WO2016016181A1 - Brennstoffzellenvorrichtung - Google Patents
Brennstoffzellenvorrichtung Download PDFInfo
- Publication number
- WO2016016181A1 WO2016016181A1 PCT/EP2015/067136 EP2015067136W WO2016016181A1 WO 2016016181 A1 WO2016016181 A1 WO 2016016181A1 EP 2015067136 W EP2015067136 W EP 2015067136W WO 2016016181 A1 WO2016016181 A1 WO 2016016181A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel cell
- unit
- layer
- cell device
- interconnector
- Prior art date
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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0236—Glass; Ceramics; Cermets
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
- H01M8/0217—Complex oxides, optionally doped, of the type AMO3, A being an alkaline earth metal or rare earth metal and M 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0241—Composites
- H01M8/0245—Composites in the form of layered or coated products
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
- H01M8/0256—Vias, i.e. connectors passing through the separator material
-
- 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
-
- 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
-
- 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
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- 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
- Y02E60/10—Energy storage using batteries
-
- 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
Definitions
- the invention relates to a fuel cell device according to the preamble of patent claim 1.
- a fuel cell device having a fuel cell unit including a plurality of fuel cells has already been proposed.
- the fuel cells are connected in series by means of a hertkonnektortechnik.
- the I nterkonnektoriser is only formed of a material.
- the invention is based on a fuel cell device with a
- Fuel cell unit which at least two fuel cells and a
- Interconnector unit which is provided, the at least two
- the at least one interconnector unit has at least two layers which are formed from mutually different materials.
- a “fuel cell device” should in particular be a device for stationary and / or mobile extraction, in particular of electrical and / or thermal energy, using at least one
- Fuel cell unit to be understood.
- a "fuel cell unit” is to be understood as meaning, in particular, a unit having a plurality of each other interconnected fuel cells are understood, which is intended to convert at least one chemical energy of at least one fuel gas, in particular hydrogen and / or carbon monoxide, and at least one oxidant, in particular oxygen, in particular into electrical energy.
- the fuel cells are preferably designed as solid oxide fuel cell (SOFC).
- an "interconnector unit” is to be understood as meaning, in particular, a unit which is intended to produce an electrically conductive connection between the at least two fuel cells, in order to connect the at least two fuel cells in series with one another.
- the at least one interconnector unit is formed, in particular, from mutually different materials which are arranged in layers against one another.
- the materials of which the interconnector unit is formed have in particular complementary and / or supplementary functional properties, in particular with regard to a conductivity and / or a sintering behavior.
- the materials of the interconnector unit each have a perovskite structure.
- Fuel cell device can be provided with improved operating characteristics.
- material properties can advantageously be combined by forming the interconnector unit from mutually different materials.
- the interconnector unit can advantageously be adapted to the requirements of a fuel cell device, whereby in particular a functionality and / or lifetime of the fuel cell device can advantageously be increased.
- the interconnector unit has at least one first layer, which is formed by a manganese-based perovskite.
- the interconnector unit preferably has at least one second layer, which is formed by a nickel-based perovskite.
- the nickel-based perovskite has the general chemical formula La Ni x Fei- X 0 3 , with 0.05 ⁇ x ⁇ 0.6.
- Fuel cell device can be advantageously increased. Furthermore, an advantageously high conductivity of the at least one second layer under a cathodic atmosphere can be achieved.
- ohmic losses can thus advantageously be reduced, since an advantageously high conductivity can be achieved both in an anodic and in a cathodic atmosphere.
- the fuel cell unit at least one
- Cathode layer which is provided to cathodes of at least two
- Form fuel cells at least one anode layer, which is intended to form anodes of the at least two fuel cells, and at least one electrolyte layer, which is provided for electrolytes of at least two
- Form fuel cells includes.
- the at least one cathode layer may in particular be composed of lanthanum-strontium-manganese oxide and / or lanthanum-strontium oxide.
- the cathode layer is formed of lanthanum-strontium-manganese oxide, lanthanum-strontium-scandium-manganese oxide, or a mixture thereof.
- the material of the at least one cathode layer has a perovskite structure.
- the at least one anode layer may in particular be formed by a cermet and / or lanthanum-strontium-titanium oxide and / or lanthanum-strontium-scandium-manganese oxide comprising nickel and yttrium-stabilized zirconium oxide.
- the at least one electrolyte layer may in particular be formed from yttrium-stabilized zirconium oxide and / or scandium-stabilized zirconium oxide.
- the at least one electrolyte layer is arranged in particular between the at least one anode layer and the at least one cathode layer.
- the at least one cathode layer in each case forms a cathode of the at least two fuel cells, wherein the cathodes of the at least two fuel cells are preferably separated from one another by an electrical and ionic insulator.
- the at least one anode layer in each case forms an anode of the at least two
- Fuel cells wherein the anodes of the at least two fuel cells preferred example, separated by an electric and ionic insulator. As a result, an advantageous construction of the at least two fuel cells can be achieved. It is further proposed that the at least two fuel cells within the
- Fuel cell unit are arranged such that a cathode of a first
- Fuel cell overlaps an anode of a second fuel cell at least partially. As a result, an advantageously compact design of the fuel cell unit can be achieved.
- the interconnector unit is arranged inside the electrolyte layer of the fuel cell unit.
- the interconnector unit is provided to connect a cathode of a first fuel cell with an anode of a second fuel cell in series.
- Interconnector unit is in particular arranged such inside the electrolyte layer of the fuel cell unit that it separates an electrolyte of a first fuel cell in particular ionically insulating of an electrolyte of a second fuel cell.
- the interconnector unit is arranged in a region of the electrolyte layer in which a cathode of a first fuel cell and an anode of a second fuel cell at least partially overlap. This can be a
- Fuel cell unit can be realized with advantageously large electrochemically active surfaces.
- Interconnector unit in the direction of the at least one anode layer and the at least one second layer of the interconnector unit in the direction of the at least one cathode layer in the direction of the at least one cathode layer.
- the fuel cell device comprises at least one carrier body on which the fuel cell unit is arranged.
- a carrier body is to be understood as meaning, in particular, an element which is intended to relieve and / or stabilize the at least one fuel cell unit, in particular mechanically, and in particular enables an advantageously thin design of the fuel cell unit.
- the carrier body may be designed in particular tubular.
- the carrier body can have a, in particular gas-tight, fastening section on at least one open tube end for attachment of the carrier body to a carrier substrate.
- the carrier body may have another such attachment portion or in particular be closed by a, in particular gas-tight, cap portion.
- the fuel cell unit is in particular arranged on the carrier body such that preferably the at least one cathode layer is adjacent to the carrier body.
- the carrier body is preferably gas-permeable and has, for example, gas-permeable pores and / or openings.
- the carrier body may in particular be formed from one or more ceramic and / or glassy materials.
- the support body may be formed of forsterite and / or zirconia and / or alumina. In this way, an advantageous mechanical and / or thermal stability of the fuel cell device can be achieved.
- at least the interconnector unit and preferably the entire fuel cell unit can be produced by means of screen printing.
- the materials of the interconnector unit and / or of the fuel cell unit and / or of the carrier body can be co-sintered. In this way, an advantageously simple and / or cost-effective production of the fuel cell device according to the invention can be achieved.
- the fuel cell device according to the invention should not be limited to the application and embodiment described above.
- the fuel cell device according to the invention may have a different number from a number of individual elements, components and units mentioned herein for fulfilling a mode of operation described herein. drawing
- FIG. 1 shows a schematic cross section through a fuel cell device with a fuel cell unit, which comprises at least two fuel cells, which by means of a two-layered
- Interconnector unit are connected in series with each other.
- FIG. 1 shows a schematic cross-section through a fuel cell device 46, which is only partially illustrated here.
- the fuel cell device 46 comprises a fuel cell unit 10, which by way of example comprises two fuel cells 12, 14 connected in series.
- the fuel cells 12, 14 are over a
- Interconnector unit 16 connected in series.
- the fuel cell unit 10 is designed in the form of a multi-layered layer system, wherein the fuel cells 12, 14 are formed substantially side by side.
- the fuel cell unit 10 comprises a cathode layer 22, an electrolyte layer 34 and an anode layer 28.
- the cathode layer 22 forms the cathodes 24, 26 of the fuel cells 12, 14.
- the anode layer 28 forms the anodes 30, 32 of the fuel cells 12, 14. Die
- Electrolyte layer 34 forms the electrolytes 36, 38 of the fuel cells 12, 14.
- the interconnect unit 16 is disposed completely within the electrolyte layer 34.
- the interconnector unit 16 is arranged such that via the interconnector unit 16, the cathode 24 of the first fuel cell 12 with the anode 32 of the second fuel cell 14 connected in series.
- the electrolyte 36 of the first fuel cell 12 is separated from the electrolyte 38 of the second fuel cell 14 by the interconnector unit 16, in particular ionically insulating.
- FIG. 1 furthermore illustrates that the cathodes 24, 26 of the fuel cells 12, 14 are separated from one another by an electrically and ionically insulating region 42 and the anodes 30, 32 of the fuel cells 12, 14 by at least one electrically and ionically insulating region 44.
- the cathodes 24, 26 and the anodes 30, 32 of the fuel cells 12, 14 are formed through the cathode layer 22 and the anode layer 28 such that the cathode 24 of the first fuel cell 12 forms the anode 32 of the second fuel cell 14 partially overlapped.
- the interconnector unit 16 is arranged in the electrolyte layer 34. Alternatively, however, it is possible to dispense with an overlap of a cathode and an anode.
- FIG. 1 furthermore shows that the fuel cell device 46 has a carrier body 40.
- the carrier body 40 may, for example, one or more
- the carrier body 40 may be both a tubular or tubular carrier body and a planar carrier body.
- the fuel cell device 46 can therefore be used both as a planar fuel cell device and preferably as a tubular one
- Fuel cell device may be formed.
- the fuel cell unit 10 may be applied in particular on an inner side or on an outer side, but preferably, as shown here, on the inner side of the carrier body 40.
- FIG. 1 illustrates that the cathodes 24, 26 of the fuel cells 12, 14 or the cathode layer 22 of the fuel cell unit 10 adjoin the carrier body 40.
- the carrier body 40 has in the at least
- the interconnector unit 16 is formed in two layers. A first layer 18 of the
- Interconnector unit 16 is at least essentially formed by a manganese-based perovskite.
- a second layer 20 of the interconnect unit 16 is at least essentially formed by a nickel-based perovskite.
- the nickel-based perovskite has the general chemical formula La Ni x Fei- X 0 3 , with 0.05 ⁇ x ⁇ 0.6.
- the layers 18, 20 of the interconnector unit 16 are arranged such that the first layer 18 of the interconnector unit 16 points in the direction of the anode layer 28 and the second layer 20 of the interconnector unit 16 in the direction of the at least one cathode layer 22.
- the interconnector unit 16 Due to the first layer 18, which is at least essentially formed by the manganese-based perovskite, the interconnector unit 16 has a sufficiently high conductivity (5 S / cm at 850 ° C.), in particular in an anodic atmosphere. At the same time, the first layer 18 protects the underlying second layer 20, which is at least substantially formed by the nickel-based perovskite, from harmful influences by the anodic atmosphere.
- the second layer 20 is advantageously gas-tight due to the good sintering properties of the nickel-based perovskite, whereby leakage of fuel gas from the fuel cell device 46 can be advantageously prevented. Due to the two-layer construction of the
- Interconnector unit 16 the positive material properties of the manganese-based perovskite of the first layer 18 and the nickel-based perovskite of the second layer 20 are advantageously combined.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Fuel Cell (AREA)
- Inert Electrodes (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020177001952A KR102444373B1 (ko) | 2014-07-28 | 2015-07-27 | 연료 전지 장치 |
JP2017504823A JP6516827B2 (ja) | 2014-07-28 | 2015-07-27 | 燃料電池装置 |
CN201580040713.3A CN106537671A (zh) | 2014-07-28 | 2015-07-27 | 燃料电池装置 |
US15/500,327 US20170222233A1 (en) | 2014-07-28 | 2015-07-27 | Fuel cell device |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102014214781.6A DE102014214781A1 (de) | 2014-07-28 | 2014-07-28 | Brennstoffzellenvorrichtung |
DE102014214781.6 | 2014-07-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2016016181A1 true WO2016016181A1 (de) | 2016-02-04 |
Family
ID=53785616
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2015/067136 WO2016016181A1 (de) | 2014-07-28 | 2015-07-27 | Brennstoffzellenvorrichtung |
Country Status (7)
Country | Link |
---|---|
US (1) | US20170222233A1 (de) |
JP (1) | JP6516827B2 (de) |
KR (1) | KR102444373B1 (de) |
CN (1) | CN106537671A (de) |
DE (1) | DE102014214781A1 (de) |
FR (1) | FR3024289A1 (de) |
WO (1) | WO2016016181A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3340356A1 (de) * | 2016-12-20 | 2018-06-27 | Robert Bosch GmbH | Brennstoffzellenvorrichtung |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB201617500D0 (en) | 2016-10-14 | 2016-11-30 | Coorstek Membrane Sciences As | Process |
GB201617494D0 (en) | 2016-10-14 | 2016-11-30 | Coorstek Membrane Sciences As | Process for the manufacture of a solide oxide membrane electrode assembly |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0198978A2 (de) * | 1985-03-21 | 1986-10-29 | Westinghouse Electric Corporation | Bildung eines haftenden Metallüberzugs auf der freiliegenden Oberfläche einer elektrischleitenden Keramik |
WO2008143657A1 (en) * | 2006-12-28 | 2008-11-27 | Saint-Gobain Ceramics & Plastics, Inc | Bilayer interconnnects for solid oxide fuel cells |
US20130101922A1 (en) * | 2011-10-19 | 2013-04-25 | Samsung Electro-Mechanics Co., Ltd. | Solid oxide fuel cell |
DE102012221427A1 (de) * | 2011-11-30 | 2013-06-06 | Robert Bosch Gmbh | Brennstoffzellensystem |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7378173B2 (en) * | 2000-05-18 | 2008-05-27 | Corning Incorporated | Fuel cells with enhanced via fill compositions and/or enhanced via fill geometries |
JP5173524B2 (ja) * | 2007-03-28 | 2013-04-03 | 三菱重工業株式会社 | 固体酸化物燃料電池及び水電解セル |
WO2009085143A1 (en) * | 2007-12-21 | 2009-07-09 | Saint-Gobain Ceramics & Plastics, Inc. | Ceramic interconnect for fuel cell stacks |
JP5222011B2 (ja) * | 2008-04-23 | 2013-06-26 | 三菱重工業株式会社 | 固体電解質型燃料電池 |
US20130122393A1 (en) * | 2011-06-15 | 2013-05-16 | Lg Fuel Cell Systems, Inc. | Fuel cell system with interconnect |
US9105880B2 (en) * | 2011-06-15 | 2015-08-11 | Lg Fuel Cell Systems Inc. | Fuel cell system with interconnect |
US20120321994A1 (en) * | 2011-06-15 | 2012-12-20 | Zhien Liu | Fuel cell system with interconnect |
US10446855B2 (en) * | 2013-03-15 | 2019-10-15 | Lg Fuel Cell Systems Inc. | Fuel cell system including multilayer interconnect |
-
2014
- 2014-07-28 DE DE102014214781.6A patent/DE102014214781A1/de active Pending
-
2015
- 2015-07-27 CN CN201580040713.3A patent/CN106537671A/zh active Pending
- 2015-07-27 JP JP2017504823A patent/JP6516827B2/ja active Active
- 2015-07-27 KR KR1020177001952A patent/KR102444373B1/ko active IP Right Grant
- 2015-07-27 WO PCT/EP2015/067136 patent/WO2016016181A1/de active Application Filing
- 2015-07-27 US US15/500,327 patent/US20170222233A1/en not_active Abandoned
- 2015-07-28 FR FR1557177A patent/FR3024289A1/fr active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0198978A2 (de) * | 1985-03-21 | 1986-10-29 | Westinghouse Electric Corporation | Bildung eines haftenden Metallüberzugs auf der freiliegenden Oberfläche einer elektrischleitenden Keramik |
WO2008143657A1 (en) * | 2006-12-28 | 2008-11-27 | Saint-Gobain Ceramics & Plastics, Inc | Bilayer interconnnects for solid oxide fuel cells |
US20130101922A1 (en) * | 2011-10-19 | 2013-04-25 | Samsung Electro-Mechanics Co., Ltd. | Solid oxide fuel cell |
DE102012221427A1 (de) * | 2011-11-30 | 2013-06-06 | Robert Bosch Gmbh | Brennstoffzellensystem |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3340356A1 (de) * | 2016-12-20 | 2018-06-27 | Robert Bosch GmbH | Brennstoffzellenvorrichtung |
Also Published As
Publication number | Publication date |
---|---|
FR3024289A1 (fr) | 2016-01-29 |
JP2017526123A (ja) | 2017-09-07 |
CN106537671A (zh) | 2017-03-22 |
KR102444373B1 (ko) | 2022-09-19 |
US20170222233A1 (en) | 2017-08-03 |
JP6516827B2 (ja) | 2019-05-22 |
KR20170033313A (ko) | 2017-03-24 |
DE102014214781A1 (de) | 2016-01-28 |
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