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
  • H01M8/002—Shape, form of a fuel cell
  • H01M8/004—Cylindrical, tubular or wound
• • 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
• • 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
  • H01M8/0252—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form tubular
• • 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
  • H01M8/1213—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material
  • H01M8/1226—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material characterised by the supporting layer
• • 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
  • H01M8/2404—Processes or apparatus for grouping fuel cells
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
  • H01M8/2425—High-temperature cells with solid electrolytes
  • H01M8/243—Grouping of unit cells of tubular or cylindrical configuration
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
  • H01M2008/1293—Fuel cells with solid oxide 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
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/023—Porous and characterised by the material
  • H01M8/0232—Metals or alloys
• • 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
• • 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

Definitions

• the present invention relates generally to solid oxide fuel cells, and, more particularly, to the electrical interconnection of solid oxide fuel cells .
• Tubular solid oxide fuel cells represent a significant advantage over planar-type SOFCs due to enhanced gas collection capability, ease of manufacture, and strength of the tubular design.
• Anode supported tubular SOFCs possess additional advantages over cathode or electrolyte supported cells due to lower cost, greater strength, and more intimate relationship with the critical gas component, i.e., the fuel. With this capture of the fuel, they also inherently have the ability to perform on-cell reformation of fuels rather than require external reforming equipment.
• Fig. 1 is a cross-sectional view of a typical anode-supported tubular SOFC as known in the art.
• an anode-supported tubular SOFC has a hollow, tubular inner anode layer 102, an electrolyte layer 104 formed on a portion of the outside of the anode layer 102 , and a cathode layer 106 formed on a portion of the electrolyte layer.
• Current flows radially from the inside to the outside along the length of the tube.
• current collection in anode-supported tubular SOFCs typically involves anodic electrical take-off connections 202 and cathodic electrical take-off connections 206 located at one end of the tubular fuel cell adjacent a fuel input 220.
• This arrangement allows mechanical ease of assembly, utilizing the gas distribution manifolds as current collection devices.
• wires must be run between the manifold and the cathode and/or anode. Due to separation and connection constraints, the manifold must be designed to allow for sufficient spacing to accommodate these connections, resulting in a relatively large system. Additionally, this arrangement generally results in large electrical power losses, proportional to the length and thickness of the anode supported fuel cell.
• Fig. 3 shows a representation of current decreasing as a function of increasing tube length for an anode-supported tubular SOFC having anodic and cathodic current collectors at one end of the fuel cell. It is therefore desirable to reduce or minimize these losses to enhance cell performance and lower fuel cell costs.
• Siemens Westinghouse describes the use of a single strip down the length of a cathode supported fuel cell, allowing current collection along the length, with only circumferential losses, although due to the design of their cathode-supported fuel cell, significant non-uniform circumferential stresses can be formed. With such a design, improved current collection is generally realized at the expense of a more complicated system design and greater variability in the packing of the tubular fuel cells.
• a system and method for interconnecting bundled solid oxide fuel cells is disclosed.
• Each one of a plurality of fuel cells has a plurality of discrete electrical connection points along an outer surface . Electrical connections are made directly between the discrete electrical connection points of adjacent fuel cells so that a manifold does not need to be used in current collection and the fuel cells can be packed more densely. In this way, the manifold is not constrained by electrical requirements and therefore can be redesigned to improve fuel cell density.
• Each fuel cell may include at least one outer electrode and at least one discrete interconnection to an inner electrode, wherein the outer electrode is one of a cathode and an anode and wherein the inner electrode is the other of the cathode and the anode .
• the system may also include a current collector configured to directly connect electrical connection points of adjacent fuel cells, and bridge connection points of the fuel cell on which it is located while not shorting the cathode to the anode for any individual fuel cell .
• Fuel cells may be aligned such that the cathode connection points of adjacent fuel cells are side-by-side and such that the anode connection points of adjacent fuel cells are side-by-side.
• fuel cells or the manufactured connections on the fuel cells may be staggered such that the cathode connection points of one fuel cell are side-by-side with the anode connection points of an adjacent fuel cell.
• the former configuration can be easily used to form serial or parallel electrical connections.
• the latter configuration is particularly useful for forming serial electrical connections, but can also be used to form parallel connections.
• these discrete connections provide for high-density packaging of fuel cells without hindering air flow between cells, as would a single connection running along the entire length of the cell (e.g., the Siemens Westinghouse connection type).
• a method of producing a fuel cell bundle comprises coupling a plurality of fuel cells to a manifold, and electrically interconnecting each fuel cell directly to at least one adjacent fuel cell so that the manifold is not required for electrical connectivity.
• Fig. 1 is a cross-sectional view of a typical anode-supported tubular SOFC as known in the art
• Fig. 2 shows a representation of a standard anode-supported tubular solid oxide fuel cell having anodic and cathodic current collectors at one end of the fuel cell as known in the art ;
• Fig. 3 shows a representation of current decreasing as a function of increasing tube length for an anode-supported tubular SOFC having anodic and cathodic current collectors at one end of the fuel cell, as shown in Fig. 2;
• Fig. 4 is a schematic of a tubular fuel cell with three electrical connection points;
• Fig. 5 shows a 4 x 4 fuel cell bundle
• Fig. 6 shows a close up of a serial connection between two adjacent fuel cells
• Fig. 7 shows a parallel connection using crimps or a welded joint
• Fig. 8 shows a serial connection using a crimp connection
• Fig. 9 shows a serial connection using a ceramic or metallic form,-
• Fig. 10 shows a serial connection using wire
• Fig. 11 shows prefabricated wire and clip segments
• Fig. 12 shows serial connections when the interconnection points on adjacent fuel cells are staggered
• Fig. 13A shows fuel cells with a current collector connecting from the cathode at substantially a 90° angle from the fuel cells
• Fig. 13B shows fuel cells with a current collector connecting from the anode interconnection at substantially a 90° angle from the fuel cells.
• Embodiments of the present invention use multiple electrical connection points along the outer surfaces of the fuel cells to make electrical connections directly between fuel cells so that the manifold does not need to be used in current collection.
• such direct electrical connections allow multiple fuel cells to be closely packed, in part because the manifold design is not constrained by electrical requirements .
• tubular anode-supported SOFCs having an inner anode, an intermediate electrolyte layer, and an outer cathode layer, although it should be understood that various aspects of the invention can apply to other types of anode-supported SOFCs (e.g., non-tubular) as well as other types of fuel cells that are not anode-supported.
• each anode-supported fuel cell may have multiple cathode and anode electrical connection points along the outer surface of the fuel cell, with the cathode being directly accessible for electrical connectivity by virtue of the cathode being the outer layer of the fuel cell, and with the anode being indirectly accessible for electrical connectivity, e.g., through an interconnection along the outer surface that is electrically coupled with the inner anode.
• fuel cell 10 includes interconnections 12a, 12b, 12c accessible from one side of the fuel cell so as to allow relatively easy access to both the cathode and anode, although it should be noted that fuel cell 10 may have a greater or fewer number of interconnections.
• the interconnections are typically constructed and placed in such a manner as to improve electrochemical and manufacturing efficiency.
• a tubular shape is used in the exemplary embodiments described, but other shapes (triangles, squares, etc) may be utilized in a similar manner.
• Serial and/or parallel electrical connections can be made between adjacent fuel cells by making electrical connections between the cathode and anode electrical connection points on one fuel cell and the cathode and anode electrical connection points on an adjacent fuel cell.
• the cathode of one fuel cell is electrically connected to the anode interconnection of the adjacent fuel cell.
• a parallel connection the cathodes of adjacent fuel cells are connected to one another, and/or the anodes of the adjacent fuel cells are connected to one another.
• Pig. 5 shows a fuel cell bundle 14 in accordance with an exemplary embodiment of the present invention.
• Fuel is distributed to fuel cells 18, which cells can be coupled to a manifold (not shown) , specifically by allowing fuel to flow through the tubular anode.
• a manifold not shown
• connections from the cathode and anode are not returned to a manifold, such as, for example, the cell- holding manifold 16. Rather, discrete connections are made directly between adjacent fuel cells, as discussed in greater detail below. In this way, the manifold is not constrained by electrical requirements and therefore can be redesigned to improve fuel cell density.
• Fig. 5 shows a serial connection between adjacent fuel cells 26 and 27.
• a current collector 24 e.g., a wire
• a current collector 24 extends from cathode 20 of fuel cell 26 to cathode 21 of fuel cell 26, but is raised above (i.e., bridged across) interconnection 23 of fuel cell 26 so that the wire does not contact interconnection 23.
• an insulator 34 may be placed between the interconnection 23 and the current collector 24.
• the current collector 24 is coupled to interconnection 22 of adjacent fuel cell 27. In this way, the cathode of fuel cell 26 is connected in series with the anode of adjacent fuel cell 27.
• wire or braid (24) may be disposed adjacent YSZ (electrolyte) and wrapped with highly conductive windings, such as a silver wire winding, to create a cathode connection.
• the wire or braid 24 may extend along the length of the fuel cell and be disposed under a winding of another cathode portion so as to form a singular cathode current collector.
• the wire or braids disposed under the cathode connection windings may terminate in a pigtail so as to allow flexibility for connection to similar pigtails disposed under cathode connection windings of the same fuel cell or for connection to cathode or anode pigtails on an adjacent fuel cell based on a desired fuel cell interconnection arrangement .
• Fig. 6 shows greater detail of a serial connection 28 of the type described above with reference to Fig. 5.
• current collector 24 ⁇ e.g., a wire
• cathode 20 of fuel cell 26 is attached to cathode 22 of fuel cell 26 and to cathode 21 of fuel cell
• Fig. 6 also shows an interconnection clip 25.
• Interconnection 23 comprises an interconnection material 36 that contacts the underlying, inner anode around which is placed a conductor layer, which can be, for example, thin wire-wrap or contact paste, or any other suitable contact material known in the art.
• cathode regions 20 and 21 comprise a cathode material 32 that covers a portion of the electrolyte.
• An uncovered electrolyte gap 85 is shown in Fig. 6, separating the cathode and interconnection regions.
• the electrolyte layer is discontinuous where the interconnection material contacts the anode layer.
• Fig. 5 and Fig. 6 depict a current collector in the form of a wire that is bridged between two cathode segments over an anode interconnection
• Fig. 13A and Fig. 13B show wire "pigtails" that are preformed on the cathodes and anode interconnections, respectively, and then coupled as needed.
• Fig. 13A shows wire pigtails 90 formed on the cathodes.
• Fig. 13B shows wire pigtails 91 formed on the anode interconnections. These pigtails can be interconnected to form serial and/or parallel connections between fuel cells.
• the cathode pigtails 90 on one fuel cell can be coupled to the anode pigtails 91 of an adjacent fuel cell, for example, by crimping, twisting, clip, wire, foam, or other means known in the art.
• the cathode pigtails 90 of adjacent fuel cells can be coupled to one another, while the anode pigtails 91 of adjacent fuel cells can be coupled to one another, for example, by crimping, twisting, clip, wire, foam, or other means known in the art.
• current collector 24 can be made from a variety of materials including, but not limited to, Ag, Au, Pt, Pdt coated metals, or conductive ceramics.
• Interconnections can be formed of a ceria-based, Fe-based, Cr-based or other gas- tight, dual-atmosphere ceramic conductor, such as, for example LaCr ⁇ 3 .
• Interconnection-to-interconnection, cathode- to-cathode, and interconnection-to-cathode connections can be made by, for example, the following: crimp 40 (for example, as shown in Fig. 7) ; clip 42 (for example, as shown in Fig.
• Fig. 7 shows parallel electrical connections using crimped wire pigtails 50, in accordance with an exemplary embodiment of the present invention. Also shown in Fig. 7 (and in Fig. 13B) , a wire or braid 91 can be disposed under an interconnection winding, interconnection chip or other electrically contacting means 92.
• the wire or braid can extend outboard of the winding to form pigtail in the manner discussed above to enable interconnection with other anode interconnection portions on the same fuel cell or to enable interconnection with other anode or cathode interconnection portions on one or more adjacent cells based on a desired fuel cell interconnection arrangement.
• electrical interconnection of fuel cells may be facilitated by aligning the anode interconnections (and, therefore, also aligning the cathodes) of adjacent fuel cells.
• adjacent fuel cells or the manufactured connection on adjacent fuel cells are staggered so that the cathodes 20 of one fuel cell are immediately adjacent to the anode interconnections 22 of the adjacent fuel cell.
• serial electrical connections between interconnections 22 and cathodes 20 can easily be made using current collectors 30, which can also act as spacers. By choosing cells of different connection spacings, serial/parallel connections can be constructed with minimal manufacturing effort .
• a uniform bundle of, for example, four cells by four cells can be constructed to have the voltage of four fuel cells and the current of four fuel cells, with fuel required for all sixteen.
• a four by four bundle is used for example only. Bundles of varying sizes may also be created to obtain the desired voltage and current. It will be understood from the above that bundles having at least two fuel cells in each of two dimensions or axes may be formed.
• bundles in this manner as a subset of a larger system.
• One bundle can be attached to a second bundle either by the same means within the bundle, or through use of interconnecting plates or wires that can be welded, crimped, sintered, or twisted.
• Construction of a fuel cell bundle can utilize on-bench fixturing. Such fixturing can be easily duplicated or automated to allow for many such bundles to be constructed in parallel, minimizing production time. Fixtures may include the use of perforated sheet at the ends of the bundle weights to maintain the bundle placement, and side-wall constraints.
• the fixtures would allow the formation of a green unsintered bundle body, as well as the sintering and fixing of that body through temperature and or gas processing. Once formation of the green body and fixing of that body is complete, the bundle should be self-supporting, requiring only fixturing as might be needed in support of the fuel cell system requirements such as gas flow or power control.
• the bundle may be sintered prior to full system assembly, or may be sintered in situ, as processing would dictate.
• Exemplary embodiments of the invention utilize 1.5 cm diameter anode-supported fuel cells with three anode interconnections each. However, similar methods and materials may be applied to any diameter with at least one discrete interconnection without substantive modification.

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• 2006
  • 2006-12-14 JP JP2008545824A patent/JP2009520326A/ja active Pending
  • 2006-12-14 EP EP06847665A patent/EP1979974A4/en not_active Withdrawn
  • 2006-12-14 WO PCT/US2006/047801 patent/WO2007075366A2/en not_active Ceased
  • 2006-12-14 US US11/639,361 patent/US8628891B2/en active Active
  • 2006-12-14 CA CA2633322A patent/CA2633322C/en active Active

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