GB2517425A - A fuel cell and its method of manufacture - Google Patents
A fuel cell and its method of manufacture Download PDFInfo
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- GB2517425A GB2517425A GB1314769.9A GB201314769A GB2517425A GB 2517425 A GB2517425 A GB 2517425A GB 201314769 A GB201314769 A GB 201314769A GB 2517425 A GB2517425 A GB 2517425A
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- 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
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- 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
- H01M8/006—Flat
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- 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
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- 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
- H01M8/0234—Carbonaceous material
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- 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
- H01M8/1097—Fuel cells applied on a support, e.g. miniature fuel cells deposited on silica supports
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- 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
- H01M8/2418—Grouping by arranging unit cells in a plane
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- 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
- H01M8/2465—Details of groupings of fuel cells
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- 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
- H01M2008/1095—Fuel cells with polymeric electrolytes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/30—Fuel cells in portable systems, e.g. mobile phone, laptop
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8828—Coating with slurry or ink
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8828—Coating with slurry or ink
- H01M4/8832—Ink jet printing
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- 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
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- 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
- H01M8/0239—Organic resins; Organic polymers
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- 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
- H01M8/1007—Fuel cells with solid electrolytes with both reactants being gaseous or vaporised
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- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02B90/10—Applications of fuel cells in buildings
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- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
- Inert Electrodes (AREA)
Abstract
A strip 1 of fuel cell components for use in forming a fuel cell comprises: a substrate 10, extending in a first direction, comprising a film having a layer of graphene 9 at least partially extending over the film; and a plurality of fuel cell components 2-8, each component formed on one or more of a plurality of substrate regions 12-18, the substrate regions being spaced apart along the first direction and separated by fold regions 22-29 which extend in a direction perpendicular to the first direction, wherein the strip is configured to be folded along the fold regions. The fuel cell components 2-8 may be formed by printing, e.g. 3D or inkjet printing. Preferably, a fuel cell or fuel cell stack is formed when the strip is folded. A method of manufacturing the strip of fuel cell components and its preferable assembly into a fuel cell is also disclosed.
Description
Intellectual Property Office Applicacion Nc,. (lB 1314769.9 RTM Dace: 4 Fchruary 2014 The following terms are registered trade marks and should he rcad as such wherever they occur in this document: Nafion.
Inlelleclual Property Office is an operaling name of the Pateni Office www.ipo.gov.uk
A FUEL CELL AND ITS METHOD OF MANUFACTURE
This invention relates to a fuel cell and, in particular, to a strip of fuel cell components for forming a fuel cell or fuel cell stack. The invention also relates to a method of manufacturing a fuel cell stack.
Typically, fuel cells comprise a proton exchange membrane (PEM) sandwiched between two porous electrodes, together comprising a membrane-electrode assembly (MEA). The MEA may include a catalyst layer. The MEA itself is conventionally sandwiched between: (i) a cathode diffusion structure (such as a cathode gas diffusion layer) having a first face adjacent to the cathode face of the MEA and (ii) an anode diffusion structure (such as an anode gas diffusion layer) having a first face adjacent the anode face of the MEA. The anode and cathode diffusion structures may each comprise a gas diffusion layer and a microporous layer. The second face of the anode diffusion structure contacts an anode fluid flow field plate for current collection and for is distributing hydrogen to the second face of the anode diffusion structure. The second face of the cathode diffusion structure contacts a cathode fluid flow field plate for current collection, for distributing oxygen to the second face of the cathode diffusion structure, and for extracting excess water from the MEA. The anode and cathode fluid flow field plates conventionally each comprise a rigid, electrically conductive, material having fluid flow channels in the surface adjacent the respective diffusion structure for delivery of the reactant gases (for example, hydrogen and oxygen) and removal of the exhaust gases (for example, unused oxygen and water vapour).
According to a first aspect of the invention we provide a strip of fuel cell components for use in forming a fuel cell comprising: a substrate, extending in a first direction, comprising a film having a layer of graphene at least partially extending over said film; and a plurality of fuel cell components, each component formed on one or more of a plurality of substrate regions, the substrate regions spaced apart along the first direction and separated by fold regions which extend in a direction perpendicular to the first direction, wherein the strip is configured to be folded along said fold regions.
This is advantageous as the strip provides for easy assembly of the fuel cell stack. The use of a thin film, which may be of a polymer, and a graphene layer provides a flexible, lightweight substrate on which the fuel cell components can be applied to form efficient micro-fuel cells.
Further, the layer of graphene provides for efficient control of the conductivity between the fuel cell components. The strip may contain fuel cell components for forming a single fuel cell or a fuel cell stack comprising a plurality of fuel cells or a subset of the components for forming a fuel cell or stack.
The film may be of a polymer material, such as Polydimethylsiloxane (PDPvIS) or Poly(methyl methacrylate). The film may be porous. This is advantageous as the film does not hinder flow through the fuel cell when the strip is assembled and the film acts as a support for the graphene layer.
The plurality of fuel cell components may be formed by printing. This is advantageous as the strip can be fed through a printer which prints the fuel cell components onto the strip. The printer may be an additive printer such as a 3D printer or an ink-jet printer.
The plurality of fuel cell components comprise at least one or more of a first membrane; a catalyst layer; a first microporous layer; a first gas diffusion layer; a bi-polar plate; a second gas diffusion layer; a second microporous layer; a second membrane; and a second catalyst layer. The components may be combined and formed on one or more of the substrate regions. For example! a combined membrane and catalyst layer may be provided which includes a proton exchange membrane having the catalyst layer thereon formed on one or more substrate regions.
The strip of fuel cell components may be configured such that, when folded, the strip of fuel cell components comprises at least a portion of a fuel cell stack or a fuel cell. Thus, the strip may include all of the components required to form the fuel cell or stack. Alternatively it may comprise a subset of said components and the missing components may be inserted into the folded or unfolded strip in a further manufacturing step.
The strip may include electrically conductive fold regions and non-electrically conductive fold regions. The conductive fold regions may comprise regions over which the layer of graphene extends and the non-conductive regions may comprise regions where the layer of graphene is absent. Thus! the non-conductive regions comprise an insulator region to prevent a flow of current between adjacent components under normal operating conditions of the assembled cell.
The conductive regions may have a resistivity of less than 100 nOm. The non-conductive regions may have a resistivity of greater than 100 Um. The strip of fuel cell components may comprise a plurality of portions of a fuel cell stack! wherein successive portions are connected to each other by electrically non-conductive fold regions, such that the strip of fuel cell components is configured to comprise a fuel cell stack when folded.
At least one of the fuel cell components may extend over a plurality adjacent substrate regions.
This is advantageous as the thickness of a fuel cell component can be controlled by the number of adjacent substrate regions it is distributed over. When the strip is folded the adjacent components will be brought together to form the complete fuel cell component layer.
The fuel cell components may include at least a first combined membrane and catalyst layer. The first membrane and catalyst layer may be formed over a plurality of adjacent substrate regions.
The combined membrane and catalyst layers may be formed by printing a catalyst onto a membrane layer. The membrane of the combined membrane and catalyst layer may include graphene oxide, such as a coating of graphene oxide. The layer may include conductive ribbons extending therefrom. The membrane may comprise graphene oxide printed with conductive ribbons. The ribbons provide a convenient way of connected a current path to the fuel cell or fuel cell stack.
The strip may include holes formed through at least one of the fuel cell components for controlling the porosity through the component.
The layer of graphene may include a plurality of holes such that the graphene layer is porous.
The membrane and catalyst layers may comprise an array of holes such that the combined membrane and catalyst layers are porous. The film of polymer and the graphene layer may comprises an array of holes such that the film with the graphene layer is porous. Thus, the layer of graphene, membrane, catalyst and other components and substrate, may include holes that provide the layer with porosity such that when folded, the layer does not detrimentally affect the transport of fluids through the assembled fuel cell/fuel cell stack.
The holes in the gas diffusion layers may have a larger diameter than holes in the microporous layers.
According to a further aspect of the invention we provide a method of manufacturing a strip of fuel cell components comprising: providing a substrate, extending in a first direction, comprising a film coated with graph en e, forming on regions of the substrate a plurality of fuel cell components, wherein the regions of the substrate are spaced apart along the first direction and separated by a plurality of fold regions.
The plurality of fuel cell components may comprise at least one or more of: a first membrane; a first catalyst layer; a first microporous layer; a first gas diffusion layer; a bi-polar plate; a second gas diffusion layer; a second microporous layer; a second membrane; and a second catalyst layer.
The step of forming may comprise printing the fuel cell components onto the substrate. The method may include the step of forming holes or pores through at least one of the fuel cell components for controlling the porosity through the component and possibly the film. The holes may extend through the film or may extend through both the fuel cell component and the film.
The holes may be formed by lithography.
The method may include the step of folding the strip to assemble a fuel cell. Adjacent components may advantageously be brought into face to face contact when the strip is fan-folded to form a fuel cell or fuel cell stack.
There now follows, by way of example only, a detailed description of embodiments of the invention with reference to the following figures, in which: Figure 1 shows a side view of a strip of fuel cell components; Figure 2 shows a plan view of the strip shown in Figure 1; Figure 3 shows the strip shown in Figure 1 folded to form part of a fuel cell stack; Figure 4 shows a diagrammatic view of the strip showing the control of porosity along the strip; Figure 5 shows a cross section through the strip; Figure 6 shows a further example of the strip; and Figure 7 shows a flow chart illustrating an example method of assembling a fuel cell using the strip of fuel cell components.
Figures 1 and 2 show a strip 1 of fuel cell components for forming a fuel cell or fuel cell stack comprising a plurality of fuel cells stacked together. The fuel cell components described in this embodiment comprise a plurality of layers. The layers form a fuel cell having a proton exchange membrane (PEM) between an anode and a cathode, which together form a membrane electrode assembly (MEA). The anode and cathode may include a catalyst material and therefore form a catalyst later. Also, the anode and cathode each have an associated gas diffusion structure, which may comprise one or more layers, such as a gas diffusion layer and a microporous layer. A flow field plate or bipolar plate may deliver fuel and/or oxidant to the gas diffusion structures.
However, it will be appreciated that the strip 1 may contain one or more or all of these fuel cell components.
The strip I includes a plurality of fuel cell components 2, 3, 4, 5, 6, 7, 8 arranged side by side.
The strip 1 comprises a substrate 10, extending in a first direction, X. The substrate 10 comprises a film of a polymer material, such as Polydimethylsiloxane (PDMS) or Polymethyl methacrylate (PMMA). The film has a layer of graphene 9 at least partially extending over said film. The film may be porous and acts as a support for the graphene layer. The film has a thickness of between 0.05 pm and 1 pm and the graphene layer may have a thickness of 0.001 pm and 0.01 pm.
The plurality of fuel cell components 2, 3, 4, 5, 6, 7, 8 are each formed on a respective substrate region 12, 13, 14, 15, 16, 17, 18. The substrate regIons are spaced apart along the first direction, X, and separated by fold regions 22, 23, 24, 25, 26, 27, 28, 29 which extend in a direction, 1, perpendicular to the first direction, X. The strip 1 is configured to be folded along said fold regions 22, 23, 24, 25, 26, 27, 28, 29 when forming a fuel cell or fuel cell stack.
In this example, the strip 1 shown in Figures 1 and 2 comprises a repeating unit, n, of fuel cell components 2, 3, 4, 5, 6, 7, 8 which are intended to be folded and form a plurality of fuel cells arranged in a stack configuration. The strip thus extends further, as represented by component 2n+1 and component 8n1 in dashed lines.
Fuel cell component 2 is located on substrate region 12 and comprises a membrane which includes a catalyst layer. The fuel cell component 2 thus forms the proton exchange membrane and catalyst layer of the resulting fuel cell. The membrane may comprise a polymer such as Nation and is preferably non-electrically conductive. The catalyst layer may be coated or printed onto the membrane. A graphene layer (distinct from graphene layer 9 which extends over the substrate) may be provided over the membrane. The graphene layer and catalyst layer may be porous and may include holes. The holes may be formed by lithography or other micro/nano fabrication techniques. The membrane and catalyst layer is shown diagrammatically in Figure 4 where holes 40 are shown extending through the catalyst layer and graphene layer 2. Rather than a graphene layer, a graphene oxide layer may cover the membrane Alternatively, a graphene oxide layer may replace the Nafion membrane. The use of graphene oxide is advantageous as it has similar properties to Nafion in that it is proton conductive, electrically non-conductive and water permeable. Terminal ribbons (not shown) of graphene may be formed, which receive the current generated by the cell and thereby provide a current flow path. The terminal ribbons may be formed by nano-heaters to reduce the graphene oxide to graphene on the graphene oxide layer. The catalyst layer can then be formed over the ribbons by coating the surface with catalyst particles, if present. The catalyst layer may comprise any suitable catalyst, such as platinum.
Fuel cell component 3 is located on substrate region 13 and forms a microporous layer (MPL) of the fuel cell. The MPL may be formed of a graphene material, although other materials may be used. The MPL is shown diagrammatically in Figure 4. The MPL may be porous and the porosity may be determined by a plurality of holes formed in the MPL. Figure 4 shows a plurality of holes 41 formed in the MPL, which provide transport of fluids to and from the membrane and catalyst layer 2. The holes may be formed through the substrate 10 as well as the MPL 3.
Fuel cell component 4 is located on substrate region 14 and forms a gas diffusion layer (GDL) of the fuel cell. The CDL is shown diagrammatically in Figure 4. The GDL is formed of a graphene material, although other materials could be used. The GDL may be porous and the porosity may be determined by a plurality of holes formed in the CDL. Figure 4 shows a plurality of holes 42 formed in the CDL, which provide transport of fluids to and from the membrane and catalyst layer 2 through the MPL 3. The holes 42 may be larger than the holes 41 of the MPL. Thus, the porosity of the layers will increase with distance from the membrane and catalyst layer 2. The holes may be formed through the substrate 10 as well as the CDL 4. Further, the CDL provides transport of fluid in a direction perpendicular to the thickness of the layer (i.e. in the X and Y directions) while the MPL provides transport substantially through the thickness of the layer with less transport in the perpendicular directions.
Fuel cell componentS is located on substrate region 15 and forms a bipolar plate of the fuel cell.
With reference to Figure 5, the bipolar plate contains at least one track 43 for transporting fluid to and from the CDL 4. The bipolar plateS contains at least one further, separate track on its opposite side for transporting fluid to and from the fuel cell component 6. The bipolar plate 5 may be of a conductive non-porous material such as graphene sheet Further, the bipolar plate may be of two halves; with one half provided on one side of substrate 10 and the other half provided on the other side of substrate 10. Each half of the plate may be configured to provide a track for transporting fluids to the respective fuel cell component 4 or 6.
Fuel cell component 6 is located on substrate region 16 and forms a gas diffusion layer (CDL) of an adjacent fuel cell in the fuel cell stack (when considering the bipolar plate as providing the boundary between adjacent fuel cells in the stack). The CDL 6 is of the same construction as CDL 4.
Fuel cell component 7 is located on substrate region 17 and forms a microporous layer (MPL) and has the same construction as MPL 3.
The fuel cell component 8 is located on substrate region 18 and forms a membrane which includes a catalyst layer. The component 8 has the same construction as fuel cell component 2.
The fold regions 22 to 29 comprise portions of the strip 1 that are foldable and in this example are absent of fuel cell components. The fold regions 23 to 28 are electrically conductive due to the graphene layer 9 extending between components 2 and 3, 3 and 4, 4 and 5, Sand 6, 6 and 7, and 7 and 8. Thus, these components are electrically connected together by the graphene layer 9.
The fold regions 22 and 29 are non-conductive and the graphene layer 9 does not extend over said regions (shown as boxes in Figure 1 for purposes of clarity). The non-conductive fold region 22 extends between membrane/catalyst layer 2 and a component of an adjacent unit along the strip 1. The component 8n1 also comprises a membrane/catalyst layer 2. The non-conductive fold region 29 extends between membrane/catalyst layer 8 and a component of an adjacent unit along the strip 1. The component 2n+1 also comprises a membrane/catalyst layer 2. Thus, no current flow path is provided through the membrane. Instead, the current flow path is provided by the ribbons, which extend from the catalyst layer and are insulated from the membrane by the layer of graphene oxide, as described above. The width of the fold regions may not be constant.
Depending how the strip is to be folded, the fold regions may alternate between narrow and wide along the strip depending on whether faces of the substrate will be brought together at a particular fold or whether faces of the adjacent fuel cell components will be brought together. The wider fold regions would thus need to accommodate the thickness of the adjacent fuel cell components to allow them to come together face to face when the strip is folded.
Figure 3 shows the strip 1 when folded to form part of a fuel cell 30. The strip 1 is fan-folded in concertina fashion. Thus, adjacent fold regions 22 to 29 are folded in opposite directions. The strip is shown spaced apart for clarity and it will be appreciated that when folded the fuel cell components 2, 3, 4, 5, 6, 7, 8 and substrate 10 are in face-to-face contact. Thus, the membrane with catalyst layer 2 contacts the microporous layer 3. The microporous layer 3 contacts the gas diffusion layer 4 (through the substrate 10). The gas diffusion layer 4 contacts the bipolar plate 5.
The bipolar plateS contacts the gas diffusion layer 6 (through the substrate 10). The gas diffusion layer 6 contacts the microporous layer 7. The microporous layer 7 contacts the membrane with catalyst layer 8 (through the substrate 10). As the substrate 10 is porous, it does not hinder the flow of fluid between the fuel cell components.
Figure 5 shows a cross-section through part of the strip 1 showing the holes or pores visible in Figure 4. The fold regions are narrow in this figure such that the fuel cell components appear to extend continuously over the substrate. Figure 5 shows the substrate 10 and the fuel cell components 2 to 8. The membrane 50 of the membrane and catalyst layer 2 is shown without holes formed therethrough. However, the catalyst layer 51 that lies on the membrane 50 has pores 40 formed therethrough. The MPLs 3 and 7 and GDLs 4 and 6 both have holes 41 and 42 respectively that extend through the strip 1. The holes 42 of the GDL are larger in area and/or diameter than the holes 41 of the MPL. The bipolar plate 5 has a track 43 on one side and a separate track 53 on its opposite side. The tracks 43, 53 are arranged to deliver fluid to the gas diffusion layers 4 and 6 respectively.
Figure 6 shows an alternative arrangement of the membrane/catalyst layer 2. In this example, the membrane/catalyst layer is formed over a plurality of substrate regions, each substrate region defined between two fold regions. Thus, several substrate regions with membrane material and catalyst material formed thereon make up the complete membrane and catalyst layer in the assembled fuel cell/fuel cell stack.
Figure 6 shows a first membrane/catalyst sub-component 60' formed on a substrate region 61.
The membrane/catalyst component has the same form as discussed above in relation to fuel cell component 2. A second membrane/catalyst sub-component 60' is formed on a substrate region 62 adjacent the first component 60, separated by the fold region 63. Likewise, further membrane/catalyst sub-components up to 60 are provided. When folded together in fan-like manner, the membrane/catalyst sub-components 60 to 6O form the complete membrane/catalyst layer of the resulting fuel cell.
It will be appreciated that any of the other fuel cell layers may be provided over one or more adjacent substrate regions. When the strip is folded, the component layers are brought together to form a complete layer of the resultant fuel cell. This provides a convenient way of forming the fuel cell component layers of a desired thickness. Thus, the fuel cell layers may be formed by a fuel cell component on a single substrate region or the fuel cell component may be distributed over multiple adjacent substrate regions. If, for example, a thicker gas diffusion layer is required, several adjacent substrate regions in the strip are formed with gas diffusion layer material thereon, which when folded together forms the gas diffusion layer.
Figure 7 shows a flow chart illustrating the formation of a fuel cell or fuel cell stack using the strip 1. Step 70 comprises receiving the substrate 10. Step 71 comprises applying the fuel cell components to the substrate regions of the substrate, Step 72 comprises providing the required porosity through the substrate and/or components, possibly by the formation of holes. Step 73 comprises the step of fan-folding the strip Ito form a fuel cell or fuel cell stack.
In the above examples, the fuel cell components are formed by printing onto one side of the substrate. However, the components may be applied to the strip by other techniques. Also, the fuel cell components may be formed on both sides of substrate.
Claims (21)
- CLAIMS1. A strip of fuel cell components for use in forming a fuel cell comprising: a substrate, extending in a first direction, comprising a film having a layer of graphene at least partially extending over said film; and a plurality of fuel cell components, each component formed on one or more of a plurality of substrate regions, the substrate regions spaced apart along the first direction and separated by fold regions which extend in a direction perpendicular to the first direction, wherein the strip is configured to be folded along said fold regions.
- 2. A strip of fuel cell components as in claim 1, wherein the plurality of fuel cell components are formed by printing.
- 3. A strip of fuel cell components as in claim 1 or 2, wherein the plurality of fuel cell components comprises at least one or more of: a first membrane a catalyst layer; a first microporous layer; a first gas diffusion layer; a bi-polar plate; a second gas diffusion layer; a second microporous layer; a second membrane; and a second catalyst layer.
- 4. A strip of fuel cell components as in claim 3, configured such that when folded the strip of fuel cell components comprises at least a portion of a fuel cell stack.
- 5. A strip of fuel cell components as in any preceding claim, in which the strip includes electrically conductive fold regions and non-electrically conductive fold regions.
- 6. A strip of fuel cell components as in any preceding claim, in which at least one of the fuel cell components extends over a plurality of adjacent substrate regions.
- 7. A strip of fuel cell components as in any preceding claim, wherein the fuel cell components include at least a first combined membrane and catalyst layer comprising a membrane having a catalyst coating.
- & A strip of fuel cell components as in claim 7, wherein the first membrane and catalyst layer is formed over a plurality of adjacent substrate regions.
- 9. A strip of fuel cell components as in claim 7 or claim 8, wherein the combined membrane and catalyst layer includes graphene oxide.
- 10. A strip of fuel cell components as in any of claims 7 to 9, wherein the membrane and catalyst layer includes at least one conductive ribbon extending therefrom.
- 11. A strip of fuel cell components as in any preceding claim, wherein the layer of graphene includes a plurality of holes such that the graphene layer is porous.
- 12. A strip of fuel cell components as in any of claims 7 to 10, wherein the membrane and catalyst layers comprise an array of holes such that the combined membrane and catalyst layers are porous.
- 13. A strip of fuel cell components as in any preceding claim, wherein the substrate includes an comprises an array of holes such that the substrate is porous.
- 14. A strip of fuel cell components as in claim 3, wherein strip includes fuel cell components comprising a gas diffusion layer and a microporous layer both including holes therein, wherein the holes in the gas diffusion layer are larger than the holes the microporous layers.
- 15. A method of manufacturing a strip of fuel cell components comprising: providing a substrate, extending in a first direction, comprising a film coated with graphene, forming on regions of the substrate a plurality of fuel cell components, wherein the regions of the substrate are spaced apart along the first direction and separated by a plurality of fold regions.
- 16. A method of manufacturing a strip of fuel cell components as in claim 15, wherein the plurality of fuel cell components comprises at least one or more of: a first membrane; a first catalyst layer; a first microporous layer; a first gas diffusion layer; a bi-polar plate; a second gas diffusion layer; a second microporous layer; a second membrane; and a second catalyst layer.
- 17. A method as defined in claim 15 or claim 16, in which the step of forming comprises printing at least one of the fuel cell components onto the substrate.
- 18. A method as defined in any one of claims 15 to 17, in which the method includes the step of forming holes through at least one of the fuel cell components for controlling the porosity through the component.
- 19. A method as defined in any one of claims 15 to 18, in which the method includes the step of folding the strip to assemble a fuel cell.
- 20. A strip as described herein and illustrated in figures ito 6 of the drawings.
- 21. A method as described herein and illustrated in figure 7 of the drawings.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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GB1314769.9A GB2517425A (en) | 2013-08-19 | 2013-08-19 | A fuel cell and its method of manufacture |
TW103127749A TWI624988B (en) | 2013-08-19 | 2014-08-13 | A fuel cell and its method of manufacture |
PCT/GB2014/052532 WO2015025147A1 (en) | 2013-08-19 | 2014-08-18 | A fuel cell and its method of manufacture |
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GB1314769.9A GB2517425A (en) | 2013-08-19 | 2013-08-19 | A fuel cell and its method of manufacture |
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GB201314769D0 GB201314769D0 (en) | 2013-10-02 |
GB2517425A true GB2517425A (en) | 2015-02-25 |
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GB1314769.9A Withdrawn GB2517425A (en) | 2013-08-19 | 2013-08-19 | A fuel cell and its method of manufacture |
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GB (1) | GB2517425A (en) |
TW (1) | TWI624988B (en) |
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Cited By (1)
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GB2545433A (en) * | 2015-12-15 | 2017-06-21 | Grafmarine | Power generation and cell storage apparatus |
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US10381654B2 (en) | 2017-02-03 | 2019-08-13 | Nissan North America, Inc. | Methods of preparing electrodes having targeted oxygen transport |
US11043687B2 (en) * | 2018-04-11 | 2021-06-22 | Dana Limited | Method of making components for an electrochemical cell and an electrochemical cell and cell stack |
AT16961U1 (en) * | 2019-04-04 | 2021-01-15 | Zieger Johannes | |
DE102019210798A1 (en) * | 2019-07-22 | 2021-01-28 | Robert Bosch Gmbh | Method for manufacturing a distribution structure for a fuel cell |
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WO2005064731A2 (en) * | 2003-12-23 | 2005-07-14 | Universität Stuttgart | Electrochemical cell arrangement having a pocket-shaped structure |
JP5007986B2 (en) * | 2004-02-04 | 2012-08-22 | 学校法人東京理科大学 | Fuel cell |
WO2007050460A2 (en) * | 2005-10-25 | 2007-05-03 | Inorganic Specialists, Inc. | Carbon nanofiber paper and applications |
KR101920713B1 (en) * | 2011-12-23 | 2018-11-22 | 삼성전자주식회사 | Graphene device and method of manufacturing the same |
KR102037469B1 (en) * | 2012-01-02 | 2019-10-28 | 삼성전자주식회사 | Graphene electronic device and manufacturing method thereof |
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2013
- 2013-08-19 GB GB1314769.9A patent/GB2517425A/en not_active Withdrawn
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- 2014-08-13 TW TW103127749A patent/TWI624988B/en not_active IP Right Cessation
- 2014-08-18 WO PCT/GB2014/052532 patent/WO2015025147A1/en active Application Filing
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US5736017A (en) * | 1996-05-15 | 1998-04-07 | Mitsubishi Denki Kabushiki Kaisha | Solid high polymer electrolytic module and method of manufacturing the same |
JP2003346867A (en) * | 2002-05-27 | 2003-12-05 | Seiko Epson Corp | Fuel cell and its manufacturing method |
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Also Published As
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TW201523994A (en) | 2015-06-16 |
GB201314769D0 (en) | 2013-10-02 |
WO2015025147A1 (en) | 2015-02-26 |
TWI624988B (en) | 2018-05-21 |
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