、この界
面で酸素イオンは外部回路に電子を放出して酸素とな
り、空気極9中に放出される。Then, water vapor is supplied to the hydrogen electrode 7 in FIG.
When the voltage is applied, the water vapor is electrolyzed at the hydrogen electrode 7, and the electrons supplied from the external circuit are taken in to generate oxygen ions and hydrogen. The oxygen ions pass through the solid electrolyte membrane 8 and the solid electrolyte membrane 8 When it reaches the interface with the air electrode 9, oxygen ions release electrons to the external circuit at this interface to become oxygen, which is released into the air electrode 9.
【0018】以上の説明は、型4が円筒型複合成形体を
製造するためのものであったが、図6のような型4を使
用すれば平板型の複合成形体を、図7のような型4を使
用すればモノリシック型の複合成形体を製造できること
は言うまでもない。In the above description, the mold 4 is for producing a cylindrical composite molded body. However, if the mold 4 as shown in FIG. 6 is used, a flat type composite molded body can be obtained as shown in FIG. It is needless to say that a monolithic type composite molded body can be manufactured by using the mold 4.
【0019】[0019]
【発明の効果】上記した如く、本発明は緻密な固体電解
質膜8と多孔性の水素極7とが容易に形成でき、その厚
みもスラリーを流す時間によって任意にコントロールす
ることができるので、容易に固体電解質膜8の抵抗と機
械的強度とをコントロールすることができ、高性能な水
蒸気電解用セルが得られる。As described above, according to the present invention, the dense solid electrolyte membrane 8 and the porous hydrogen electrode 7 can be easily formed, and the thickness thereof can be arbitrarily controlled by the time of flowing the slurry. Moreover, the resistance and mechanical strength of the solid electrolyte membrane 8 can be controlled, and a high-performance cell for steam electrolysis can be obtained.
【0020】また、吸水性を有する型4にスラリーを流
し込んで電解質成形体5と水素極成形体6とを構成して
焼成しているので、製造工程の簡素化を図ることができ
る。Further, the slurry is poured into the water-absorbing mold 4 to form the electrolyte molded body 5 and the hydrogen electrode molded body 6 and fired, so that the manufacturing process can be simplified.
【図1】本発明の水蒸気電解用セルの製造方法に使用す
る型4の断面図である。FIG. 1 is a cross-sectional view of a mold 4 used in the method for manufacturing a cell for steam electrolysis according to the present invention.
【図2】図1の型4にスラリーを流し込んで一定時間放
置して電解質成形体5とした後、余剰のスラリーを除去
した状態の断面図である。FIG. 2 is a cross-sectional view showing a state in which a slurry is poured into a mold 4 of FIG. 1 and left for a certain period of time to form an electrolyte molded body 5, and then excess slurry is removed.
【図3】図2の電解質成形体5の上にスラリーを流し込
んで一定時間放置して水素極成形体6とした後、余剰の
スラリーを除去して複合成形体とした状態の断面図であ
る。FIG. 3 is a cross-sectional view showing a state where a slurry is poured onto the electrolyte molded body 5 of FIG. 2 and left for a certain period of time to form a hydrogen electrode molded body 6, and then excess slurry is removed to form a composite molded body. .
【図4】図3の複合成形体から型4を除去した後焼成し
て得た固体電解質−水素極複合体の断面図である。4 is a cross-sectional view of a solid electrolyte-hydrogen electrode composite obtained by firing after removing the mold 4 from the composite formed body of FIG.
【図5】固体電解質−水素極複合体の外側に空気極9を
形成した状態の断面図である。FIG. 5 is a cross-sectional view showing a state in which an air electrode 9 is formed outside the solid electrolyte-hydrogen electrode composite.
【図6】本発明の他の実施例に係る複合成形体とした状
態の断面図である。FIG. 6 is a cross-sectional view of a composite molded body according to another embodiment of the present invention.
【図7】本発明の他の実施例に係る複合成形体とした状
態の断面図である。FIG. 7 is a cross-sectional view of a composite molded body according to another embodiment of the present invention.
【図8】従来の水蒸気電解用セルの製造方法により製造
された固体電解質膜8の断面図である。FIG. 8 is a cross-sectional view of a solid electrolyte membrane 8 manufactured by a conventional method for manufacturing a cell for steam electrolysis.
4 型 5 電解質成形体 6 水素極成形体 7 水素極 8 固体電解質膜 9 空気極 Type 4 5 Electrolyte compact 6 Hydrogen electrode molded body 7 Hydrogen electrode 8 Solid electrolyte membrane 9 air poles
Claims (5)
るスラリーを成形して電解質成形体とする工程と、前記
電解質成形体の一方の面に、金属もしくは金属酸化物を
含有するスラリーを成形して水素極成形体を構成し、電
解質成形体と水素極成形体とを一体化した複合成形体を
得る工程と、この複合成形体を焼成して固体電解質−水
素極複合体を得る工程と、この固体電解質−水素極複合
体の固体電解質側に空気極を形成することを特徴とする
水蒸気電解用セルの製造方法。1. A step of forming a slurry containing zirconia to which a stabilizer is added to form an electrolyte compact, and forming a slurry containing a metal or a metal oxide on one surface of the electrolyte compact. And forming a hydrogen electrode formed body, a step of obtaining a composite formed body that integrates the electrolyte formed body and the hydrogen electrode formed body, and a step of firing the composite formed body to obtain a solid electrolyte-hydrogen electrode composite, A method for producing a cell for steam electrolysis, which comprises forming an air electrode on the solid electrolyte side of this solid electrolyte-hydrogen electrode composite.
ジルコニア、正方晶ジルコニア、部分安定化ジルコニア
の単独物もしくは複数種の混合物からなることを特徴と
する請求項第1項記載の水蒸気電解用セルの製造方法。2. The steam electrolysis according to claim 1, wherein the zirconia added with the stabilizer comprises cubic zirconia, tetragonal zirconia and partially stabilized zirconia alone or as a mixture of plural kinds. Cell manufacturing method.
ム、スカンジウム、イッテルビウム、ネオジウム、ガド
リニウムの酸化物であることを特徴とする請求項第1項
記載の水蒸気電解用セルの製造方法。3. The method for producing a cell for steam electrolysis according to claim 1, wherein the stabilizer is an oxide of yttrium, calcium, scandium, ytterbium, neodymium, or gadolinium.
たはコバルトの酸化物もしくは金属ニッケルまたは金属
コバルトであることを特徴とする請求項第1項記載の水
蒸気電解用セルの製造方法。4. The method for producing a cell for steam electrolysis according to claim 1, wherein the metal oxide or metal is an oxide of nickel or cobalt, or metal nickel or metal cobalt.
シウムをドープしたLaMnO3 、LaCoO3 、Ca
MnO3 であることを特徴とする請求項第1項記載の水
蒸気電解用セルの製造方法。5. The air electrode comprises LaMnO 3 , LaCoO 3 , Ca doped with strontium or calcium.
The method for producing a cell for steam electrolysis according to claim 1, wherein the cell is MnO 3 .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3216132A JPH0533179A (en) | 1991-07-31 | 1991-07-31 | Production of cell for steam electrolysis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3216132A JPH0533179A (en) | 1991-07-31 | 1991-07-31 | Production of cell for steam electrolysis |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0533179A true JPH0533179A (en) | 1993-02-09 |
Family
ID=16683768
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3216132A Pending JPH0533179A (en) | 1991-07-31 | 1991-07-31 | Production of cell for steam electrolysis |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0533179A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110791774A (en) * | 2018-08-02 | 2020-02-14 | 国家能源投资集团有限责任公司 | Method for producing hydrogen by electrolyzing water vapor |
-
1991
- 1991-07-31 JP JP3216132A patent/JPH0533179A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110791774A (en) * | 2018-08-02 | 2020-02-14 | 国家能源投资集团有限责任公司 | Method for producing hydrogen by electrolyzing water vapor |
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