[go: up one dir, main page]

DE4119498A1 - Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing - Google Patents

Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing

Info

Publication number
DE4119498A1
DE4119498A1 DE4119498A DE4119498A DE4119498A1 DE 4119498 A1 DE4119498 A1 DE 4119498A1 DE 4119498 A DE4119498 A DE 4119498A DE 4119498 A DE4119498 A DE 4119498A DE 4119498 A1 DE4119498 A1 DE 4119498A1
Authority
DE
Germany
Prior art keywords
layer
firing
paste
electrode
thin layer
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.)
Ceased
Application number
DE4119498A
Other languages
German (de)
Inventor
Heinz Dr Stadelmann
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ABB Patent GmbH
Original Assignee
ABB Patent GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ABB Patent GmbH filed Critical ABB Patent GmbH
Priority to DE4119498A priority Critical patent/DE4119498A1/en
Publication of DE4119498A1 publication Critical patent/DE4119498A1/en
Ceased legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9016Oxides, hydroxides or oxygenated metallic salts
    • H01M4/9025Oxides specially used in fuel cell operating at high temperature, e.g. SOFC
    • H01M4/9033Complex oxides, optionally doped, of the type M1MeO3, M1 being an alkaline earth metal or a rare earth, Me being a metal, e.g. perovskites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M1/00Inking and printing with a printer's forme
    • B41M1/12Stencil printing; Silk-screen printing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M3/00Printing processes to produce particular kinds of printed work, e.g. patterns
    • 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
    • Y02E60/50Fuel cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inert Electrodes (AREA)
  • Fuel Cell (AREA)

Abstract

A fuel cell air electrode consists of a ceramic electrolyte. The mfg. process is as follows: a paste is formed by making a screen printing paste using a perowskite material of the compsn. La1-xM1xM2O3 in which M1 is Ca and/or Sr; M2 is Mn, Ni, Cr and/or Co which has been made by a wet chemical or a spray pyrolysis process. This is mixed with terpineol, a binder, a plasticiser and a dispersing agent. A thin layer, e.g., 30 microns thick, is deposited on the unsintered, not sandblasted ceramic electrolyte part and the electrode fired at 1400 deg.C. Esp. claimed is the use of La0.84Sr0.16MnO3. The solvent mixt. pref. contains terpineol, ethocel 10, triolein and dibutylphthalate. USE/ADVANTAGE - The electrode layer is thin, about 10 microns after firing, avoiding the pore blockage. There are extensive 3-phase boundaries present which allow for efficient electrochemical reaction. The conductivity of the layer is very good, i.e., about 225 Scm(-1) at 1000 deg.C., resulting in good current carrying capability. The material sinters very well, giving a strongly adhering layer.

Description

Die Erfindung bezieht sich auf ein Verfahren zur Her­ stellung einer Brennstoffzellen-Luftelektrode auf einem keramischen Elektrolyten.The invention relates to a method for Her position of a fuel cell air electrode on a ceramic electrolyte.

Hochtemperaturbrennstoffzellen mit Festelektrolyten sind beispielsweise in der DE-OS 39 07 485 beschrieben. Sol­ che Hochtemperaturbrennstoffzellen weisen auf einer der Hauptflächen eines keramischen Elektrolyten eine soge­ nannte Luftelektrode auf. Diese Elektrode muß einerseits ausreichend porös und dünn sein, um einen möglichst un­ gehemmten Sauerstofftransport zu gewährleistet, anderer­ seits muß sie ein guter elektrischer Leiter sein, um re­ lativ hohe Ströme führen zu können. High temperature fuel cells with solid electrolytes are described for example in DE-OS 39 07 485. Sol che high-temperature fuel cells point to one of the Main surfaces of a ceramic electrolyte a so-called called air electrode. This electrode must on the one hand be sufficiently porous and thin to be as un as possible inhibited oxygen transport to ensure others on the one hand, it must be a good electrical conductor in order to to be able to carry relatively high currents.  

In der DE-OS 39 07 485 ist in Spalte 4, Zeile 32 bis 35 beschrieben, daß die als Luftelektrode ausgeführte Ka­ thode durch Plasmaspritzen oder Siebdruck auf den Elek­ trolyten aufgebracht werden kann, wobei eine Schichtdicke von 0,2 bis 1 mm angegeben ist. Diese Schichten werden bisher mit über Festkörperreaktionen hergestellte Pulver aus LaSrMnO3 hergestellt. Solche über Festkörperreaktio­ nen hergestellte Pulver zeigen eine im Vergleich zum Einkristall sehr geringe Leitfähigkeit. Dies ist vor al­ lem auf das mäßige Sinterverhalten, d. h. schlechten Schichtzusammenhalt bzw. Inhomogenitäten in der Schicht zurückzuführen. Um diese Nachteile auszugleichen, wurden bisher über Plasmaspritzen mehr als 100 µm dicke Schich­ ten auf zuvor sandgestrahlten Elektrolytscheiben aufge­ bracht. Um eine befriedigende Haftung zu erzielen, wurde sehr energiereich gespritzt. Dies führt zum teilweisen Verschluß der Poren und dadurch zu einer Hemmung des Sauerstofftransports und somit zu einer kinetischen Hem­ mung der Brennstoffzellen-Reaktion.In DE-OS 39 07 485 in column 4, lines 32 to 35 it is described that the air electrode designed as a method can be applied to the electrolyte by plasma spraying or screen printing, a layer thickness of 0.2 to 1 mm being indicated . Until now, these layers have been produced using powder made from LaSrMnO 3 by means of solid-state reactions. Such powders produced via solid-state reactions show a very low conductivity compared to single crystals. This is mainly due to the moderate sintering behavior, ie poor layer cohesion or inhomogeneities in the layer. In order to compensate for these disadvantages, more than 100 µm thick layers have previously been applied to previously sandblasted electrolyte discs by means of plasma spraying. In order to achieve satisfactory adhesion, very high-energy spraying was used. This leads to the partial closure of the pores and thereby to an inhibition of oxygen transport and thus to a kinetic inhibition of the fuel cell reaction.

Davon ausgehend liegt der Erfindung die Aufgabe zugrun­ de, ein verbessertes Verfahren zur Herstellung einer Brennstoffzellen-Luftelektrode auf einem keramischen Elektrolyten anzugeben.Proceeding from this, the invention is based on the object de, an improved method of making a Fuel cell air electrode on a ceramic Specify electrolytes.

Diese Aufgabe wird durch ein Verfahren gelöst zur Her­ stellung einer Brennstoffzellen-Luftelektrode auf einem keramischen Elektrolyten, das nachstehende Verfahrens­ schritte aufweist:This problem is solved by a method for the manufacture position of a fuel cell air electrode on a ceramic electrolyte, the procedure below steps:

  • a) Anrühren einer Siebdruckpaste aus einem naßchemisch z. B. durch Spraypyrolyse hergestellten Perowskit des Typs La1-xMx¹M²O₃(Mx¹=Ca, Sr; M²=Mn, Ni, Cr, Co) unter Zusatz von Terpineol, einem Binder, einem Plastifizierer und einer Dispergierhilfe, a) stirring a screen printing paste from a wet chemical z. B. perovskite of the type La 1-x M x ¹M²O₃ (M x ¹ = Ca, Sr; M² = Mn, Ni, Cr, Co) prepared by spray pyrolysis with the addition of terpineol, a binder, a plasticizer and a dispersing aid,
  • b) Aufbringen einer dünnen, z. B. 30 µm dicken Schicht der Paste auf eine gesinterte, nicht sandgestrahlte Elektrolytscheibe, undb) applying a thin, e.g. B. 30 micron thick layer the paste onto a sintered, not sandblasted Electrolyte disc, and
  • c) Einbrennen der Schicht bei etwa 1400°C.c) baking the layer at about 1400 ° C.

Mit dem erfindungsgemäßen Verfahren hergestellte Luft­ elektrodenschichten zeigen eine Reihe von Vorteilen. Die erfindungsgemaß hergestellte und verwendete Siebdruckpa­ ste ist sehr sinteraktiv und führt bei relativ niedriger Sintertemperatur zu einer extrem gut haftenden Schicht. Es ist keine Vorbehandlung der Unterlage durch Sand­ strahlen erforderlich. Mit einem Rasterelektronen-Mikro­ skop angefertigte Schliffbilder lassen selbst bei 2000facher Vergrößerung keine Korngrenzen erkennen. Dies läßt darauf schließen, daß eine merkliche Ausbil­ dung von Verunreinigungen enthaltenden Korngrenzen unter­ blieben ist. Eine solche, als Zeichnung beigefügte Auf­ nahme zeigt eine für einen hinreichenden Sauerstoff­ transport benötigte Porösität von etwa 50%. Außerdem zeigt die REM-Aufnahme die Ausbildung ausgedehnter, für die elektrochemische Umsetzung wesentlicher 3-Phasen­ grenzen.Air produced with the method according to the invention Electrode layers show a number of advantages. The Screen printing pa produced and used according to the invention ste is very sinter active and performs at relatively low Sintering temperature to an extremely well adhering layer. It is not pretreatment of the surface with sand blasting required. With a scanning electron micro Skop-made micrographs allow themselves 2000 times magnification no grain boundaries detect. This suggests that a noticeable training grain boundaries remained. One such, attached as a drawing Acceptance shows one for sufficient oxygen transport required porosity of about 50%. Furthermore the REM image shows the training for extended the electrochemical implementation of essential 3 phases limit.

Ein anderer Vorteil ist darin zu sehen, daß für die sehr dünnen Elektrodenschichten nur eine kleine Materialmenge erforderlich ist.Another advantage is that for the very thin electrode layers only a small amount of material is required.

Die elektrische Leitfähigkeit der nach dem erfindungsge­ mäßen Verfahren hergestellten Schicht ist besonders gut. In Versuchen wurde bei einer Betriebstemperatur von 1000°C eine Leitfähigkeit von 225 Scm-1 gemessen.The electrical conductivity of the layer produced by the method according to the invention is particularly good. In experiments, a conductivity of 225 Scm -1 was measured at an operating temperature of 1000 ° C.

Nachstehend wird ein Ausführungsbeispiel für das erfin­ dungsgemäße Verfahren beschrieben. An embodiment of the invention is described below described method according to the invention.  

In dem Ausführungsbeispiel wurde ein Perowskit-Pulver aus La0,84Sr0,16MnO₃ der Firma Merck verwendet, das durch Spraypyrolyse hergestellt wurde. Dieses Pulver ist aufgrund seiner Feinheit extrem sinteraktiv. Wegen sei­ ner hohen Reinheit wird eine Ausbildung von Korngrenzen mit hohen Widerständen nicht beobachtet. Aufgrund der hohen Homogenität des Ausgangspulvers sind die Bulk-Ei­ genschaften (Leitfähigkeit, Zusammensetzung etc.) über die komplette Elektrode sehr einheitlich. Das Pulver wurde mit Terpineol, Ethocel 10 der Fa. Dow Chemicals als Binder, Triolein als Plastifizierer und Dibutylphtha­ lat als Dispergierhilfe zu einer Siebdruckpaste ange­ rührt. Der Feststoffgehalt lag idealerweise bei 65%, er kann aber auch nach oben bis etwa 80% und nach unten bis etwa 55% variiert werden.In the exemplary embodiment, a perovskite powder made of La 0.84 Sr 0.16 MnO₃ from Merck was used, which was produced by spray pyrolysis. This powder is extremely sinter-active due to its fineness. Because of its high purity, the formation of grain boundaries with high resistances is not observed. Due to the high homogeneity of the starting powder, the bulk properties (conductivity, composition, etc.) are very uniform across the entire electrode. The powder was mixed with terpineol, Ethocel 10 from Dow Chemicals as a binder, triolein as a plasticizer and dibutyl phthalate as a dispersing aid to form a screen printing paste. The solids content was ideally 65%, but it can also be varied up to about 80% and down to about 55%.

Die so hergestellte Paste wurde dann auf eine gesinter­ te, nicht sandgestrahlte Elektrolytscheibe mit einer Dicke von etwa 30 µm im grünen Zustand aufgetragen und bei 1400°C eingebrannt. Es wurde eine etwa 10 µm dicke, gut haftende Schicht erzielt.The paste thus produced was then sintered te, not sandblasted electrolyte disc with a Thickness of about 30 microns applied in the green state and Baked at 1400 ° C. It was about 10 microns thick well adhering layer achieved.

Da die Schicht eine hohe elektrische Leitfähigkeit auf­ weist, kann sie z. B. als stromführende Schicht einer im Sinne der Patentanmeldung P 41 04 838.5 zweigeteilten Luftelektrode verwendet werden.Because the layer has high electrical conductivity points, it can e.g. B. as a current-carrying layer in In terms of patent application P 41 04 838.5 two-part Air electrode can be used.

Claims (3)

1. Verfahren zur Herstellung einer Brennstoffzel­ len-Luftelektrode auf einem keramischen Elektrolyten, gekennzeichnet durch nachstehende Verfahrensschritte:
  • a) Anrühren einer Siebdruckpaste aus einem naßchemisch z. B. durch Spraypyrolyse hergestellten Perowskit des Typs La1-xMx¹M²O₃(Mx¹=Ca, Sr; M²=Mn, Ni, Cr, Co) unter Zusatz von Terpineol, einem Binder, einem Plastifizierer und einer Dispergierhilfe,
  • b) Aufbringen einer dünnen, z. B. 30 µm dicken Schicht der Paste auf eine gesinterte, nicht sandgestrahlte Elektrolytscheibe, und
  • c) Einbrennen der Schicht bei etwa 1400°C.
1. A process for producing a fuel cell air electrode on a ceramic electrolyte, characterized by the following process steps:
  • a) stirring a screen printing paste from a wet chemical z. B. perovskite of the type La 1-x M x ¹M²O₃ (M x ¹ = Ca, Sr; M² = Mn, Ni, Cr, Co) prepared by spray pyrolysis with the addition of terpineol, a binder, a plasticizer and a dispersing aid,
  • b) applying a thin, e.g. B. 30 micron thick layer of paste on a sintered, not sandblasted electrolyte disc, and
  • c) baking the layer at about 1400 ° C.
2. Verfahren nach Anspruch 1, dadurch gekennzeich­ net, daß zur Herstellung der Siebdruckpaste das Perow­ skitpulver La0,84Sr0,16MnO₃ verwendet wird.2. The method according to claim 1, characterized in that the Perow skit powder La 0.84 Sr 0.16 MnO₃ is used to produce the screen printing paste. 3. Verfahren nach Anspruch 1 oder 2, dadurch ge­ kennzeichnet, daß die organischen Zusätze außer Terpine­ ol Ethocel 10, Triolein und Dibutylphthalat enthalten.3. The method according to claim 1 or 2, characterized ge indicates that the organic additives except terpine ol ethocel 10, triolein and dibutyl phthalate.
DE4119498A 1991-06-13 1991-06-13 Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing Ceased DE4119498A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE4119498A DE4119498A1 (en) 1991-06-13 1991-06-13 Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE4119498A DE4119498A1 (en) 1991-06-13 1991-06-13 Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing

Publications (1)

Publication Number Publication Date
DE4119498A1 true DE4119498A1 (en) 1992-12-17

Family

ID=6433857

Family Applications (1)

Application Number Title Priority Date Filing Date
DE4119498A Ceased DE4119498A1 (en) 1991-06-13 1991-06-13 Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing

Country Status (1)

Country Link
DE (1) DE4119498A1 (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4439533A1 (en) * 1994-06-02 1995-12-07 Rolf Dipl Phys Weidemann Electronic image digitaliser as individual module of modular image processing system or as component of integrated colour copier
EP0803134A1 (en) * 1995-01-13 1997-10-29 The University Of Houston Fabrication of superconducting wires and rods
DE19718849A1 (en) * 1997-05-03 1998-11-12 Forschungszentrum Juelich Gmbh Agglomerate-free fine perovskite powder suspension
DE19746504A1 (en) * 1997-10-22 1999-04-29 Lwk Plasmaceramic Internationa Procedure for making ceramic workpieces, especially for insulating frames for high-temperature fuel cells
US7347887B2 (en) 2003-12-22 2008-03-25 The Boc Group, Inc. Oxygen sorbent compositions and methods of using same
WO2008133549A1 (en) * 2007-04-27 2008-11-06 Obschestvo S Ogranichennoi Otvetstvennost'yu 'natsional'naya Innovatsionnaya Kompaniya 'novye Energeticheskie Proekty' Cathode material for solid oxide fuel cells based on cobalt-containing perovskite-like oxides of transition metals
US7592090B2 (en) 2003-04-28 2009-09-22 Nextech Materials, Ltd. Perovskite electrodes and method of making the same
CN102616035A (en) * 2012-04-06 2012-08-01 浙江晶科能源有限公司 Method for improving printability of electronic paste
US9905883B2 (en) 2013-03-28 2018-02-27 Corning Incorporated Ceramic electrolyte material comprising a modified polycrystalline lithium metal phosphate
US10320019B2 (en) 2006-07-07 2019-06-11 Plansee Se Process for producing a solid oxide fuel cell by depositing an electrically conductive and gas permeable layer on a porous support substrate
CN112726234A (en) * 2020-12-28 2021-04-30 武汉纺织大学 Organic perovskite thickener for cotton fabric vat dye printing and preparation method and application thereof
CN114441619A (en) * 2022-01-28 2022-05-06 安徽大学 Electrode substrate of solid electrochemical gas sensor and sensor manufacturing method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2614728A1 (en) * 1976-04-06 1977-10-20 Bbc Brown Boveri & Cie COMPONENT FOR AN ELECTROCHEMICAL BATTERY
DE2920268A1 (en) * 1978-05-18 1979-11-22 Nissan Motor PASTE FOR THE PRODUCTION OF SOLID ELECTROLYTES
DE2824408B2 (en) * 1978-06-03 1981-04-09 Dornier System Gmbh, 7990 Friedrichshafen Use of mixed oxides with a perovskite structure based on LaMnO 3, LaNiO 3 or LaCoO? 3? and processes for producing the mixed oxides
EP0387643A1 (en) * 1989-03-08 1990-09-19 Asea Brown Boveri Aktiengesellschaft Fuel cell assembly

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2614728A1 (en) * 1976-04-06 1977-10-20 Bbc Brown Boveri & Cie COMPONENT FOR AN ELECTROCHEMICAL BATTERY
DE2920268A1 (en) * 1978-05-18 1979-11-22 Nissan Motor PASTE FOR THE PRODUCTION OF SOLID ELECTROLYTES
DE2824408B2 (en) * 1978-06-03 1981-04-09 Dornier System Gmbh, 7990 Friedrichshafen Use of mixed oxides with a perovskite structure based on LaMnO 3, LaNiO 3 or LaCoO? 3? and processes for producing the mixed oxides
EP0387643A1 (en) * 1989-03-08 1990-09-19 Asea Brown Boveri Aktiengesellschaft Fuel cell assembly

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4439533A1 (en) * 1994-06-02 1995-12-07 Rolf Dipl Phys Weidemann Electronic image digitaliser as individual module of modular image processing system or as component of integrated colour copier
EP0803134A1 (en) * 1995-01-13 1997-10-29 The University Of Houston Fabrication of superconducting wires and rods
DE19718849A1 (en) * 1997-05-03 1998-11-12 Forschungszentrum Juelich Gmbh Agglomerate-free fine perovskite powder suspension
DE19746504A1 (en) * 1997-10-22 1999-04-29 Lwk Plasmaceramic Internationa Procedure for making ceramic workpieces, especially for insulating frames for high-temperature fuel cells
US7592090B2 (en) 2003-04-28 2009-09-22 Nextech Materials, Ltd. Perovskite electrodes and method of making the same
US7347887B2 (en) 2003-12-22 2008-03-25 The Boc Group, Inc. Oxygen sorbent compositions and methods of using same
US10320019B2 (en) 2006-07-07 2019-06-11 Plansee Se Process for producing a solid oxide fuel cell by depositing an electrically conductive and gas permeable layer on a porous support substrate
WO2008133549A1 (en) * 2007-04-27 2008-11-06 Obschestvo S Ogranichennoi Otvetstvennost'yu 'natsional'naya Innovatsionnaya Kompaniya 'novye Energeticheskie Proekty' Cathode material for solid oxide fuel cells based on cobalt-containing perovskite-like oxides of transition metals
CN102616035A (en) * 2012-04-06 2012-08-01 浙江晶科能源有限公司 Method for improving printability of electronic paste
US9905883B2 (en) 2013-03-28 2018-02-27 Corning Incorporated Ceramic electrolyte material comprising a modified polycrystalline lithium metal phosphate
CN112726234A (en) * 2020-12-28 2021-04-30 武汉纺织大学 Organic perovskite thickener for cotton fabric vat dye printing and preparation method and application thereof
CN114441619A (en) * 2022-01-28 2022-05-06 安徽大学 Electrode substrate of solid electrochemical gas sensor and sensor manufacturing method

Similar Documents

Publication Publication Date Title
DE4004172C2 (en) An oxygen sensor for air-fuel mixture control having a protective layer comprising an oxygen occluding substance, and a method of manufacturing the sensor
DE10324396B4 (en) Fuel cell and fuel cell assembly
EP0788175B1 (en) High temperature fuel cell with an electrolyte thin film
EP2676318B1 (en) Layered structure and use thereof to form a ceramic layered structure between an interconnect and a cathode of a high-temperature fuel cell
EP0239771B1 (en) Manufacture of long-lasting oxygen electrodes for electrolysis cells containing a solid electrolyte
DE2837118A1 (en) OXIDE ELECTRODES FOR ELECTROCHEMICAL HIGH TEMPERATURE CELLS
DE19949431A1 (en) Solid oxide fuel cell of cylindrical or flat layered structure has solid electrolyte and air electrode layers or an interlayer of continuously varying perovskite composition
DE19963882A1 (en) Electrode for high temperature fuel cell and method of manufacturing the same
EP2036152A1 (en) Ceramic material combination for an anode of a high-temperature fuel cell
DE4119498A1 (en) Gas electrode for fuel-cell with improved conductivity and porosity - is formed by printing a thin layer of fine-grained perovskite material on the ceramic substrate and then firing
DE60123839T2 (en) STACKED MICROSTRUCTURES OF LEADING, CERAMIC OXIDION MEMBRANES; USE FOR THE SEPARATION OF OXYGEN FROM AIR
DE69108160T2 (en) Fuel electrodes for solid oxide fuel cells and process for their manufacture.
DE102006045086A1 (en) Electrochemical cell structures and process for their preparation
DE102006047823A1 (en) Electrode for a molten carbonate fuel cell and process for its preparation
DE19626342A1 (en) Procedure for making solid electrolyte as thin layer on porous electrode for fuel-cell
DE3131927A1 (en) Process for fabricating a solid-electrolyte oxygen sensor element having a laminar structure, whose external electrode is deposited from the vapour phase
EP2619834B1 (en) Method for producing solid oxide fuel cells having a cathode-electrolyte-anode unit borne by a metal substrate, and use of said solid oxide fuel cells
DE4116734C1 (en)
EP1979078B1 (en) Production method of a proton conducting layer system
EP4198175A2 (en) Supported electrolyte, method for the production thereof and use thereof
EP2210308B1 (en) Functional layer for high-temperature fuel cells and method for production
DE10212966B4 (en) High-temperature fuel cell and method for its production
EP3697944B1 (en) Fuel gas electrode and method for producing a fuel gas electrode
DE19935271C2 (en) Matrix material for fuel cells, process for its production and its use
DE19801440C2 (en) Inexpensive method for producing an electrode-electrolyte unit

Legal Events

Date Code Title Description
OP8 Request for examination as to paragraph 44 patent law
8131 Rejection