JPS63250065A - Oxygen ion conductive membrane and its manufacturing method - Google Patents
Oxygen ion conductive membrane and its manufacturing methodInfo
- Publication number
- JPS63250065A JPS63250065A JP62082473A JP8247387A JPS63250065A JP S63250065 A JPS63250065 A JP S63250065A JP 62082473 A JP62082473 A JP 62082473A JP 8247387 A JP8247387 A JP 8247387A JP S63250065 A JPS63250065 A JP S63250065A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen ion
- ion conductive
- conductive membrane
- yttria
- oxygen
- 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
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/2425—High-temperature cells with solid electrolytes
- H01M8/243—Grouping of unit cells of tubular or cylindrical configuration
-
- 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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/124—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte
- H01M8/1246—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte the electrolyte consisting of oxides
- H01M8/126—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte the electrolyte consisting of oxides the electrolyte containing cerium oxide
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Fuel Cell (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
この発明は固体電解質を利用した高温固体電解質燃料電
池(以下固体燃料電池と略称する)や酸素センサー、酸
禦ボング等の酸素イオン伝導体に関するものである。[Detailed Description of the Invention] Industrial Application Field This invention relates to oxygen ion conductors such as high-temperature solid electrolyte fuel cells (hereinafter abbreviated as solid fuel cells) using solid electrolytes, oxygen sensors, and acid bongs. be.
従来の技術
酸素イオン伝導体として、#化ジルコニウム(ZrO,
)K酸化イットリウA (Y、 0. )または酸化カ
ルシウム(CaO)をモル比で90 : 10ないし8
0 : 20で固溶させたものが用いられている。Conventional technology As an oxygen ion conductor, zirconium chloride (ZrO,
) K yttrium oxide A (Y, 0.) or calcium oxide (CaO) in a molar ratio of 90:10 to 8
A solid solution of 0:20 is used.
また、イオン伝導体の製造方法として焼結法やグラズマ
溶射法、フレーム溶射法、CVD法。In addition, sintering methods, glazma spraying methods, flame spraying methods, and CVD methods are used to manufacture ion conductors.
スパッタリング法、塗膜熱分解法が用いられている。Sputtering method and coating film pyrolysis method are used.
発明が解決しようとする問題点
酸化ジルコニウム(ZrO□)ICd化イツトリウム(
Y、 Os )を固溶させた安定化ジルコニアでは、1
000℃においてイオン伝導率が9X10”(Ω−1・
am−’)、 6QQ℃において2XIO−”(Ω−1
・―″″′)と小さい。そのため1例えば、固体慾料−
2〜
電池の固体電解質として用いた場合1000℃程度の高
温でしか作動することができない。本発明は酸素イオン
伝導率の向上を目的とする。ものである。Problems to be solved by the invention Zirconium oxide (ZrO□) IC yttrium oxide (
In stabilized zirconia containing Y, Os) as a solid solution, 1
The ionic conductivity at 000℃ is 9X10"(Ω-1・
am-'),2XIO-''(Ω-1 at 6QQ℃
・―″″′) and small. Therefore, 1. For example, solid stimulant -
2~ When used as a solid electrolyte in a battery, it can only operate at a high temperature of about 1000°C. The present invention aims to improve oxygen ion conductivity. It is something.
問題点を解決するための手段
本発明はセリア−イットリアからなる固溶体で、酸素イ
オン伝導His構成したものである。Means for Solving the Problems The present invention is a solid solution consisting of ceria-yttria, which has an oxygen ion conductive His structure.
酸素イオンの高イオン伝導率を持つ物質として酸化セリ
クム、即ちセリアを選び、酸化セリウム(CeO,)に
酸化イツトリウム(Yt03)。Cerium oxide, or ceria, was selected as a material with high ionic conductivity for oxygen ions, and cerium oxide (CeO,) and yttrium oxide (Yt03) were selected.
即ち、イツトリアを固溶させイオン伝導率の高いモル比
である70 : 30〜96.5 : 3.5の材料を
選んだ、また、同物質を高温の得られるプラズマ溶射装
置などを用い厚さ5〜750(μrn)の範囲で薄膜化
し酸素イオン伝導膜を形成した。That is, we selected a material with a molar ratio of 70:30 to 96.5:3.5, which contains ittria as a solid solution and has a high ionic conductivity. The oxygen ion conductive film was formed into a thin film in the range of 5 to 750 (μrn).
作用
本発明の酸素イオン伝導膜を固体燃料電池に応用した時
の作用について説明する。矛1図に固体燃料電池の動作
原理図をしめす。酸素イオン伝導膜2は、固体電解質で
あって酸素イオン02−を透過させる。これは1例えば
酸化ジルコニタム(ZrO,)に酸化イツトリウム(L
Os )を固溶させた場合Zrイオンは4イ価である
が。Function The function when the oxygen ion conductive membrane of the present invention is applied to a solid fuel cell will be explained. Figure 1 shows the operating principle of a solid fuel cell. The oxygen ion conductive membrane 2 is a solid electrolyte and allows oxygen ions 02- to pass therethrough. For example, zirconitum oxide (ZrO, ) and yttrium oxide (L
When Zr ions are dissolved in solid solution, Zr ions have a valence of 4.
固溶したイツトリウムは34面となり酸素イオンの空孔
子が発生し、この空孔子により酸素イオンが移動する。The solid-dissolved yttrium has 34 planes, and vacancies of oxygen ions are generated, and the vacancies cause the movement of oxygen ions.
1は水素側電極で、3は酸素側′tPL極である。酸業
ガス入07より4入された醒業は酸素側電極3と電解質
2の界面12にて、1/2・0. +2e→02−の反
応で一部イオン化され、電界質2内を移動し、水禦側電
極IK達する。余剰酸素は酸素ガス出口8より排出され
る。一方慾料ガス人口9より導入された燃料ガス塩の一
部は水素側電極1と′IJtP!I質界面11にてH,
−f−0” −→H,0+ 26の反応により水蒸気と
なる。この水蒸気は余刺水巣と共に燃料ガス出口10よ
りυP川される。一方。1 is a hydrogen side electrode, and 3 is an oxygen side 'tPL electrode. The acid gas entered from 07 to 4 times is 1/2.0 at the interface 12 between the oxygen side electrode 3 and the electrolyte 2. It is partially ionized by the reaction +2e→02-, moves in the electrolyte 2, and reaches the water electrode IK. Excess oxygen is discharged from the oxygen gas outlet 8. On the other hand, a part of the fuel gas salt introduced from the fuel gas population 9 is connected to the hydrogen side electrode 1 and 'IJtP! H at the I-quality interface 11,
-f-0'' -→H,0+ The reaction of 26 turns into water vapor. This water vapor is discharged from the fuel gas outlet 10 along with the remaining water vapor into the υP river. On the other hand.
水素側電極1で発生した電子は外部回路を通過し、負#
4で仕事をした俊、酸素側を極3に達する。この際電圧
1ft5により負荷40両端の起′亀力を電流計6によ
り電流値を測距する。また水素を燃料にした時の水蒸気
生成に伴う起電力は1次式で与えられる。The electrons generated at the hydrogen side electrode 1 pass through the external circuit and become negative #
Shun, who worked at 4, reached pole 3 on the oxygen side. At this time, the current value of the starting force at both ends of the load 40 is measured using the ammeter 6 using a voltage of 1 ft5. Furthermore, the electromotive force associated with water vapor generation when hydrogen is used as fuel is given by a linear equation.
[=33θ十几T/2F 1%CP(Hz)”〆゛・
P(Hオ)/P(H2O))Eθ:標準起電力(V)
P(0,):酸素極側の酸素分圧 R:気体室数 P
CHt)”燃料中の水素分圧P (Hz Ox ) ”
燃料中の水素分圧 T:絶対温度Fニアアラデー足数
この式より無負荷時、即ち開回路時の起電力があたえら
れる。[=33θ 10T/2F 1%CP (Hz)”〆゛・
P(HO)/P(H2O))Eθ: Standard electromotive force (V)
P(0,): Oxygen partial pressure on the oxygen electrode side R: Number of gas chambers P
CHt) "Hydrogen partial pressure in fuel P (Hz Ox)"
Partial pressure of hydrogen in fuel T: Absolute temperature F Near Alladay number This formula gives the electromotive force at no load, that is, at an open circuit.
また、電池に負荷をかけたときの電流−電圧特性即ち1
−V特性の模式図を図2に示す。電極単位面積肖りの電
流即ち電流密度が増すと、固体電解質及び電極内の内部
抵抗のため端子電圧は低下する。この電圧降下はイオン
や電子の移動に対する抵抗によるものが主であるが、次
の手段によって低減できる。即ち
■ ′RL解質として酸素イオン伝専′注の高く電子電
導性の低い材料を選択する。Also, the current-voltage characteristics when a load is applied to the battery, that is, 1
A schematic diagram of the −V characteristics is shown in FIG. As the current per unit area of the electrode, or current density, increases, the terminal voltage decreases due to the solid electrolyte and internal resistance within the electrode. This voltage drop is mainly due to resistance to the movement of ions and electrons, but it can be reduced by the following means. That is, 1) A material with high oxygen ion conductivity and low electron conductivity is selected as the RL solute.
■ 電解質を薄膜として全抵抗を低下させる。■ Lower the total resistance by using a thin electrolyte film.
■ 電解質両側の一宏分圧の比を高(保つため−ζ −
に、ガスが電解質を通過しないように緻密な皮膜を形成
する。■ To maintain a high ratio of Kazuhiro partial pressures on both sides of the electrolyte (-ζ -), a dense film is formed to prevent gas from passing through the electrolyte.
本発明では図1の■で示す固体電解質、即ち・酸素イオ
ン伝導体に係るもので材料として酸化セリウム(ceo
オ)に酸化イツトリウム(Ym Os )をCeO,:
yo、、で70 : 30〜96,5 : 3.5の
モル比で固溶させたものを用いている。同材料は、ジル
コニア−イツトリアと同様、蛍石型構造の結晶において
4鋤のセリウムイオン位置に34曲のイツトリウムイオ
ンが置換され、酸素イオン空孔が発生し、この空孔によ
り酸素イオン伝導性が発生する。例えば酸化セリウムに
酸化イツトリウムをlOモ/l/%固溶させた場合と、
酸倍と、セリア系の材料は高い伝導率をしめす。In the present invention, the solid electrolyte indicated by ■ in FIG.
e) yttrium oxide (YmOs) to CeO,:
A solid solution of 70:30 to 96,5:3.5 is used. Similar to zirconia-yttria, this material has a fluorite-type crystal structure in which 34 yttrium ions are substituted for 4 cerium ion positions, creating oxygen ion vacancies, and these vacancies provide oxygen ion conductivity. occurs. For example, when yttrium oxide is dissolved in cerium oxide at lOmol/l/%,
Acid-based materials exhibit high conductivity.
又、ジルコニア系の1000℃の稼働と、セリア系の5
00℃の稼働が同程度に伝導率を示す。In addition, zirconia-based 1000℃ operation and ceria-based 5
00°C operation shows similar conductivity.
実施例 矛3図に実用化された燃料電池素子を示す。Example Figure 3 shows a fuel cell element that has been put to practical use.
内側の円筒型の多孔質のセ5ミックスチューブ加に後述
する電極、電解質、電流導出部を複数組形成した。 7
00〜1000℃の高温状態におかれた燃料電池素子の
内部に燃料ガス人口31よ排出される。46 、47は
電流導出部である。In addition to the inner cylindrical porous semi-mix tube, a plurality of sets of electrodes, electrolytes, and current lead-out portions, which will be described later, were formed. 7
Fuel gas 31 is discharged into the fuel cell element which is kept at a high temperature of 00 to 1000 degrees Celsius. 46 and 47 are current deriving parts.
矛3図の燃料電池素子の断面拡大図である矛4図におい
て42は水素側の電極、43は固体電解質。In Figure 4, which is an enlarged cross-sectional view of the fuel cell element shown in Figure 3, 42 is an electrode on the hydrogen side, and 43 is a solid electrolyte.
■は酸素側電極であり、45は接続部であり、46゜4
7は電流導出部であり、才4図の溝近の電池を複数個直
列抜脱することにより、を力の増大が出来た。■ is the oxygen side electrode, 45 is the connection part, 46°4
7 is a current lead-out part, and the power can be increased by removing and removing multiple Mizochika batteries shown in Figure 4 in series.
電解質以外の材料としては例えば、水素側電極42には
酸化ニッケル(MJ、0)、賑素側電極材には酸化ラン
タンコバルト(Labors )また接続部45 ’P
1tfN、導出部45 、47にはニッケルアルミ(
NtAx)等を用いた。Examples of materials other than the electrolyte include nickel oxide (MJ, 0) for the hydrogen side electrode 42, lanthanum cobalt oxide (Labors) for the nitrogen side electrode material, and connection part 45'P.
1tfN, the lead-out parts 45 and 47 are made of nickel aluminum (
NtAx) etc. were used.
また、薄膜形成方法として用いるプラズマ溶射装置は例
えば特願昭ω−101082号の発明の溝近をもってお
り、その溝近は矛5図に示す域昭τ℃滞17時間が長く
保持されるρで、よ(溶融され、緻密な伝導膜54を形
成する。以上の様に高いイオン伝導率のセリア−イット
リア固溶体を用いて固体電解質を形成することにより、
初期の目的である燃料電池の内部抵抗を低減でき、かつ
酸素及び、燃料ガスの漏れを防ぎ、高発電特性が得られ
た。In addition, the plasma spraying apparatus used as a thin film forming method has, for example, a groove breaker according to the invention of Japanese Patent Application No. Showa ω-101082. , is melted to form a dense conductive film 54. By forming a solid electrolyte using the ceria-yttria solid solution with high ionic conductivity as described above,
The initial objective was to reduce the internal resistance of the fuel cell, prevent oxygen and fuel gas leaks, and achieve high power generation characteristics.
牙5図において、55は基板、56は陰極、57は陽極
、58は溶融被膜材料である。なお、上述のプラズマ溶
射装置は、それに限定されるものでなく1例えば、特願
昭60−101081号等の装置を用いることができる
。In Figure 5, 55 is a substrate, 56 is a cathode, 57 is an anode, and 58 is a molten coating material. Note that the above-mentioned plasma spraying apparatus is not limited thereto, and for example, an apparatus such as that disclosed in Japanese Patent Application No. 101081/1981 can be used.
発明の効果
本発明は上述の溝底にしたので、#R素イオン伝導率を
著しく向上することができる。更に。Effects of the Invention Since the present invention uses the above-mentioned groove bottom, #R elementary ion conductivity can be significantly improved. Furthermore.
固体電解質燃料電池に本発明により作成した醗紫イオン
伝導膜を固体電解質として適用した場合の発電特性に対
する効果についてのべる。This article describes the effect on power generation characteristics when the red ion conductive membrane prepared according to the present invention is applied as a solid electrolyte to a solid electrolyte fuel cell.
従来の焼結法で作成した厚さ2簡のジルコニア−イツト
リア固溶体電解質による燃料電池と。A fuel cell using a 2-layer zirconia-yttria solid solution electrolyte made using a conventional sintering method.
本発明によるプラズマ溶射により作成した厚さ200/
jsのセリア−イットリア固溶体電、弄質による燃料電
池の発電特性を800℃において比較する。オ6図に示
す如<i−v特性においては直線の傾きが61のジルコ
ニア−イツトリアの焼結体電解質に対して62のセリア
−イットリアの溶射電解質膜では直線の勾配が約177
と減少した。Thickness 200/200 mm produced by plasma spraying according to the present invention
The power generation characteristics of a fuel cell using a ceria-yttria solid solution electrolyte of JS are compared at 800°C. As shown in Figure 6, in the i-v characteristics, the slope of the straight line is approximately 177 for the zirconia-yttria sintered electrolyte with a slope of 62, and the sprayed electrolyte membrane of ceria-yttria of 62.
and decreased.
これは、電解質の内部抵抗が約1/7になったことを示
している。また矛7図に示すように電流−電力特性で(
I−P特性)比較すると、72のセリア−イットリア系
溶射電解質膜では、71のジルコニア−イツトリア焼結
電解質に比較して。This indicates that the internal resistance of the electrolyte was reduced to about 1/7. In addition, as shown in Figure 7, the current-power characteristics (
I-P characteristics) In comparison, the ceria-yttria sprayed electrolyte membrane of 72 compared to the zirconia-yttria sintered electrolyte of 71.
ピーク値で約2.5倍の電力密度が得られる。Approximately 2.5 times the power density can be obtained at the peak value.
また1本発明によるプラズマ溶射により作成した厚さ2
00μmのセリア−イットリア固溶体電解質とした燃料
電池の発電特性を900℃において比較する。矛8図は
、900℃における電流−電力特性で、81はセリア−
イットリア系溶射電解質、82はジルコニア−イツトリ
ア系溶射電解質であり、ピーク値で約1.7倍の電力密
度が得られた。In addition, 1 the thickness 2 created by plasma spraying according to the present invention.
The power generation characteristics of a fuel cell using a ceria-yttria solid solution electrolyte with a thickness of 00 μm are compared at 900°C. Figure 8 shows the current-power characteristics at 900°C, and 81 shows the ceria-power characteristics.
The yttria-based thermal sprayed electrolyte 82 is a zirconia-yttria-based thermal sprayed electrolyte, and a power density of about 1.7 times the peak value was obtained.
矛1図は本発明の酸素イオン伝導膜を用いた燃料電池の
回路図、乏・2図は矛1図の燃料電池に負荷をかけたと
きの電流■−電圧V線図、矛3図は本発明の燃料電池の
実施例の一部分を切断した正面図%、114図は矛3図
の一部分拡大断面図、矛5図は本発明の酸素イオン伝導
膜の製造方法を示す断面図、Ar6図は本発明と従来例
の電流■−電電圧時特性示す線図、矛7図及び矛8図は
本発明と従来例の電流I−電力P特性を示す線図である
。
1・・・水素側電極
2・・・固体電解質
3・・・酸素側電極
7・・・酸素ガス入口
9・・・燃料ガス入口
シ・・・伝導膜
代理人弁理士 盾 藤 侑、]−“−(ほか 2名
)−Figure 1 is a circuit diagram of a fuel cell using the oxygen ion conductive membrane of the present invention, Figures 2 and 2 are current ■ - voltage V diagrams when a load is applied to the fuel cell shown in Figure 1, and Figure 3 is a diagram of the current Figure 114 is a partial enlarged sectional view of Figure 3, Figure 5 is a sectional view showing the method for manufacturing the oxygen ion conductive membrane of the present invention, Figure Ar6 is a partially cutaway front view of the embodiment of the fuel cell of the present invention. 1 is a diagram showing the current I-voltage characteristic of the present invention and the conventional example, and Figures 7 and 8 are diagrams showing the current I-power P characteristic of the present invention and the conventional example. 1...Hydrogen side electrode 2...Solid electrolyte 3...Oxygen side electrode 7...Oxygen gas inlet 9...Fuel gas inlet...Conductive membrane agent Yu Shishifuji, ]- “-(2 others)-
Claims (1)
る事を特徴とする酸素イオン伝導膜。 2 セリア−イットリアの対比で70:30ないし96
.5:3.5の範囲である事を特徴とする酸素イオン伝
導膜。 3 セリア−イットリアからなる固溶体が溶射により通
気性基材に膜状に形成されていることを特徴とする酸素
イオン伝導膜。 4 膜状の固溶体の厚さが5μmないし750μmであ
ることを特徴とする酸素イオン伝導膜。 5 セリア−イットリアの固溶体からなる粒径10〜8
0μmの溶射材料を通気性基材に溶射して薄膜を形成す
ることを特徴とする酸素イオン伝導膜の製造方法。[Claims] 1. An oxygen ion conductive membrane characterized by being formed of a solid solution of ceria-yttria. 2 Seria-Yttria comparison 70:30 to 96
.. An oxygen ion conductive membrane characterized in that the ratio is in the range of 5:3.5. 3. An oxygen ion conductive membrane characterized in that a solid solution consisting of ceria-yttria is formed in the form of a membrane on an air-permeable base material by thermal spraying. 4. An oxygen ion conductive membrane characterized in that the thickness of the membrane-like solid solution is 5 μm to 750 μm. 5 Particle size 10-8 consisting of ceria-yttria solid solution
A method for producing an oxygen ion conductive membrane, comprising spraying a 0 μm sprayed material onto a breathable base material to form a thin film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62082473A JPS63250065A (en) | 1987-04-03 | 1987-04-03 | Oxygen ion conductive membrane and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62082473A JPS63250065A (en) | 1987-04-03 | 1987-04-03 | Oxygen ion conductive membrane and its manufacturing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63250065A true JPS63250065A (en) | 1988-10-17 |
Family
ID=13775479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62082473A Pending JPS63250065A (en) | 1987-04-03 | 1987-04-03 | Oxygen ion conductive membrane and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63250065A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0855630A (en) * | 1994-05-09 | 1996-02-27 | Air Prod And Chem Inc | Electrochemical solid state device for ion transport by electrolyte |
| WO2018190205A1 (en) * | 2017-04-10 | 2018-10-18 | 三井金属鉱業株式会社 | Solid-electrolyte integrated element, method for manufacturing solid-electrolyte integrated element, and solid-electrolyte element |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61198570A (en) * | 1985-02-28 | 1986-09-02 | Mitsubishi Heavy Ind Ltd | Manufacture of solid electrolyte fuel cell |
| JPS61198569A (en) * | 1985-02-28 | 1986-09-02 | Mitsubishi Heavy Ind Ltd | Manufacturing method of solid electrolyte fuel cell |
-
1987
- 1987-04-03 JP JP62082473A patent/JPS63250065A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61198570A (en) * | 1985-02-28 | 1986-09-02 | Mitsubishi Heavy Ind Ltd | Manufacture of solid electrolyte fuel cell |
| JPS61198569A (en) * | 1985-02-28 | 1986-09-02 | Mitsubishi Heavy Ind Ltd | Manufacturing method of solid electrolyte fuel cell |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0855630A (en) * | 1994-05-09 | 1996-02-27 | Air Prod And Chem Inc | Electrochemical solid state device for ion transport by electrolyte |
| WO2018190205A1 (en) * | 2017-04-10 | 2018-10-18 | 三井金属鉱業株式会社 | Solid-electrolyte integrated element, method for manufacturing solid-electrolyte integrated element, and solid-electrolyte element |
| JP6435442B1 (en) * | 2017-04-10 | 2018-12-05 | 三井金属鉱業株式会社 | Solid electrolyte integrated element, method for manufacturing solid electrolyte integrated element, and solid electrolyte element |
| US11569528B2 (en) | 2017-04-10 | 2023-01-31 | Mitsui Mining & Smelting Co., Ltd. | Solid electrolyte integrated device, method of manufacturing solid electrolyte integrated device, and solid electrolyte element |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3843766B2 (en) | Solid oxide fuel cell | |
| CN101682068B (en) | Composite anode showing low performance loss with time | |
| US6207311B1 (en) | Solid oxide fuel cell operable over wide temperature range | |
| CA2204632A1 (en) | Protective interlayer for high temperature solid electrolyte electrochemical cells | |
| JPH06107462A (en) | Oxygen ion conductor and solid fuel cell | |
| JP2004319492A (en) | Fuel cells and inert supports | |
| Ishihara et al. | Preparation of Yttria-Stabilized Zirconia Films for Solid Oxide Fuel Cells by Electrophoretic Deposition Method. | |
| US20110053045A1 (en) | Solid oxide fuel cell and method of manufacturing the same | |
| JP3358884B2 (en) | Interconnector material | |
| JP3259756B2 (en) | Multilayer solid electrolyte for solid fuel cells | |
| JPH1074528A (en) | Solid oxide fuel cell and method of manufacturing the same | |
| JPS63250065A (en) | Oxygen ion conductive membrane and its manufacturing method | |
| JP3128099B2 (en) | Air electrode material for low temperature operation type solid fuel cell | |
| KR101582975B1 (en) | Bilayer electrolyte for cathode-supported direct cabon fuel cells and manufacturing method of the same | |
| JPH09266000A (en) | Solid oxide fuel cell and method of manufacturing the same | |
| JP2018139182A (en) | Solid electrolyte member, solid oxide fuel cell, water electrolysis device, hydrogen pump, and method for producing solid electrolyte member | |
| US7691770B2 (en) | Electrode structure and methods of making same | |
| JP3351865B2 (en) | Fuel electrode for solid oxide fuel cell and self-standing membrane flat solid electrolyte fuel cell using this fuel electrode | |
| JP2025532526A (en) | electrochemical cell | |
| JP2003331874A (en) | Interconnector for solid oxide fuel cell and method of forming the same | |
| KR20230087170A (en) | Sintering method of proton ceramic fuel cell electrolyte and proton ceramic fuel cell manufactured using the same | |
| JP2018139180A (en) | Method for producing solid electrolyte member | |
| JP2870126B2 (en) | Solid oxide fuel cell | |
| JPS63285877A (en) | Solid electrolyte manufacturing method | |
| JPH076774A (en) | Scandia-stabilized zirconia-based solid oxide fuel cell |