WO2016124937A1 - Component for a fuel cell system - Google Patents
Component for a fuel cell system Download PDFInfo
- Publication number
- WO2016124937A1 WO2016124937A1 PCT/GB2016/050266 GB2016050266W WO2016124937A1 WO 2016124937 A1 WO2016124937 A1 WO 2016124937A1 GB 2016050266 W GB2016050266 W GB 2016050266W WO 2016124937 A1 WO2016124937 A1 WO 2016124937A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- state
- component
- fuel cell
- trigger
- condition
- Prior art date
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 239000012530 fluid Substances 0.000 claims description 33
- 230000005684 electric field Effects 0.000 claims description 9
- 238000009792 diffusion process Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 5
- 239000003446 ligand Substances 0.000 claims description 5
- 150000002500 ions Chemical class 0.000 claims description 4
- DYLIWHYUXAJDOJ-OWOJBTEDSA-N (e)-4-(6-aminopurin-9-yl)but-2-en-1-ol Chemical compound NC1=NC=NC2=C1N=CN2C\C=C\CO DYLIWHYUXAJDOJ-OWOJBTEDSA-N 0.000 claims description 3
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 3
- 150000007942 carboxylates Chemical class 0.000 claims description 3
- JUJWROOIHBZHMG-UHFFFAOYSA-O pyridinium Chemical compound C1=CC=[NH+]C=C1 JUJWROOIHBZHMG-UHFFFAOYSA-O 0.000 claims description 3
- 239000000376 reactant Substances 0.000 claims description 3
- 125000003827 glycol group Chemical group 0.000 claims description 2
- 210000004027 cell Anatomy 0.000 description 46
- 239000010410 layer Substances 0.000 description 14
- 230000002209 hydrophobic effect Effects 0.000 description 11
- 239000007789 gas Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 3
- 230000003993 interaction Effects 0.000 description 3
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- WGQKYBSKWIADBV-UHFFFAOYSA-O benzylaminium Chemical compound [NH3+]CC1=CC=CC=C1 WGQKYBSKWIADBV-UHFFFAOYSA-O 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000012954 diazonium Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-O diazynium Chemical compound [NH+]#N IJGRMHOSHXDMSA-UHFFFAOYSA-O 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000002094 self assembled monolayer Substances 0.000 description 2
- 239000013545 self-assembled monolayer Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- INOAASCWQMFJQA-UHFFFAOYSA-N 16-sulfanylhexadecanoic acid Chemical compound OC(=O)CCCCCCCCCCCCCCCS INOAASCWQMFJQA-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 210000003850 cellular structure Anatomy 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
-
- 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
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
-
- 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
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
-
- 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 invention relates to a component for a fuel cell system and in particular, although not exclusively, to such a component with improved fluid flow properties.
- FIG. 1 One example layout of a conventional fuel cell 10 is shown in figure 1 which, for clarity, illustrates the various layers in exploded form.
- a solid polymer ion transfer membrane 11 is sandwiched between an anode 12 and a cathode 13.
- the anode 12 and the cathode 13 are both formed from an electrically conductive, porous material such as porous carbon, to which small particles of platinum and/or other precious metal catalyst are bonded.
- the anode 12 and cathode 13 are often bonded directly to the respective adjacent surfaces of the membrane 11. This combination is commonly referred to as the membrane-electrode assembly, or MEA.
- Intermediate backing layers 15a and 13a may also be employed between the anode fluid flow field plate 14 and the anode 12 and similarly between the cathode fluid flow field plate 15 and the cathode 13.
- the backing layers 15a are of a porous nature and fabricated so as to ensure effective diffusion of gas to and from the anode and cathode surfaces as well as assisting in the management of water vapour and liquid water. For this reason, the backing layers 15a are sometimes also referred to as gas diffusion layers (GDLs).
- GDLs gas diffusion layers
- the fluid flow field plates 14, 15 are formed from an electrically conductive, non-porous material by which electrical contact can be made to the respective anode electrode 12 or cathode electrode 13.
- the fluid flow field plates facilitate the delivery and/or exhaust of fluid fuel, oxidant and/or reaction product to or from the porous electrodes 12, 13. This is conventionally effected by forming fluid flow passages in a surface of the fluid flow field plates, such as grooves or channels 16 in the surface presented to the porous electrodes 12, 3.
- one conventional configuration of fluid flow channel provides a serpentine structure 20 in a face of the anode 14 (or cathode 15) having an inlet manifold 21 and an outlet manifold 22 as shown in figure 2a.
- the serpentine structure 20 comprises a channel 16 in the surface of the plate 14 (or 15), while the manifolds 21 and 22 each comprise an aperture through the plate so that fluid for delivery to, or exhaust from, the channel 20 can be communicated throughout the depth of a stack of plates in a direction orthogonal to the plate as particularly indicated by the arrow in the cross-section on A-A shown in the figure 2b.
- a conventional fuel cell assembly stacks of plates are built up.
- adjacent anode and cathode fluid flow field plates are combined in conventional manner to form a single bipolar plate 31 having anode channels 32 on one face and cathode channels 33 on the opposite face, each adjacent to a respective membrane-electrode assembly (MEA) 34.
- MEA membrane-electrode assembly
- the inlet manifold apertures 21 and outlet manifold apertures 22 are all overlaid to provide the inlet and outlet manifolds to the entire stack.
- the various elements of the stack are shown slightly separated for clarity, although it will be understood for the purposes of the present invention that they will be compressed together using sealing gaskets.
- the individual fuel cell assemblies 30 can be provided separately, for example in a row.
- Water management is an important consideration in the operation of such fuel cells.
- product water from the reaction between hydrogen and oxygen is formed at catalytic sites of the MEA. This water must be exhausted from the MEA via the cathode diffusion structure at the same time that oxygen is transported to the cathode face of the MEA.
- the MEA remains suitably hydrated to ensure that the internal electrical resistance of the cell remains within tolerable limits. Failure to control the MEA humidification leads to hot spots and potential cell failure and/or poor electrical cell performance.
- a component for a fuel cell system having a surface region that is reconfigurable between at least a first state and a second state, wherein the first state is more hydrophiiic than the second state and wherein the surface is configured to adopt the first state or the second state in accordance with a condition at the surface.
- the surface region may be dynamically controlled.
- the surface region may be dynamically reconfigurable during operation of the fuel cell system.
- the surface region may be reversibly configurable between at least a first state and a second state.
- the surface region may be reconfigurable in response to time-dependent stimulus.
- the surface region may be configured to adopt the second state in response to a localised increase in a water level at the surface.
- the surface region may be configured to switch from the first state to the second state in response to an increase in a water level at the surface.
- the condition may be one or more of a water level, a current density, an electric field, electric potential at the surface, a temperature, temperature gradient at the surface, a pH of a fluid at the surface or a concentration of a ligand or ion at the surface.
- the component may be one of: a gas diffusion layer, a fuel cell plate, a fluid flow plate configured to guide reactant over an active area of a fuel cell of the fuel cell system, a water separator, a heat exchanger, a pump or a fluid line.
- the surface region may have one or more further states in addition to the first and second states.
- the surface region may have a continuum of states between the first and second states. Each state may have a different level of hydrophobicity to the other states.
- Such a surface region may provide a variety of hydrophobic conditions in response to the condition at the surface.
- the component may comprise a plurality of independently reconfigurable surface regions.
- the plurality of independently reconfigurable surface regions may comprise at least first and second subsets. Each subset may comprise one or more reconfigurable surface regions.
- the first subset may be configured to adopt one of the first state and the second state in response to the condition at the surface meeting a first trigger.
- the second subset may be configured to adopt one of the first state and the second state in response to the condition at the surface meeting a second trigger.
- the first trigger may be different to, or the same as, the second trigger.
- the first trigger may relate to a different type of condition to the second trigger.
- the first trigger may relate to the same type of condition as the second trigger.
- the first trigger may be at a different level to the second trigger.
- a layer of molecules may be attached to the surface.
- Each molecule may have a functional end group.
- Each molecule may have a chain connecting the surface to the functional end group.
- the functional end group may be configured to attract or repel water molecules.
- the chain may be configurable such that in one of the first state and the second state the functional end group is provided distally from the surface for interacting with water molecules.
- the chain may be configurable such that in the other of the first state and the second state the functional end group is provided proximal to the surface and inhibited from interacting with water molecules.
- the functional end group may comprise a benzyl moiety, such as benzyl ammonium, pyridinium or a carboxylate.
- the chain may comprise an alkyl chain or glycol chain selected to have a different hydrophobicity to the functional end group.
- the chain may be more or less hydrophobic than the functional end group.
- the chain may comprise a trans- isomer in one of the first and second states.
- the chain may comprise a cis-isome
- a method of operating a fuel cell system comprising a component having a surface region with at least a first state and a second state, wherein the first state is more hydrophilic than the second state, the method comprising reconfiguring the surface to adopt the first state or the second state in accordance with a condition at the surface.
- a fuel cell system comprising a component as described above.
- Figure 1 shows a schematic cross-sectional view through a part of a conventional fuel cell
- Figures 2a and 2b respectively show a simplified plan and sectional view of a fluid flow field plate of the fuel cell of figure 1 ;
- Figure 3 shows a cross-sectional view through a conventional fuel cell stack with bipolar plates
- Figures 4 illustrates an example of a component with a surface having a reconfigurable hydrophobicity
- Figures 5a and 5b show schematic views of a first state and a second state of a surface having reconfigurable hydrophobicity.
- the invention relates generally to a component for a fuel cell system that has a reconfigurable surface.
- the reconfigurable, or switchable, surface is able to vary its hydrophobicity between at least a first state and a second state according to its environment.
- the first state is more hydrophilic than the second state.
- the second state is more hydrophobic than the first state because hydrophobicity can be considered to be the absence of a hydrophilic attraction.
- the surface is configured to adopt the first state or the second state in accordance with a condition at the surface, for example a voltage change at a gas diffusion layer or bipolar plate. In this way interracial properties, such as wetting behaviour, at the surface can be dynamically controlled in accordance with the environment at the surface.
- the surface may therefore automatically compensate for variations in the environmental condition without the need for any active, or external, control in order to improve the performance of the component.
- Figures 4 illustrates an example of a component 40 for a fuel cell system.
- the component is a fuel cell plate configured to guide reactant over an active area of a fuel cell, which may be provided in a fuel cell stack of the fuel cell system.
- the component 40 of figure 4 is generally similar to the component described with reference to 2a and 2b except that the component 40 of figure 4 has a surface 42 with a reconfigurable hydrophobicity.
- the reconfigurable surface may also be provided in the water manifolds (the inlet and outlet) of the plate.
- the surface 42 of the component 40 comprises a plurality of reconfigurable surface regions 44, 46. Each regions is independently reconfigurable between at least a first state and a second state. That is, a state of one region 44 of the surface 42 does not affect a state of another region 46 of the surface 42.
- the plurality of surface regions may be provided over the entirety of the surface or over only a portion of the surface (less than the entirety of the surface).
- reconfigurable surface regions 44, 46 are provided along a fluid flow path between the inlet and the outlet. In this example it is not necessary to coat the inlands that separate the regions of the fluid flow path and so the amount of reconfigurable material used may be reduced compared to examples in which the entire surface is coated.
- the plurality of surface regions 44, 46 are configured to adopt the first state or the second state in accordance with a condition at the surface.
- localised flooding can occur at one or more regions of the surface 42 due to a build-up of water by-product from electrochemical reactions occurring at the MEA.
- Localised flooding caused by the water build-up results in a decrease in the efficiency of the cell and can cause premature and localised failure of the cell.
- Another effect of localised flooding is that an electrical potential in the region of the cell that is flooded may be reduced because of the localised decrease in efficiency. This change in potential provides a trigger for switching the state of the reconfigurable surface.
- the reconfigurable surface may change from a hydrophilic, or neutral, first state to a hydrophobic second state in order to clear the flooded water from the affected region and so improve the localised operation of the component 40.
- An advantage of this technique is that the response of the surface 40 to the environmental conditions is automatic in that no additional control or actuation is required in order to affect the change. In this way, the component automatically compensates for the occurrence of undesirable surface conditions, such as localised flooding.
- a first surface region 44 is in the first state.
- Second and third surface regions 46 have adopted the second state (more hydrophobic than the first state) in response to a localised increase in water level, or more specifically in response to the localised increase in water level altering the local potential within the second and third regions 46. In this way, the interfacial properties of the regions of the surface are dynamically controlled in accordance with the local environment at the surface 42.
- the condition that acts as a trigger for the switching is a current density, an electric field or electric potential at the surface.
- the surface may be configured to adopt a particular configuration in response to a temperature or temperature gradient at the surface, or in response to a pH of a fluid at the surface, the relative humidity of the fluid at the surface, the pressure of the fluid at the surface, a compressive force applied to the surface or the chemistry of the fluid at the surface.
- Each of these conditions may be affected by localised flooding of the surface.
- the surface may be configured to adopt a particular configuration directly in response to relative humidity of the fluid at the surface
- the component may be a different fuel cell stack component such as a gas diffusion layer.
- the component may be a water separator, a heat exchanger, a pump or a fluid line of a fuel cell system.
- the surface 42 of the component 40 may comprise a plurality of reconfigurable surface regions in which there are first and second subsets of the plurality of reconfigurable surface regions. Each subset can comprise one or more reconfigurable surface regions. The first subset is configured to adopt the first state or the second state in response to the condition at the surface 42 meeting a first trigger.
- the second subset is configured to adopt the first state or the second state in response to the condition at the surface 42 meeting a second trigger.
- All of the surface regions 44, 46 in figure 4 have the same type and level of trigger and so any division of these regions 44, 46 into first and second subsets results in the first subset having a first trigger that is both the same type and same level as a second trigger of the second subset.
- the first trigger may be different from the second trigger.
- the first trigger may be a different type to the second trigger.
- the first trigger may be related to the ionic conductivity of fluid at the surface and the second trigger may be related to an electric field at the surface (or any other type of condition).
- both the first trigger and the second trigger are related to the electric field, for example, then the triggers are of the same type.
- the first trigger may be at a different level than the second trigger.
- the first trigger may have a level of 100 V.m "1 and the second trigger may have a level of 200 V.m "1 .
- the first subset of reconfigurable surface regions may switch from the second state to the first state when the electric field at those regions falls below 100 V.m 1 and the second subset of reconfigurable surface regions may switch from the second state to the first state when the electric field at regions falls below 200 V.m "1 .
- the reconfigurable surface regions in the first and second subset may both be sensitive to the temperature at the surface.
- the state of the first subset may be set in response to the temperature passing 300 K and the state at the second subset may be set in response to the temperature passing 350 K.
- Figures 5a and 5b show schematic views of a surface 50 having reconfigurable hydrophobicity. The surface is shown in a first state in figure 5a and in a second, less hydrophilic state in figure 5b.
- the surface 50 comprises a bulk 52 and a layer of molecules 54a, 54b, 56 attached to the bulk 52.
- the layer of molecules 54a, 54b, 56 may be provided as a self-assembled monolayer.
- Each molecule 54a, 54b, 56 has a functional end group 56 and a chain 54a, 54b connecting the bulk 52 to the functional end group 56.
- the functional end group 56 is configured to attract or repel water molecules and also configured to be attracted to, or repelled from, the bulk depending upon a condition.
- the condition is the electric potential of the bulk 52 of the surface 50 and the functional end group 56 is a positively-charged hydrophilic ligand that exhibits an attractive force for water molecules.
- the functional group may be chosen from elements or compounds that are known to exhibit an attraction or repulsion in response to a particular temperature or temperature gradient at the surface, or in response to a pH of a fluid at the surface, the relative humidity of the fluid at the surface, the pressure of the fluid at the surface, a compressive force applied to the surface or the chemistry of the fluid at the surface, including, for example a concentration of a particular ligand or ion at the surface.
- the surface 50 may be made to be responsive to a variety of conditions.
- end groups for use in fuel cell applications include a benzyl end group, covalently bound to the substrate using diazonium chemistry; or pyridinium, benzyl ammonium or other positively-charged group attached to an unbound end of the alkyl chain; its positive charge conferring potential-dependent switching behaviour.
- An alkyl chain may be attached to the end group in a para position.
- an electro-positive end group in a fuel cell environment may provide the additional benefit of absorbing any free anions which are present in the system, such as CI " .
- the functional end group 56 may be a negative end group such as a hydrophilic carboxylate.
- the chain 54a, 54b is resiliently flexible between a first configuration in the first state and a second configuration in the second state to allow the functional end group 56 to move relative to the bulk 52.
- the chain is a molecule that is able to shift between isomer configurations depending upon the applied conditions.
- the chain may adopt a trans-isomer in the first state and a cis-isomer in the second state.
- the chain may itself be hydrophobic, such as a hydrophobic alkyl chain, in order to increase the variation in hydrophobicity between the first and second states.
- a preferred route for effecting a bond between the functional end group, or ligand, and the substrate of the surface is to form a covalent bond using diazonium chemistry.
- the layer of molecules 54a, 54b, 56 may also be provided as a self-assembled monolayer, such as a monolayer of (16-Mercapto)hexadecanoic acid (MHA). MHA self assembles on Au(111) and provides the reconfigurable surface properties.
- MHA (16-Mercapto)hexadecanoic acid
- Figure 5a illustrates a first state of the surface 50 in which the bulk is electropositive (carries a positive charge 58).
- the functional end group 56 is also electropositive and so is repelled from the bulk 52.
- the chain 54a is configured such that the functional end group 56 is provided distally from the bulk 52.
- the chain 54a is therefore orientated to enable interaction between the functional end group 56 and water molecules.
- the functional end group 56 exerts an attractive force on water molecules in this example and so the first state of the surface is hydrophilic.
- the absolute sign of the electric field applied at the surface 50 does not necessarily need to change in order to cause a reorientation of the chain molecules between the first and second positions. Instead the sign of the potential may change with respect to a potential of zero charge (pzc) of the surface.
- the pzc of the surface, including switchable chain molecules, may be tuned so that it is at a trigger level intermediate between, for example, the potential of a flooded cell and a functioning fuel cell.
- Figure 5b illustrates a second state of the surface 50 in which the bulk is less electropositive than the surface 50 in the first state, and so is relatively electronegative (illustrated as carrying a negative charge 60).
- the electropositive functional end group 56 is attracted to the bulk 52.
- the chain 54b is configured such that the functional end group 56 is provided proximal to the bulk 52.
- the orientation of the chain 54b therefore inhibits interaction between the functional end group 56 and water molecules.
- the interaction between the functional end group 56 and water molecules is inhibited by shielding of the functional end group 56 from the water molecules by the chain 54b.
- the surface 50 illustrated in figures 5a and 5b may be provided on a component of a fuel cell such as a fuel cell plate that is positively charged during operation. During normal operation, a higher positive charge is present on the surface 50 than during impaired operation when the surface 50 is flooded.
- the surface 50 therefore adopts the first, hydrophilic state (illustrated in figure 5a) during normal operation and the second hydrophobic state (illustrated in figure 5b) during impaired operation.
- the adoption of a hydrophobic state counteracts the flooding that is impairing operation of the fuel cell. In this way, operational fuel cell may be automatically improved.
- the molecules may move through a range of conformations between the extremes shown in figures 5a and 5b.
- the surface energy of the surface may vary continuously between first state and the second state. This property may be advantageous in fuel cell applications because it enables fine control of the movement of liquid water within the fuel cell system.
- a level of hydrophobicity may be provided by the reconfigurable surface in proportion to the level of water at the surface.
Abstract
The invention relates to a component for a fuel cell system. The component has a surface region that is reconfigurable between at least a first state and a second state, wherein the first state is more hydrophilic than the second state and wherein the surface is configured to adopt the first state or the second state in accordance with a condition at the surface.
Description
Component for a Fuel Cell System
The invention relates to a component for a fuel cell system and in particular, although not exclusively, to such a component with improved fluid flow properties.
Conventional electrochemical fuel cells convert fuel and oxidant into electrical energy and a reaction product. One example layout of a conventional fuel cell 10 is shown in figure 1 which, for clarity, illustrates the various layers in exploded form. A solid polymer ion transfer membrane 11 is sandwiched between an anode 12 and a cathode 13. Typically, the anode 12 and the cathode 13 are both formed from an electrically conductive, porous material such as porous carbon, to which small particles of platinum and/or other precious metal catalyst are bonded. The anode 12 and cathode 13 are often bonded directly to the respective adjacent surfaces of the membrane 11. This combination is commonly referred to as the membrane-electrode assembly, or MEA.
Sandwiching the polymer membrane and porous electrode layers is an anode fluid flow field plate 14 and a cathode fluid flow field plate 15. Intermediate backing layers 15a and 13a may also be employed between the anode fluid flow field plate 14 and the anode 12 and similarly between the cathode fluid flow field plate 15 and the cathode 13. The backing layers 15a are of a porous nature and fabricated so as to ensure effective diffusion of gas to and from the anode and cathode surfaces as well as assisting in the management of water vapour and liquid water. For this reason, the backing layers 15a are sometimes also referred to as gas diffusion layers (GDLs). The fluid flow field plates 14, 15 are formed from an electrically conductive, non-porous material by which electrical contact can be made to the respective anode electrode 12 or cathode electrode 13. At the same time, the fluid flow field plates facilitate the delivery and/or exhaust of fluid fuel, oxidant and/or reaction product to or from the porous electrodes 12, 13. This is conventionally effected by forming fluid flow passages in a surface of the fluid flow field plates, such as grooves or channels 16 in the surface presented to the porous electrodes 12, 3.
With reference also to figure 2a, one conventional configuration of fluid flow channel provides a serpentine structure 20 in a face of the anode 14 (or cathode 15) having an inlet manifold 21 and an outlet manifold 22 as shown in figure 2a. According to conventional design, it will be understood that the serpentine structure 20 comprises a channel 16 in the surface of the plate 14 (or 15), while the manifolds 21 and 22 each
comprise an aperture through the plate so that fluid for delivery to, or exhaust from, the channel 20 can be communicated throughout the depth of a stack of plates in a direction orthogonal to the plate as particularly indicated by the arrow in the cross-section on A-A shown in the figure 2b.
With reference to figure 3, in an example of a conventional fuel cell assembly 30, stacks of plates are built up. In this arrangement, adjacent anode and cathode fluid flow field plates are combined in conventional manner to form a single bipolar plate 31 having anode channels 32 on one face and cathode channels 33 on the opposite face, each adjacent to a respective membrane-electrode assembly (MEA) 34. The inlet manifold apertures 21 and outlet manifold apertures 22 are all overlaid to provide the inlet and outlet manifolds to the entire stack. The various elements of the stack are shown slightly separated for clarity, although it will be understood for the purposes of the present invention that they will be compressed together using sealing gaskets. Alternatively, the individual fuel cell assemblies 30 can be provided separately, for example in a row.
Water management is an important consideration in the operation of such fuel cells. During operation of a fuel cell, product water from the reaction between hydrogen and oxygen is formed at catalytic sites of the MEA. This water must be exhausted from the MEA via the cathode diffusion structure at the same time that oxygen is transported to the cathode face of the MEA. However, it is also important that the MEA remains suitably hydrated to ensure that the internal electrical resistance of the cell remains within tolerable limits. Failure to control the MEA humidification leads to hot spots and potential cell failure and/or poor electrical cell performance.
According to a first aspect of the invention there is provided a component for a fuel cell system, the component having a surface region that is reconfigurable between at least a first state and a second state, wherein the first state is more hydrophiiic than the second state and wherein the surface is configured to adopt the first state or the second state in accordance with a condition at the surface.
The surface region may be dynamically controlled. The surface region may be dynamically reconfigurable during operation of the fuel cell system. The surface region may be reversibly configurable between at least a first state and a second state. The surface region may be reconfigurable in response to time-dependent stimulus.
The surface region may be configured to adopt the second state in response to a localised increase in a water level at the surface. The surface region may be configured to switch from the first state to the second state in response to an increase in a water level at the surface. The condition may be one or more of a water level, a current density, an electric field, electric potential at the surface, a temperature, temperature gradient at the surface, a pH of a fluid at the surface or a concentration of a ligand or ion at the surface.
The component may be one of: a gas diffusion layer, a fuel cell plate, a fluid flow plate configured to guide reactant over an active area of a fuel cell of the fuel cell system, a water separator, a heat exchanger, a pump or a fluid line.
The surface region may have one or more further states in addition to the first and second states. The surface region may have a continuum of states between the first and second states. Each state may have a different level of hydrophobicity to the other states. Such a surface region may provide a variety of hydrophobic conditions in response to the condition at the surface.
The component may comprise a plurality of independently reconfigurable surface regions. The plurality of independently reconfigurable surface regions may comprise at least first and second subsets. Each subset may comprise one or more reconfigurable surface regions. The first subset may be configured to adopt one of the first state and the second state in response to the condition at the surface meeting a first trigger. The second subset may be configured to adopt one of the first state and the second state in response to the condition at the surface meeting a second trigger. The first trigger may be different to, or the same as, the second trigger. The first trigger may relate to a different type of condition to the second trigger. The first trigger may relate to the same type of condition as the second trigger. The first trigger may be at a different level to the second trigger. A layer of molecules may be attached to the surface. Each molecule may have a functional end group. Each molecule may have a chain connecting the surface to the functional end group. The functional end group may be configured to attract or repel water molecules. The chain may be configurable such that in one of the first state and the second state the functional end group is provided distally from the surface for interacting with water molecules. The chain may be configurable such that in the other of the first state and the second state the functional end group is provided proximal to the surface and inhibited from interacting with water molecules.
The functional end group may comprise a benzyl moiety, such as benzyl ammonium, pyridinium or a carboxylate. The chain may comprise an alkyl chain or glycol chain selected to have a different hydrophobicity to the functional end group. The chain may be more or less hydrophobic than the functional end group. The chain may comprise a trans- isomer in one of the first and second states. The chain may comprise a cis-isomer in the other of the first and second states.
According to a further aspect of the invention there is provided a method of operating a fuel cell system comprising a component having a surface region with at least a first state and a second state, wherein the first state is more hydrophilic than the second state, the method comprising reconfiguring the surface to adopt the first state or the second state in accordance with a condition at the surface. According to a further aspect of the invention there is provided a fuel cell system comprising a component as described above.
Embodiments of the present invention are now described, by way of example only, with reference to the accompanying drawings, in which:
Figure 1 shows a schematic cross-sectional view through a part of a conventional fuel cell;
Figures 2a and 2b respectively show a simplified plan and sectional view of a fluid flow field plate of the fuel cell of figure 1 ;
Figure 3 shows a cross-sectional view through a conventional fuel cell stack with bipolar plates;
Figures 4 illustrates an example of a component with a surface having a reconfigurable hydrophobicity; and
Figures 5a and 5b show schematic views of a first state and a second state of a surface having reconfigurable hydrophobicity.
The invention relates generally to a component for a fuel cell system that has a reconfigurable surface. The reconfigurable, or switchable, surface is able to vary its hydrophobicity between at least a first state and a second state according to its environment. The first state is more hydrophilic than the second state. Expressed in another way, the second state is more hydrophobic than the first state because hydrophobicity can be considered to be the absence of a hydrophilic attraction.
The surface is configured to adopt the first state or the second state in accordance with a condition at the surface, for example a voltage change at a gas diffusion layer or bipolar plate. In this way interracial properties, such as wetting behaviour, at the surface can be dynamically controlled in accordance with the environment at the surface. The surface may therefore automatically compensate for variations in the environmental condition without the need for any active, or external, control in order to improve the performance of the component.
Figures 4 illustrates an example of a component 40 for a fuel cell system. In this example, the component is a fuel cell plate configured to guide reactant over an active area of a fuel cell, which may be provided in a fuel cell stack of the fuel cell system. The component 40 of figure 4 is generally similar to the component described with reference to 2a and 2b except that the component 40 of figure 4 has a surface 42 with a reconfigurable hydrophobicity. The reconfigurable surface may also be provided in the water manifolds (the inlet and outlet) of the plate.
The surface 42 of the component 40 comprises a plurality of reconfigurable surface regions 44, 46. Each regions is independently reconfigurable between at least a first state and a second state. That is, a state of one region 44 of the surface 42 does not affect a state of another region 46 of the surface 42.
The plurality of surface regions may be provided over the entirety of the surface or over only a portion of the surface (less than the entirety of the surface). In the example shown in figure 4, reconfigurable surface regions 44, 46 are provided along a fluid flow path between the inlet and the outlet. In this example it is not necessary to coat the inlands that separate the regions of the fluid flow path and so the amount of reconfigurable material used may be reduced compared to examples in which the entire surface is coated.
The plurality of surface regions 44, 46 are configured to adopt the first state or the second state in accordance with a condition at the surface. During operation of a fuel cell in which the component 40 is located, localised flooding can occur at one or more regions of the surface 42 due to a build-up of water by-product from electrochemical reactions occurring at the MEA. Localised flooding caused by the water build-up results in a decrease in the efficiency of the cell and can cause premature and localised failure of the cell. Another effect of localised flooding is that an electrical potential in the region of the cell that is flooded may be reduced because of the localised decrease in efficiency. This change in potential provides a trigger for switching the state of the reconfigurable surface. The
reconfigurable surface may change from a hydrophilic, or neutral, first state to a hydrophobic second state in order to clear the flooded water from the affected region and so improve the localised operation of the component 40. An advantage of this technique is that the response of the surface 40 to the environmental conditions is automatic in that no additional control or actuation is required in order to affect the change. In this way, the component automatically compensates for the occurrence of undesirable surface conditions, such as localised flooding.
Three of the plurality of reconfigurable surface regions are labelled in figure 4. A first surface region 44 is in the first state. Second and third surface regions 46 have adopted the second state (more hydrophobic than the first state) in response to a localised increase in water level, or more specifically in response to the localised increase in water level altering the local potential within the second and third regions 46. In this way, the interfacial properties of the regions of the surface are dynamically controlled in accordance with the local environment at the surface 42.
In this example, the condition that acts as a trigger for the switching is a current density, an electric field or electric potential at the surface. Alternatively, the surface may be configured to adopt a particular configuration in response to a temperature or temperature gradient at the surface, or in response to a pH of a fluid at the surface, the relative humidity of the fluid at the surface, the pressure of the fluid at the surface, a compressive force applied to the surface or the chemistry of the fluid at the surface. Each of these conditions may be affected by localised flooding of the surface. As a further alternative, the surface may be configured to adopt a particular configuration directly in response to relative humidity of the fluid at the surface
Although figure 4 is discussed in relation to a fuel cell plate, it will be appreciated that similar surfaces may be advantageous in other fuel cell components. For example, the component may be a different fuel cell stack component such as a gas diffusion layer. Alternatively, the component may be a water separator, a heat exchanger, a pump or a fluid line of a fuel cell system.
An advantage of providing a switchable surface region with a hydrophobicity that varies in accordance with local conditions, as opposed to providing a region that is hydrophobic all of the time, is that a certain level of moisture, or hydration is required in order for efficient cell operation and so providing a permanent hydrophobic layer may cause the cell to dry out.
The surface 42 of the component 40 may comprise a plurality of reconfigurable surface regions in which there are first and second subsets of the plurality of reconfigurable surface regions. Each subset can comprise one or more reconfigurable surface regions. The first subset is configured to adopt the first state or the second state in response to the condition at the surface 42 meeting a first trigger. Similarly, the second subset is configured to adopt the first state or the second state in response to the condition at the surface 42 meeting a second trigger. All of the surface regions 44, 46 in figure 4 have the same type and level of trigger and so any division of these regions 44, 46 into first and second subsets results in the first subset having a first trigger that is both the same type and same level as a second trigger of the second subset. Alternatively, the first trigger may be different from the second trigger. The first trigger may be a different type to the second trigger. For example, the first trigger may be related to the ionic conductivity of fluid at the surface and the second trigger may be related to an electric field at the surface (or any other type of condition). If both the first trigger and the second trigger are related to the electric field, for example, then the triggers are of the same type. In the case where the triggers are of the same type, the first trigger may be at a different level than the second trigger. Where the first and second triggers are related to the electric field, the first trigger may have a level of 100 V.m"1 and the second trigger may have a level of 200 V.m"1. In this example, the first subset of reconfigurable surface regions may switch from the second state to the first state when the electric field at those regions falls below 100 V.m 1 and the second subset of reconfigurable surface regions may switch from the second state to the first state when the electric field at regions falls below 200 V.m"1.
In another example in which the first trigger is of the same type as the second trigger but the first and second triggers are at different trigger levels, the reconfigurable surface regions in the first and second subset may both be sensitive to the temperature at the surface. The state of the first subset may be set in response to the temperature passing 300 K and the state at the second subset may be set in response to the temperature passing 350 K.
Figures 5a and 5b show schematic views of a surface 50 having reconfigurable hydrophobicity. The surface is shown in a first state in figure 5a and in a second, less hydrophilic state in figure 5b. In both figures 5a and 5b the surface 50 comprises a bulk 52 and a layer of molecules 54a, 54b, 56 attached to the bulk 52. The layer of molecules 54a, 54b, 56 may be provided as a self-assembled monolayer. Each molecule 54a, 54b, 56 has a functional end group 56 and a chain 54a, 54b connecting the bulk 52 to the functional end group 56. The functional end group 56 is configured to attract or repel water molecules and also configured to be attracted to, or repelled from, the bulk depending upon a condition. In the example illustrated, the condition is the electric potential of the bulk 52 of the surface 50 and the functional end group 56 is a positively-charged hydrophilic ligand that exhibits an attractive force for water molecules. In other examples, the functional group may be chosen from elements or compounds that are known to exhibit an attraction or repulsion in response to a particular temperature or temperature gradient at the surface, or in response to a pH of a fluid at the surface, the relative humidity of the fluid at the surface, the pressure of the fluid at the surface, a compressive force applied to the surface or the chemistry of the fluid at the surface, including, for example a concentration of a particular ligand or ion at the surface. In this way, the surface 50 may be made to be responsive to a variety of conditions.
Examples of end groups for use in fuel cell applications include a benzyl end group, covalently bound to the substrate using diazonium chemistry; or pyridinium, benzyl ammonium or other positively-charged group attached to an unbound end of the alkyl chain; its positive charge conferring potential-dependent switching behaviour. An alkyl chain may be attached to the end group in a para position.
The presence of an electro-positive end group in a fuel cell environment may provide the additional benefit of absorbing any free anions which are present in the system, such as CI". Alternatively, the functional end group 56 may be a negative end group such as a hydrophilic carboxylate.
The chain 54a, 54b is resiliently flexible between a first configuration in the first state and a second configuration in the second state to allow the functional end group 56 to move relative to the bulk 52. In some examples, the chain is a molecule that is able to shift between isomer configurations depending upon the applied conditions. For example, the chain may adopt a trans-isomer in the first state and a cis-isomer in the second state.
The chain may itself be hydrophobic, such as a hydrophobic alkyl chain, in order to increase the variation in hydrophobicity between the first and second states. A preferred route for effecting a bond between the functional end group, or ligand, and the substrate of the surface is to form a covalent bond using diazonium chemistry. The layer of molecules 54a, 54b, 56 may also be provided as a self-assembled monolayer, such as a monolayer of (16-Mercapto)hexadecanoic acid (MHA). MHA self assembles on Au(111) and provides the reconfigurable surface properties.
Figure 5a illustrates a first state of the surface 50 in which the bulk is electropositive (carries a positive charge 58). In this example the functional end group 56 is also electropositive and so is repelled from the bulk 52. In the first state, the chain 54a is configured such that the functional end group 56 is provided distally from the bulk 52. The chain 54a is therefore orientated to enable interaction between the functional end group 56 and water molecules. The functional end group 56 exerts an attractive force on water molecules in this example and so the first state of the surface is hydrophilic.
The absolute sign of the electric field applied at the surface 50 does not necessarily need to change in order to cause a reorientation of the chain molecules between the first and second positions. Instead the sign of the potential may change with respect to a potential of zero charge (pzc) of the surface. The pzc of the surface, including switchable chain molecules, may be tuned so that it is at a trigger level intermediate between, for example, the potential of a flooded cell and a functioning fuel cell.
Figure 5b illustrates a second state of the surface 50 in which the bulk is less electropositive than the surface 50 in the first state, and so is relatively electronegative (illustrated as carrying a negative charge 60). The electropositive functional end group 56 is attracted to the bulk 52. In the second state, the chain 54b is configured such that the functional end group 56 is provided proximal to the bulk 52. The orientation of the chain 54b therefore inhibits interaction between the functional end group 56 and water molecules. The interaction between the functional end group 56 and water molecules is inhibited by shielding of the functional end group 56 from the water molecules by the chain 54b.
The surface 50 illustrated in figures 5a and 5b may be provided on a component of a fuel cell such as a fuel cell plate that is positively charged during operation. During normal
operation, a higher positive charge is present on the surface 50 than during impaired operation when the surface 50 is flooded. The surface 50 therefore adopts the first, hydrophilic state (illustrated in figure 5a) during normal operation and the second hydrophobic state (illustrated in figure 5b) during impaired operation. The adoption of a hydrophobic state counteracts the flooding that is impairing operation of the fuel cell. In this way, operational fuel cell may be automatically improved.
In some practical applications, the molecules may move through a range of conformations between the extremes shown in figures 5a and 5b. In such examples, the surface energy of the surface may vary continuously between first state and the second state. This property may be advantageous in fuel cell applications because it enables fine control of the movement of liquid water within the fuel cell system. In such examples a level of hydrophobicity may be provided by the reconfigurable surface in proportion to the level of water at the surface.
Claims
1. A component for a fuel cell system, the component having a surface region that is reconfigurable between at least a first state and a second state, wherein the first state is more hydrophilic than the second state and wherein the surface is configured to adopt the first state or the second state in accordance with a condition at the surface.
2. The component of claim 1 , wherein the condition is a water level at the surface.
3. The component of claim 2, wherein the surface region is configured to adopt the second state in response to an increase in the water level at the surface.
4. The component of claim 1 , wherein the condition is a current density, an electric field or electric potential at the surface.
5. The component of claim 1 , wherein the condition is a temperature or temperature gradient at the surface.
6. The component of claim 1 , wherein the condition is a pH of a fluid at the surface or a concentration of a ligand or ion at the surface.
7. The component of any preceding claim, wherein the component is one of: a gas diffusion layer, a fuel cell plate or a fluid flow plate configured to guide reactant over an active area of a fuel cell of the fuel cell system.
8. The component of any of claims 1 to 6, wherein the component is one of: a water separator, a heat exchanger, a pump or a fluid line.
9. The component of any preceding claim, wherein the surface region is dynamically reconfigurable during operation of the fuel cell system.
10. The component of any preceding claim, wherein the surface region has one or more further states in addition to the first and second states, each state having a different level of hydrophobicity to the other states.
11. The component of any preceding claim, wherein the surface region has a continuum of states between the first and second states.
12. The component of any preceding claim, comprising a plurality of independently reconfigurable surface regions.
13. The component of any preceding claim, wherein the plurality of independently reconfigurable surface regions comprises first and second subsets, wherein each subset comprises one or more reconfigurable surface regions, wherein the first subset is configured to adopt the first state or the second state in response to the condition at the surface meeting a first trigger, wherein the second subset is configured to adopt the first state or the second state in response to the condition at the surface meeting a second trigger and wherein the first trigger is different from the second trigger.
14. The component of claim 13, wherein the first trigger relates to a different type of condition to the second trigger.
15. The component of claim 13 or claim 14, wherein the first trigger is at a different level to the second trigger.
16. The component of any preceding claim, wherein a layer of molecules is attached to the surface, each molecule having a functional end group and a chain connecting the surface to the functional end group, wherein the functional end group is configured to attract or repel water molecules, wherein the chain is configurable such that:
in the first state the functional end group is provided distally from the surface for interacting with water molecules; and
in the second state the functional end group is provided proximal to the surface and inhibited from interacting with water molecules.
17. The component of claim 16, wherein the functional end group comprises a benzyl moiety, pyridinium or a carboxylate.
18. The component of claim 17, wherein the chain comprises an alkyl chain or glycol chain selected to have a different hydrophobicity to the functional end group.
19. The component of claim 16 or claim 7, wherein the chain comprises a trans- isomer in the first state and a cis-isomer in the second state.
20. A fuel cell system comprising the component of any preceding claim.
2 . A method of operating a fuel cell system comprising a component having a surface region with at least a first state and a second state, wherein the first state is more hydrophilic than the second state, the method comprising reconfiguring the surface to adopt the first state or the second state in accordance with a condition at the surface.
22. A component for a fuel cell system as described herein with reference to the accompanying figures.
23. A method of operating a fuel cell system as described herein with reference to the accompanying figures.
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GB1501932.6 | 2015-02-05 | ||
GB1501932.6A GB2535150A (en) | 2015-02-05 | 2015-02-05 | Component for a fuel cell system |
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030142901A1 (en) * | 2001-11-02 | 2003-07-31 | Joerg Lahann | Switchable surfaces |
US20080292940A1 (en) * | 2007-05-23 | 2008-11-27 | Gm Global Technology Operations, Inc. | Hydrophilic/hydrophobic patterned surfaces and methods of making and using the same |
US20110171564A1 (en) * | 2010-01-08 | 2011-07-14 | Gm Global Technology Operations, Inc. | Reversible superhydrophilic-superhydrophobic coating for fuel cell bipolar plates and method of making the same |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS61273871A (en) * | 1985-05-29 | 1986-12-04 | Fuji Electric Co Ltd | Matrix for fuel cell |
JP2006294294A (en) * | 2005-04-06 | 2006-10-26 | Dainippon Printing Co Ltd | Separator for solid polymer fuel cell and its manufacturing method |
JP2008034191A (en) * | 2006-07-27 | 2008-02-14 | Toyota Motor Corp | Manufacturing method for membrane-electrode assembly for fuel cell, and inspection method of catalyst grain for fuel cell |
-
2015
- 2015-02-05 GB GB1501932.6A patent/GB2535150A/en not_active Withdrawn
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2016
- 2016-02-04 WO PCT/GB2016/050266 patent/WO2016124937A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030142901A1 (en) * | 2001-11-02 | 2003-07-31 | Joerg Lahann | Switchable surfaces |
US20080292940A1 (en) * | 2007-05-23 | 2008-11-27 | Gm Global Technology Operations, Inc. | Hydrophilic/hydrophobic patterned surfaces and methods of making and using the same |
US20110171564A1 (en) * | 2010-01-08 | 2011-07-14 | Gm Global Technology Operations, Inc. | Reversible superhydrophilic-superhydrophobic coating for fuel cell bipolar plates and method of making the same |
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