JPH031453A - Solid electrolyte fuel cell - Google Patents
Solid electrolyte fuel cellInfo
- Publication number
- JPH031453A JPH031453A JP1134535A JP13453589A JPH031453A JP H031453 A JPH031453 A JP H031453A JP 1134535 A JP1134535 A JP 1134535A JP 13453589 A JP13453589 A JP 13453589A JP H031453 A JPH031453 A JP H031453A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- solid electrolyte
- alpha
- fuel
- baceo3
- 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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
- H01M4/9025—Oxides specially used in fuel cell operating at high temperature, e.g. SOFC
- H01M4/9033—Complex oxides, optionally doped, of the type M1MeO3, M1 being an alkaline earth metal or a rare earth, Me being a metal, e.g. perovskites
-
- 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
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inert Electrodes (AREA)
- Fuel Cell (AREA)
- Conductive Materials (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はBaCe0a系を固体電解質とする高温燃料電
池に係り、とりわけ白金に代る安価で高性能の電極材料
を使用したBaCe0.系固体電解質型燃料電池に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a high-temperature fuel cell using a BaCe0a system as a solid electrolyte, and particularly to a BaCe0. The present invention relates to solid oxide fuel cells.
高温固体電解質燃料電池は活性化分極が殆んどなく、出
力電圧が高い、また出力電流密度が高く、エネルギー変
換効率が高い、さらに低純度の安価な燃料ガスによって
も動作させることができる、排ガスが高温なので次段の
発電に利用できる、などの利点を有し、第三世代の燃料
電池として開発が進められている。なかでも、カルシア
、イツトリアなどで安定化したジルコニアを固体電解質
(酸素イオン導電体)として使用した高温固体電解質燃
料電池が最も盛んに研究開発が進んでいる。High-temperature solid electrolyte fuel cells have almost no activation polarization, have high output voltage, high output current density, and high energy conversion efficiency. Furthermore, they can be operated with low-purity and inexpensive fuel gas, and exhaust gas It has the advantage of being able to be used for the next stage of power generation because of its high temperature, and is currently being developed as a third-generation fuel cell. Among these, high-temperature solid electrolyte fuel cells that use zirconia stabilized with calcia, ittria, etc. as a solid electrolyte (oxygen ion conductor) are the most actively researched and developed.
本発明者らは、ペロブスカイト型酸化物を固体電解質に
用いた高温型燃料電池に関して、研究を進めており、B
aCeO3系およびCaT+[]3系焼結体を固体電解
質とした各種の燃料電池については既に成果を発表して
いる。なかでも、BaCeO3系セラミックスは高温で
比較的高いプロトン−酸化物イオン混合導電性を示し、
安定に機能するので、燃料電池用固体電解質として有望
である。The present inventors have been conducting research on high-temperature fuel cells using perovskite oxides as solid electrolytes, and
Results have already been announced regarding various fuel cells using aCeO3-based and CaT+[]3-based sintered bodies as solid electrolytes. Among them, BaCeO3-based ceramics exhibit relatively high proton-oxide ion mixed conductivity at high temperatures;
Since it functions stably, it is promising as a solid electrolyte for fuel cells.
上記の如(、BaCeO3系セラミックスは高温型燃料
電池の固体電解質材料として優れているが、これまで電
極材として用いられている白金は高価であるので、これ
に代る安価でかつ高性能の電極材が望まれる。As mentioned above, BaCeO3-based ceramics are excellent as solid electrolyte materials for high-temperature fuel cells, but platinum, which has been used as an electrode material so far, is expensive, so we have developed an inexpensive and high-performance electrode to replace it. material is desired.
そこで、本発明はBaCeO3系固体電解質燃料電池に
おいて白金に代る安価で高性能、安定な電極材を提供す
ることを目的とするものである。Therefore, an object of the present invention is to provide an inexpensive, high-performance, and stable electrode material to replace platinum in BaCeO3 solid electrolyte fuel cells.
上記目的を実現するために、本発明は、Raced3系
固体電解系全体電解質温固体電解質型燃料電池において
、燃料極にニッケルを、また酸化剤極にBaをドープし
たLaMnO3を用いることを特徴とする高温燃料電池
を提供する。In order to achieve the above object, the present invention is characterized in that a Raced 3 solid electrolyte overall electrolyte temperature solid electrolyte fuel cell uses LaMnO3 doped with nickel for the fuel electrode and Ba for the oxidizer electrode. Provides high temperature fuel cells.
電極材として白金を使用することを排除するために、燃
料極にニッケルを、そして酸化剤極に8aドープしたL
aMnO3を用いることが好ましいが、燃料極にニッケ
ルを使用し、酸化剤極には白金を使用したり、逆に酸化
剤極にBaドープしたLaMnO3を使用し、燃料極に
は白金を使用した場合にも、電極材としての白金の使用
量を半減する効果があり、これらの場合も本発明の範囲
内にある。In order to eliminate the use of platinum as an electrode material, L was doped with nickel in the fuel electrode and 8a in the oxidizer electrode.
It is preferable to use aMnO3, but if nickel is used for the fuel electrode and platinum is used for the oxidizer electrode, or conversely, Ba-doped LaMnO3 is used for the oxidizer electrode and platinum is used for the fuel electrode. This also has the effect of halving the amount of platinum used as an electrode material, and these cases are also within the scope of the present invention.
本発明で固体電解質として用いるBaCe0.、系セラ
ミックスはBaCeO3をベースとして、これにNd
、 LaまたはYを5〜15%程度含む組成りaCe+
−JxO3−&(式中、MはNd、LaまたはYであり
、0≦xく0.15、αは0〜0.075)を有するも
のである。このようなりaCeO,系セラミックスは公
知の5rCe03系高温型プロトン導電性セラミツクス
にくらべて更に高いプロトン導電性を有し、かつ800
℃以上の高温では酸化物イオン混合導電性を示すので、
燃料電池用固体電解質として優れている。好ましいもの
はBaCeo、 9NdO,+03−”およびBaCe
o−sYo、 +03−txで、特に後者は1000℃
で7 XIO” Scm−’という、現存の高温型プロ
トン導電性酸化物で最高の導電率を示す。BaCe0. used as a solid electrolyte in the present invention. , based ceramics are based on BaCeO3 and Nd
, composition aCe+ containing about 5 to 15% La or Y
-JxO3-& (where M is Nd, La or Y, 0≦x0.15, and α is 0 to 0.075). As such, aCeO, based ceramics have higher proton conductivity than known 5rCe03 based high temperature proton conductive ceramics, and
At high temperatures above ℃, it exhibits oxide ion mixed conductivity, so
Excellent as a solid electrolyte for fuel cells. Preferred are BaCeo, 9NdO,+03-” and BaCe
o-sYo, +03-tx, especially the latter at 1000℃
It exhibits the highest conductivity of the existing high-temperature proton conductive oxides at 7 XIO''Scm-'.
本発明で燃料極としてニッケルを用いると電圧と出力電
流密度とが直線関係を示し、作動特性が安定している。When nickel is used as the fuel electrode in the present invention, the voltage and output current density show a linear relationship, and the operating characteristics are stable.
白金燃料極を用いた電池よりも取出しうる出力電流は低
下するが、作動特性が安定しており、しかも、燃料ガス
拡散の容易な微細構造にすることによって、出力電流が
向上することも見い出されており、かつ安価な材料であ
るので、白金の代替材料として優れている。Although the output current that can be extracted is lower than that of a battery using a platinum fuel electrode, it has been found that the operating characteristics are stable, and that the output current can be improved by creating a microstructure that facilitates fuel gas diffusion. It is an excellent material as an alternative to platinum because it is a low-cost material.
本発明で酸化剤極としてBaをドープしたLaMnO3
を用いるのは、ペロブスカイト型結晶構造を有する、B
aCe0.系固体電解質とのなじみがよく、電極材抵抗
、分極抵抗とも低く、良好な性能を示す。LaMnO3 doped with Ba as an oxidant electrode in the present invention
is used for B, which has a perovskite crystal structure.
aCe0. It has good compatibility with solid electrolytes, has low electrode material resistance and low polarization resistance, and exhibits good performance.
BaをドープしたLaMn[l、の組成はLa、 xB
aJn03m(o<x<0.15、好ましくは0.05
< x < 0.10.0.025 < a < 0
.05)で表わされ、Lao−5Bao、 JnO3−
&が性能上特に好ましい。The composition of LaMn[l, doped with Ba is La, xB
aJn03m (o<x<0.15, preferably 0.05
< x < 0.10.0.025 < a < 0
.. 05), Lao-5Bao, JnO3-
& is particularly preferable in terms of performance.
本発明の高温型固体電解質燃料電池の構成は、電極材と
して特定の材料を用いる意思外は特に限定されず、常法
に従うことができる(例、特願昭63−96757号明
細書)。また、燃料(水素、−酸化炭素、炭化水素など
)、酸化剤(純酸素、空気)も一般的なものが使用され
る。The structure of the high-temperature solid electrolyte fuel cell of the present invention is not particularly limited, except that a specific material is used as the electrode material, and conventional methods can be followed (eg, Japanese Patent Application No. 1983-96757). Also, common fuels (hydrogen, carbon oxide, hydrocarbons, etc.) and oxidizers (pure oxygen, air) are used.
NiはBaCe0.系電解質と固体間反応を起さず、メ
タン等を燃料とすると触媒効果が期待できる。Baドー
プしalnQ3は電解質のBaCeO3と同じペロブス
カイト型酸化物でかつ双方ともBaを含むのでなじみが
よく、また電子導電率が高い。従って、これらは13a
ce03系電解質燃料電池の電極材として優れている。Ni is BaCe0. A catalytic effect can be expected if methane or the like is used as a fuel without causing a solid-state reaction with the system electrolyte. Ba-doped AlnQ3 is a perovskite-type oxide similar to the electrolyte BaCeO3, and both contain Ba, so it is compatible and has high electronic conductivity. Therefore, these are 13a
Excellent as an electrode material for CE03 electrolyte fuel cells.
実施例l
CeO2,Ban、 Nd2O3の各粉末を15.3
:15.5 :3.36の比率(重量比)で混合し、空
気中1300℃で10時間焼成したのち微粉砕し、2t
/cnの静水圧で加圧成形後、空気中1500℃で10
時間焼成して緻密な焼結体を得た。これを直径12mm
厚さ約0゜5m市の円盤状に切出し、表面をよく研磨し
て電解質ディスクとした。このディスクの一面に白金ペ
ースト、他面にニッケルペーストを塗り、焼き付けてそ
れぞれ空気極及び燃料極とした。電極材の厚みはそれぞ
れ50I!raであった。これをガラスガスケットを介
してアルミナ磁製管ではさみ、両極室を分離した。加熱
によってガラスガスケットは半融状態となり、燃料およ
び空気の外部への漏れを防止する。Example 1 CeO2, Ban, Nd2O3 powder at 15.3
:15.5 :3.36 ratio (weight ratio), calcined in air at 1300℃ for 10 hours, and then finely ground to produce 2 tons.
/cn hydrostatic pressure, then molded in air at 1500℃ for 10
A dense sintered body was obtained by firing for several hours. This is 12mm in diameter
It was cut out into a disk shape with a thickness of approximately 0.5 m, and the surface was thoroughly polished to obtain an electrolyte disk. One side of this disk was coated with platinum paste, and the other side was coated with nickel paste, and baked to form an air electrode and a fuel electrode, respectively. The thickness of each electrode material is 50I! It was ra. This was sandwiched between alumina porcelain tubes via a glass gasket to separate the two polar chambers. When heated, the glass gasket becomes semi-molten, preventing fuel and air from leaking to the outside.
燃料として水素、酸化剤として空気をそれぞれの電極室
に導入すると約0.95Vの安定な電圧が生じ負荷を連
結することにより定常的な電流を取出すことができた。When hydrogen as a fuel and air as an oxidizer were introduced into each electrode chamber, a stable voltage of about 0.95V was generated, and a steady current could be obtained by connecting the load.
第1図に、この燃料電池の性能を示す。第1図から、こ
の燃料電池が800〜1000℃において端子電圧と出
力電流密度の間に直線関係があることが認められる。な
お、この電池では白金燃料極を用いた電池(第1図の破
線)よりも取り出しうる出力電流は低下したが、その低
下はわずかであり、かつ作動特性は安定である。本電池
の電解質厚さは約500J!Iaでその最大出力は約0
.11W/Cnであるが、この厚さを現在開発が進めら
れているジルコニア系電池並みの50〜100Jaにす
れば電極での分極を考慮しても最大出力0.3〜0.7
W/c++fが期待できる。Figure 1 shows the performance of this fuel cell. From FIG. 1, it is recognized that in this fuel cell, there is a linear relationship between the terminal voltage and the output current density at 800 to 1000°C. Although the output current that can be extracted from this battery was lower than that of a battery using a platinum fuel electrode (dashed line in FIG. 1), the decrease was slight and the operating characteristics were stable. The electrolyte thickness of this battery is approximately 500J! Ia and its maximum output is about 0
.. 11W/Cn, but if this thickness is made 50 to 100 Ja, which is comparable to the zirconia batteries currently being developed, the maximum output will be 0.3 to 0.7 even considering polarization at the electrodes.
W/c++f can be expected.
次に、同じセルに燃料ガスとしてメタンを水蒸気(濃度
13〜30%)とともに導入した。この電池の燃料極側
の排ガスをガスクロにより分析したところ、1000℃
では、H2約33%、CD約10%であり、他に数%の
CO2とメタンのカップリング反応による微量のC2H
,、C2116を含んでいた。この組成は、白金燃料極
でのそれとほとんど同じであった。Next, methane was introduced into the same cell as a fuel gas together with water vapor (concentration 13-30%). When the exhaust gas on the fuel electrode side of this cell was analyzed by gas chromatography, it was found that the temperature was 1000℃.
In this case, H2 is about 33%, CD is about 10%, and there is also a trace amount of C2H due to the coupling reaction of several percent of CO2 and methane.
,,C2116 was included. This composition was almost the same as that of the platinum anode.
すなわち、この試験電池では燃料極材の種類によらず、
H2とCDの比がほぼ3であることから、次式のメタン
の水蒸気改質反応
CH4+H20→3H2+CO
が、主反応であると考えられた。In other words, in this test cell, regardless of the type of fuel electrode material,
Since the ratio of H2 and CD was approximately 3, it was thought that the main reaction was the steam reforming reaction of methane CH4+H20→3H2+CO of the following formula.
第2図にこの電池の作動特性を示した。この電池では、
燃料に水素を用いた電池よりも短絡電流は減少したが、
作動特性は安定であった。Figure 2 shows the operating characteristics of this battery. With this battery,
Although the short-circuit current was lower than that of batteries using hydrogen as fuel,
The operating characteristics were stable.
次に、このような型の燃料電池の性能を評価する目的で
、ニッケル電極材の電極反応抵抗及び電極材抵抗(電解
質との接触抵抗)を計算したところ、それぞれ0.23
〜0.37ΩcrAと0.11〜0.21ΩC[+!で
あり、十分に実用に供しうる値であった。Next, in order to evaluate the performance of this type of fuel cell, we calculated the electrode reaction resistance and electrode material resistance (contact resistance with electrolyte) of the nickel electrode material, and found that they were each 0.23.
~0.37ΩcrA and 0.11~0.21ΩC[+! This value was sufficient for practical use.
上記の実験に用いたニッケル燃料極と白金燃料極のSE
M写真を撮映したところ、白金電極では数μの大きさの
細孔が数多く均一に分布していたが、ニッケルの粒子は
比較的大きく島状に分布し、現時点では有効反応面積が
かなり小さいことがうかがえた。従って、このような微
細構造に留意して電極を取り付ければ、ニッケルを用い
た電池の性能をさらに向上できると考えられる。SE of the nickel fuel electrode and platinum fuel electrode used in the above experiment
When the M photo was taken, it was found that the platinum electrode had many pores with a size of several microns uniformly distributed, but the nickel particles were relatively large and distributed in the form of islands, and the effective reaction area was currently quite small. That seems to be the case. Therefore, if electrodes are attached with such microstructure in mind, it is thought that the performance of batteries using nickel can be further improved.
実施例2
実施例1と同様にしてBaCeo、 5oNdo、+o
Os−*固体電解質燃料電池を作製した。但し燃料極に
は白金を用い、空気極には各種の導電性酸化物を用いた
。具体的には、空気極としてSrをドープしたLaMn
O3とLaCoTo、及びBaをドープしたしalJn
03とLaCoO3を用い、これらをBaCeo、 5
oNdo、 1003−&固体電解質ディスクの空気極
側にして燃料電池を形成した。Example 2 BaCeo, 5oNdo, +o in the same manner as Example 1
An Os-* solid electrolyte fuel cell was fabricated. However, platinum was used for the fuel electrode, and various conductive oxides were used for the air electrode. Specifically, Sr-doped LaMn was used as the air electrode.
AlJn doped with O3, LaCoTo, and Ba
03 and LaCoO3, and convert them into BaCeo, 5
oNdo, 1003-& A fuel cell was formed with the air electrode side of the solid electrolyte disk.
次に、実施例1と同様の条件下で、燃料として水素、酸
化剤として空気を用いて、電池の作動試験を行なった。Next, an operation test of the cell was conducted under the same conditions as in Example 1, using hydrogen as the fuel and air as the oxidizing agent.
そして、実施例1の場合と同様にして、電極材抵抗と分
極抵抗を求めた。結果を下記表に示す。Then, in the same manner as in Example 1, the electrode material resistance and polarization resistance were determined. The results are shown in the table below.
羞
水素−空気燃料電池における抵抗(空気極側)操作温度
1000℃
表に見られるように、Srをドープした系(LaMnO
,系、1aco03系とも)では電極材抵抗、分極抵抗
ともに高く、電解質とのなじみも悪い。しかしながら、
電解質の構成成分であるBaをドープしたLaMnOs
を用いた場合には、電解質とのなじみがよくなり、とく
にBaを40%ドープしたものは電極材抵抗、分極抵抗
ともに良好な性能を示した。Resistance (air electrode side) operating temperature in hydrogen-air fuel cell: 1000°C As shown in the table, Sr-doped system (LaMnO
, and 1aco03 series), both the electrode material resistance and polarization resistance are high, and the compatibility with the electrolyte is poor. however,
LaMnOs doped with Ba, which is a component of the electrolyte
In the case of using B, the compatibility with the electrolyte was improved, and in particular, the one doped with 40% Ba showed good performance in both electrode material resistance and polarization resistance.
第3図に、Baを40%ドープしたLaMnO3を空気
極材として用いた燃料電池の作動特性を示す。FIG. 3 shows the operating characteristics of a fuel cell using LaMnO3 doped with 40% Ba as the air electrode material.
以上の通り、BaCeO3系固体電解質燃料電池におい
て燃料極としてN11酸化剤極としてBaをドープした
LaMnO3を用いると、作動特性が優れかつ安定した
燃料電池が得られる。いずれも白金の場合よりは特性が
いくらか劣るが、ニッケル極では燃料ガス拡散の容易な
微細構造、BaドープLaMn0.極では電解質とのな
じみのよい有効反応面積の高い構造になるようにするこ
とによって、さらに特性が向上し、高価な白金の代替材
料としての価値はさらに向上する。As described above, when Ba-doped LaMnO3 is used as the fuel electrode and the N11 oxidizer electrode in a BaCeO3-based solid electrolyte fuel cell, a stable fuel cell with excellent operating characteristics can be obtained. Both properties are somewhat inferior to those of platinum, but the nickel electrode has a fine structure that facilitates fuel gas diffusion, and Ba-doped LaMn0. By making the electrode have a structure with a high effective reaction area that is compatible with the electrolyte, the properties will be further improved, and its value as an alternative material to expensive platinum will be further improved.
本発明によれば、白金に代わって、安定で優れた電池作
動特性を有する電極材を使用したBaCe0゜系固体電
解質燃料電池が提供される。According to the present invention, a BaCe 0° solid electrolyte fuel cell is provided that uses an electrode material having stable and excellent cell operating characteristics in place of platinum.
第1〜3図は本発明による各種固体電解質型燃料電池の
作動特性を示すグラフ図である。
電流密度
[mA 7cm2]
電流密度[mA/cm21
第2回1 to 3 are graphs showing the operating characteristics of various solid oxide fuel cells according to the present invention. Current density [mA 7cm2] Current density [mA/cm21 2nd
Claims (1)
にニッケルを用いたことを特徴とする固体電解質型燃料
電池。 2、BaCeO_3系電解質を固体電解質とし、酸化剤
極にBaをドープしたLaMnO_3を用いたことを特
徴とする固体電解質型燃料電池。[Claims] 1. A solid electrolyte fuel cell characterized in that a BaCeO_3-based electrolyte is used as a solid electrolyte and nickel is used for the fuel electrode. 2. A solid electrolyte fuel cell characterized in that a BaCeO_3-based electrolyte is used as a solid electrolyte and Ba-doped LaMnO_3 is used as an oxidizer electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1134535A JPH031453A (en) | 1989-05-30 | 1989-05-30 | Solid electrolyte fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1134535A JPH031453A (en) | 1989-05-30 | 1989-05-30 | Solid electrolyte fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH031453A true JPH031453A (en) | 1991-01-08 |
Family
ID=15130590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1134535A Pending JPH031453A (en) | 1989-05-30 | 1989-05-30 | Solid electrolyte fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH031453A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5158020A (en) * | 1991-05-10 | 1992-10-27 | Zygmunt Alexander Kunczynski | Drive shoe assembly with resiliently flexible traction members and method |
| WO2002063709A1 (en) * | 2001-02-07 | 2002-08-15 | Forschungszentrum Jülich GmbH | Proton conductor for high-temperature fuel cells |
| WO2005001980A1 (en) * | 2003-06-30 | 2005-01-06 | Japan Energy Corporation | Fuel cell with reformer |
| CN106007714A (en) * | 2016-05-17 | 2016-10-12 | 东北大学 | Solid electrolyte for hydrogen probe in aluminum and aluminum alloy melt and preparation method |
-
1989
- 1989-05-30 JP JP1134535A patent/JPH031453A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5158020A (en) * | 1991-05-10 | 1992-10-27 | Zygmunt Alexander Kunczynski | Drive shoe assembly with resiliently flexible traction members and method |
| WO2002063709A1 (en) * | 2001-02-07 | 2002-08-15 | Forschungszentrum Jülich GmbH | Proton conductor for high-temperature fuel cells |
| WO2005001980A1 (en) * | 2003-06-30 | 2005-01-06 | Japan Energy Corporation | Fuel cell with reformer |
| CN106007714A (en) * | 2016-05-17 | 2016-10-12 | 东北大学 | Solid electrolyte for hydrogen probe in aluminum and aluminum alloy melt and preparation method |
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