WO2004105154A2 - Method of forming freestanding thin chromium components for an electrochemical converter - Google Patents
Method of forming freestanding thin chromium components for an electrochemical converter Download PDFInfo
- Publication number
- WO2004105154A2 WO2004105154A2 PCT/US2003/025517 US0325517W WO2004105154A2 WO 2004105154 A2 WO2004105154 A2 WO 2004105154A2 US 0325517 W US0325517 W US 0325517W WO 2004105154 A2 WO2004105154 A2 WO 2004105154A2
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- Prior art keywords
- component
- chromium
- electrochemical converter
- plate
- interconnector
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/64—Burning or sintering processes
- C04B35/645—Pressure sintering
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F5/00—Manufacture of workpieces or articles from metallic powder characterised by the special shape of the product
- B22F5/006—Manufacture of workpieces or articles from metallic powder characterised by the special shape of the product of flat products, e.g. sheets
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- B22F7/00—Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression
- B22F7/02—Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite layers
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- B22F7/00—Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression
- B22F7/06—Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite workpieces or articles from parts, e.g. to form tipped tools
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- B32B15/00—Layered products comprising a layer of metal
- B32B15/02—Layer formed of wires, e.g. mesh
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- B32B15/00—Layered products comprising a layer of metal
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- B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
- B32B5/22—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by the presence of two or more layers which are next to each other and are fibrous, filamentary, formed of particles or foamed
- B32B5/30—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by the presence of two or more layers which are next to each other and are fibrous, filamentary, formed of particles or foamed one layer being formed of particles, e.g. chips, granules, powder
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- B32B9/04—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00 comprising such particular substance as the main or only constituent of a layer, which is next to another layer of the same or of a different material
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/42—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on chromites
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- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/56—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C24/00—Coating starting from inorganic powder
- C23C24/08—Coating starting from inorganic powder by application of heat or pressure and heat
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C26/00—Coating not provided for in groups C23C2/00 - C23C24/00
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
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- H—ELECTRICITY
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- 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
- H01M8/0219—Chromium complex oxides
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
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- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
- H01M8/025—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form semicylindrical
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- B22F2998/10—Processes characterised by the sequence of their steps
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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Definitions
- the present invention relates to a method of fabricating a component of an electrochemical converter.
- Electrochemical converters generally comprise a series of electrolyte units onto which electrodes are applied, and a series of interconnector units, disposed between the electrolyte units, to provide serial electrical connections.
- Each electrolyte unit is typically an ionic conductor having low ionic resistance, thereby allowing the transport of an ionic species from one electrode-electrolyte interface to the opposite electrode- electrolyte interface under the particular operating conditions of the converter.
- electrolytes can be used in such electrochemical converters.
- zirconia stabilized with such compounds as magnesia, calcia or yttria can satisfy these requirements when operating at an elevated temperature, e.g., about 1000° C.
- These electrolyte materials utilize oxygen ions to carry electrical current.
- the electrolyte does not conduct electrons which can cause a short-circuit of the converter.
- the interconnector unit is typically a good electronic conductor.
- the interaction of the input reacting gas, electrode and electrolyte occur at the electrode-electrolyte interface, which requires that the electrodes be sufficiently porous to admit the reacting gas species to, and to permit exit of product gas species from the electrolyte surfaces.
- the converter element includes a series of electrolyte plates having an oxidizer electrode material on one side and a fuel electrode material on the opposing side, and a series of interconnector plates, alternately stacked with the electrolyte plates, that provide electrical contact with the electrolyte plates.
- the interconnector plate or the electrolyte plate may have a textured pattern that forms reactant-flow passageways. These passageways selectively distribute the fuel and oxidizer reactants introduced to the columnar converter element. For example, the passageways distribute the fuel reactant over the fuel electrode side of the electrolyte plate, and the oxidant reactant over the oxidizer electrode side of the electrolyte plate.
- a spacer plate can be interposed between the electrolyte and interconnector plates to provide passageways through which the reactants can flow.
- the spacer plate can be either a corrugated or a perforated plate.
- the present invention provides an improved method for fabricating a component of an electrochemical converter.
- the process of the present invention includes forming a free standing thin plate by using a tape casting method to form thin green sheets, and then applying a hot press method to density the sheet to a near zero porosity state: A plurality of tapes may be laminated together prior to hot pressing to provide a thicker structure or a composite structure comprising layers of different materials.
- the resulting component is ultra dense, thin, has high oxidation and corrosion resistance, high electrical and thermal conductivity, hydrogen reduction stability, and low thermal expansion to match with ceramic components also used in the electrochemical converter.
- the process of the present invention can be applied to silicon carbide SiC, high chromium alloys, chromium iron alloys (e.g., Cr-5wt%Fe-lwt%Y2O3), chromium magnesium alloys (e.g., Cr-5wt%Ni-lwt%MgO) and mixtures thereof.
- chromium iron alloys e.g., Cr-5wt%Fe-lwt%Y2O3
- chromium magnesium alloys e.g., Cr-5wt%Ni-lwt%MgO
- Figure 1 illustrates an electrochemical converter employing an interconnector plate formed by the teachings of the present invention.
- Figure 2 is a schematic flow chart diagram illustrating a method for forming a component of an electrochemical converter according to an illustrative embodiment of the invention.
- the present invention provides an improved method of fabricating a component of an electrochemical converter.
- the present invention will be described below relative to an illustrative embodiment. Those skilled in the art will appreciate that the present invention may be implemented in a number of different applications and embodiments and is not specifically limited in its application to the particular embodiments depicted herein.
- FIG. 1 shows an isometric view of an electrochemical converter 10 including one or more components manufactured according to the teachings of the present invention.
- the electrochemical converter 10 is shown consisting of alternating layers of an electrolyte plate 20 and an interconnector plate 30.
- Internal gas passages through the plates in the electrochemical converter provide conduits for the passage of fuel and oxidizer gases, e.g., input reactants, and permit the resultants to exit.
- Reactant-flow passageways formed in the interconnector plates or the electrolyte plates facilitate the distribution and collection of these gases.
- a flow adjustment element (not shown), may be provided between each electrolyte plate and each interconnector plate to serve as a fluid-flow impedance between the plates by restricting the flow of input reactants through the reactant-flow passageways.
- Gas seals and electrical contact between plates are obtained in the assembly by spring loading the interconnector plates against the surface of the electrolyte plates with or without seal materials.
- the plates of the electrochemical converter 10 are held in compression by a spring loaded tie-rod assembly 12.
- the tie-rod assembly 12 includes a tie-rod member 14 seated within a central oxidizer manifold that includes an assembly nut 14 A.
- High temperature electrochemical converters generally employ components that satisfy a number of demanding requirements, including the use of a thermally conductive metal of 10 btu/F-ft-hr and an electrically conductive metal of 10 4 mho/cm, low thermal expansion ceramics of 5 x 10 "6 in/in-F, a lightweight thin plate, for example, about 0.02 inch thickness, and a gas tight structure with no gas permeation.
- electrochemical converters generally have an oxidation resistance up to about 1000° C.
- zirconia a refractory ceramic material
- the zirconia electrochemical converter offer higher efficiency than most other conventional or advanced energy conversion systems.
- a zirconia electrochemical converter is assembled with thin plates of zirconia electrolyte alternately arranged with interconnector plates.
- the electrolyte plates are made of thin zirconia plates with electrode coatings.
- the interconnector plates are fabricated from corrosion-resistant, electrically conductive materials.
- To fabricate a zirconia electrochemical converter a freestanding electrolyte plate 20 with electrode coatings and a freestanding interconnector plate 30 are first fabricated. The plates are assembled by compression, with or without sealing material. Then, internal holes or manifolds and reactant-flow passageways can be formed in the plates to facilitate the passage of reactants and exhaust species.
- the illustrated interconnector plates 30 provide multiple functions in the electrochemical converter.
- the interconnector plates 30 provide low-loss electrical connections from cell-to-cell through a stack by contact with adjacent electrodes.
- the interconnector plates 30 also provide gas partitions to allow a repetitive series voltage connection of cells.
- the interconnector plates 30 also form effective thermal paths to conduct heat from the electrode surfaces to the outer edge of the plates, i.e., surfaces of the cell stack.
- the interconnector plates 30 may also form gaskets to prevent leakage of the reactants by the controlled yield of the material at operating temperature.
- the interconnector plates 30 also form stable structural members in the composite assembly encompassing the ceramic electrolyte plates and electrical conducting interconnector plates.
- a wide variety of conductive materials can be used for the thin interconnector plates of this invention. Such materials should meet the following requirements: (1) high strength, as well as electrical and thermal conductivity; (2) good oxidation resistance up to the working temperature; (3) chemical compatibility and stability with the input reactants; and (4) manufacturing economy when formed into the textured plate configuration exemplified by reactant-flow passageways.
- the material also optionally and preferably exhibits a coefficient of thermal expansion that correlates closely with the ceramic electrolyte plates, including Zirconia electrolyte plates.
- Suitable materials for interconnector plate fabrication include silicon carbide (SiC), high chromium alloys, such as a chromium oxide mixture, chromium iron alloys (Cr-5wt%Fe-lwt%Y 2 O 3 ) and chromium magnesium alloys (Cr-5wt%Ni-lwt%MgO). Chromium alloys are typically suitable for high temperature applications that employ ambient air of an oxidation environment. One skilled in the art will recognize that the invention is not limited to these materials and that any suitable material may be used.
- electrolyte and interconnector plates of between about 5 centimeters and about 15 centimeters in diameter are appropriate. However, depending upon the application and design parameters, other sizes obvious to the ordinary skilled artisan will be obvious. Stacks of a relatively smaller diameter are suitable for systems requiring quick transient response, while stacks of a relatively larger diameter are appropriate for base-load power systems.
- a zirconia converter of modular design can be conveniently packaged as a , small kW-level generator and also in a 10-25kW module as a building block in scaled- up MW-level general applications. The distinctive features that make this electrochemical converter stack suitable for practical power applications are its high power density, ease of heat removal, structural ruggedness and low stress assembly.
- FIG. 2 is a schematic flow chart diagram illustrating the steps involved in fabricating a component, such as a component of an electrochemical converter.
- the electrochemical converter components that can be made according to the method of the present invention include, but are not limited to, an interconnector plate and the contact surfaces of an interconnector plate.
- the component is a lightweight thin plate having a thickness of less than about 0.03 inches and preferably about 0.02 inch and having a relatively gas tight structure with little or no gas permeation.
- the fabrication method may be used to produce a thin, chrome-based, composite electrically conductive plate offering relatively high oxidation and corrosion resistances, high electrical conductivity, and excellent CTE to match with ceramic electrochemical converter components, though one skilled in the art will recognize that the invention is not limited to a chrome-based plate.
- a raw material of a selected composition in powder form is provided in step 10.
- the component raw material is mixed with selected additives, such as solvents, plasticizers, binders and/or dispersants, to create a generally uniform slurry.
- additives such as solvents, plasticizers, binders and/or dispersants
- the slurry is then cast into a sheet form, such as a "green tape” or pre-form, using tape casting, roll compaction, extrusion or calendaring machines.
- a tape casting machine produces a "green tape” by first pouring a slurry onto a flat surface, which may include a carrier film.
- a "doctor” blade is drawn over the slurry, or the slurry is drawn out beneath the doctor blade by the relative motion of the flat surface or carrier film, to produce a layer of tape with uniform thickness.
- the height of the blade which is adjustable, controls the thickness of the tape.
- the slurry dries in air to produce the "green tape", which is very flexible, due to the additives, and easy to handle.
- Each green tape produced in step 30 is then separately trimmed into one or more sheets in step 40.
- a plurality of sheets can be optionally stacked and laminated into a multilayered laminate structures in step 50, to provide thickness control or to combine materials of different composition into a multilayered body.
- the laminate structure can comprise a composite structure having layers of different materials or a plurality of layers of the same material.
- the laminate structure may be mechanically, chemically or thermally machined or trimmed into pre-determined configurations in step 60. Those of ordinary skill will readily recognize that the structure can be formed in any suitable shape.
- the laminate structure is hot pressed in step 70 by applying heat and pressure to form a high density, near zero porosity sintered structure.
- high density refers to a material having a specific density of about 96% or greater, i.e., the material occupies at least 96% of the volume of the component, such that the total pore volume is less than about 4% of the total volume of the component.
- the step of hot pressing comprises sintering the laminate structure into a dense structure using a pressure-assisted furnace or kiln in an inert or reducing atmosphere.
- Suitable temperatures and pressure for performing hot-pressing are obvious to those of ordinary skill in the art, and are generally in the range of about 1300°C and 1000 psi, respectively.
- the sintered structure may be mechanically, chemically, or thermally machined or trimmed to a desirable configuration in step 80.
- the trimmed sintered structure may be coated with other compounds, such as protective coatings, in step 90.
- the coating may be applied using plasma spray, chemical vapor deposition, or physical vapor deposition equipment, though one skilled in the art will recognize that the invention is not limited to these coating techniques.
- the fabrication method includes a step of subjecting the laminated structure to a furnace sintering process before the hot press process in step 70.
- a raw material comprising a fine powder i.e., having a particle size on the nanometer scale, is used to form the component.
- step 70 may alternatively comprise a pressure-free sintering step, which uses heat only to sinter the structure.
- the component is an electrically conductive interconnector plate, though one skilled in the art will recognize that the illustrated fabrication method may be used to fabricate any suitable component, including that of an electrochemical converter, or any other plate.
- the fabrication method of an illustrative embodiment of the invention produces a composite plate consisting of a high chromium core and a lanthanum chromite surface protection layer.
- the illustrated method produces an interconnector plate for an electrochemical converter that comprises a high chromium composite core and a lanthanum chromite surface protective sheet, though one skilled in the art will recognize that any suitable material may be used in the fabrication method of the present invention and any suitable component may be produced.
- a chromium-lanthanum chromite composite plate a sheet having a high chromium content, formed of a powder material that is preferably more than 95% chromium, is produced by tape casting, following steps 10-30 in Figure 2.
- a lanthanum chromite sheet is also produced by tape casting, following steps 10-30 in Figure 2.
- the chromium sheet is placed on top of the lanthanum chromite sheet, and pressed into a laminate structure, in step 50.
- the high chromium sheet can be sintered without the lanthanum chromite layer.
- the high chromium composite core of the interconnector plate provides an impermeable separator for the electrochemical converter stack.
- the lanthanum chromite surface layer provides protection against the loss of chromium from vaporization in the form of Cr 2 O 3 in the oxidizer side of the electrochemical devices.
- the interconnector plate formed by the illustrative fabrication method may have textured surfaces, which oppose flat surfaces of adjacent electrolyte plates in the stacked electrochemical converter.
- the interconnector plate may have flat surfaces, which oppose textured surfaces of adjacent electrolyte plates in the stacked electrochemical converter.
- the fabrication method of an illustrative embodiment of the present invention provides an ultra dense (i.e., having a specific density of at least 96%), thin and cheaper component for an electrochemical converter.
- the fabrication method produces a component having high oxidation and corrosion resistance, high electrical and thermal conductivity, hydrogen reduction stability of up to 1000 ° C, and low thermal expansion to match with ceramic components.
- the fabrication method for dense thin plates of the present invention can also employ in any applications including the electrochemical devices such as molten carbonate, phosphoric acid, and proton exchange membrane converters.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Composite Materials (AREA)
- Structural Engineering (AREA)
- Metallurgy (AREA)
- Wood Science & Technology (AREA)
- Inorganic Chemistry (AREA)
- Fuel Cell (AREA)
- Laminated Bodies (AREA)
Abstract
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004572198A JP2006510190A (en) | 2002-08-13 | 2003-08-13 | Method for forming freestanding thin chrome components for electrochemical transducers |
| EP03816846A EP1542864A2 (en) | 2002-08-13 | 2003-08-13 | Method of forming freestanding thin chromium components for an electrochemical converter |
| US10/524,805 US20060183018A1 (en) | 2002-08-13 | 2003-08-13 | Method of forming freestanding thin chromium components for an electochemical converter |
| AU2003304141A AU2003304141A1 (en) | 2002-08-13 | 2003-08-13 | Method of forming freestanding thin chromium components for an electrochemical converter |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40321802P | 2002-08-13 | 2002-08-13 | |
| US60/403,218 | 2002-08-13 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2004105154A2 true WO2004105154A2 (en) | 2004-12-02 |
| WO2004105154A3 WO2004105154A3 (en) | 2005-02-03 |
Family
ID=33476534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2003/025517 Ceased WO2004105154A2 (en) | 2002-08-13 | 2003-08-13 | Method of forming freestanding thin chromium components for an electrochemical converter |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20060183018A1 (en) |
| EP (1) | EP1542864A2 (en) |
| JP (1) | JP2006510190A (en) |
| CN (1) | CN1688438A (en) |
| AU (1) | AU2003304141A1 (en) |
| WO (1) | WO2004105154A2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101511582B1 (en) | 2013-12-10 | 2015-04-14 | 재단법인 포항산업과학연구원 | Method for manufacturing metal support for solid oxide fuel cell and solid oxide fuel cell comprising the same |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR3104324B1 (en) * | 2019-12-10 | 2021-12-03 | Commissariat A L Energie Atomique Et Aux Energies Alternatives | Improved method of making a component constituting an EHT electrolyzer or SOFC fuel cell interconnector. |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4749632A (en) * | 1986-10-23 | 1988-06-07 | The United States Of America As Represented By The United States Department Of Energy | Sintering aid for lanthanum chromite refractories |
| US4913982A (en) * | 1986-12-15 | 1990-04-03 | Allied-Signal Inc. | Fabrication of a monolithic solid oxide fuel cell |
| US4857420A (en) * | 1987-10-13 | 1989-08-15 | International Fuel Cell Corporation | Method of making monolithic solid oxide fuel cell stack |
| US5028650A (en) * | 1988-01-27 | 1991-07-02 | W. R. Grace & Co.-Conn. | Boron nitride sheets |
| US4883497A (en) * | 1988-03-28 | 1989-11-28 | Arch Development Corporation | Formation of thin walled ceramic solid oxide fuel cells |
| US5085720A (en) * | 1990-01-18 | 1992-02-04 | E. I. Du Pont De Nemours And Company | Method for reducing shrinkage during firing of green ceramic bodies |
| US5290642A (en) * | 1990-09-11 | 1994-03-01 | Alliedsignal Aerospace | Method of fabricating a monolithic solid oxide fuel cell |
| US5256499A (en) * | 1990-11-13 | 1993-10-26 | Allied Signal Aerospace | Monolithic solid oxide fuel cells with integral manifolds |
| US5171645A (en) * | 1991-01-08 | 1992-12-15 | Gas Research Institute, Inc. | Zirconia-bismuth oxide graded electrolyte |
| US5298469A (en) * | 1991-01-22 | 1994-03-29 | Alliedsignal Inc. | Fluxed lanthanum chromite for low temperature air firing |
| JP2945157B2 (en) * | 1991-03-27 | 1999-09-06 | 日本碍子株式会社 | Solid oxide fuel cell and method of manufacturing the same |
| US5273837A (en) * | 1992-12-23 | 1993-12-28 | Corning Incorporated | Solid electrolyte fuel cells |
| US5368667A (en) * | 1993-01-29 | 1994-11-29 | Alliedsignal Inc. | Preparation of devices that include a thin ceramic layer |
| DK94393D0 (en) * | 1993-08-18 | 1993-08-18 | Risoe Forskningscenter | PROCEDURE FOR THE PREPARATION OF CALCIUM-DOPED LANTHANCHROMITE |
| KR100395611B1 (en) * | 1994-03-21 | 2004-02-18 | 지텍 코포레이션 | Electrochemical Converter Assembly for Optimal Pressure Distribution |
| DE19730770C2 (en) * | 1996-08-06 | 2001-05-10 | Wacker Chemie Gmbh | Non-porous sintered bodies based on silicon carbide, process for their production and their use as substrates for hard disk storage |
| US5882809A (en) * | 1997-01-02 | 1999-03-16 | U.S. The United States Of America As Represented By The United States Department Of Energy | Solid oxide fuel cell with multi-unit construction and prismatic design |
| US6228520B1 (en) * | 1997-04-10 | 2001-05-08 | The Dow Chemical Company | Consinterable ceramic interconnect for solid oxide fuel cells |
| US5922486A (en) * | 1997-05-29 | 1999-07-13 | The Dow Chemical Company | Cosintering of multilayer stacks of solid oxide fuel cells |
| US6051330A (en) * | 1998-01-15 | 2000-04-18 | International Business Machines Corporation | Solid oxide fuel cell having vias and a composite interconnect |
| US6605316B1 (en) * | 1999-07-31 | 2003-08-12 | The Regents Of The University Of California | Structures and fabrication techniques for solid state electrochemical devices |
| US7163713B2 (en) * | 1999-07-31 | 2007-01-16 | The Regents Of The University Of California | Method for making dense crack free thin films |
| US6613468B2 (en) * | 2000-12-22 | 2003-09-02 | Delphi Technologies, Inc. | Gas diffusion mat for fuel cells |
| US6949307B2 (en) * | 2001-10-19 | 2005-09-27 | Sfco-Efs Holdings, Llc | High performance ceramic fuel cell interconnect with integrated flowpaths and method for making same |
| US7067208B2 (en) * | 2002-02-20 | 2006-06-27 | Ion America Corporation | Load matched power generation system including a solid oxide fuel cell and a heat pump and an optional turbine |
| YU88103A (en) * | 2002-05-14 | 2006-08-17 | H.Lundbeck A/S. | Treatment adhd |
| US6843960B2 (en) * | 2002-06-12 | 2005-01-18 | The University Of Chicago | Compositionally graded metallic plates for planar solid oxide fuel cells |
| AU2004247229B2 (en) * | 2003-06-09 | 2006-12-14 | Saint-Gobain Ceramics & Plastics, Inc. | Fused zirconia-based solid oxide fuel cell |
| US7550217B2 (en) * | 2003-06-09 | 2009-06-23 | Saint-Gobain Ceramics & Plastics, Inc. | Stack supported solid oxide fuel cell |
| US7303833B2 (en) * | 2004-12-17 | 2007-12-04 | Corning Incorporated | Electrolyte sheet with a corrugation pattern |
-
2003
- 2003-08-13 US US10/524,805 patent/US20060183018A1/en not_active Abandoned
- 2003-08-13 CN CNA038241366A patent/CN1688438A/en active Pending
- 2003-08-13 EP EP03816846A patent/EP1542864A2/en active Pending
- 2003-08-13 JP JP2004572198A patent/JP2006510190A/en active Pending
- 2003-08-13 WO PCT/US2003/025517 patent/WO2004105154A2/en not_active Ceased
- 2003-08-13 AU AU2003304141A patent/AU2003304141A1/en not_active Abandoned
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101511582B1 (en) | 2013-12-10 | 2015-04-14 | 재단법인 포항산업과학연구원 | Method for manufacturing metal support for solid oxide fuel cell and solid oxide fuel cell comprising the same |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2003304141A1 (en) | 2004-12-13 |
| EP1542864A2 (en) | 2005-06-22 |
| CN1688438A (en) | 2005-10-26 |
| JP2006510190A (en) | 2006-03-23 |
| AU2003304141A8 (en) | 2004-12-13 |
| US20060183018A1 (en) | 2006-08-17 |
| WO2004105154A3 (en) | 2005-02-03 |
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