Flow field plate assembly for an electrochemical fuel cell
AssigneeBallard Power Systems Inc.
InventorsPeter R. Gibb, Neil V. Davis, Emerson R. Gallagher
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AssigneeBallard Power Systems Inc.
InventorsPeter R. Gibb, Neil V. Davis, Emerson R. Gallagher
Estimating the term…
A flow field plate assembly for an electrochemical fuel cell comprises two flow field plates, each of which has channels formed on an inner surface of the plate. The plates are alignable with and engage each other such that their cooperating inner surfaces form at least one inner coolant fluid channel. The coolant channel has an essentially constant cross-sectional perimeter along its length, which is defined by the perimeters of the channels of the two plates and their difference in width at the cooperating plate surfaces. Additionally, a flow field plate assembly, which comprises a corrugated flow field plate and a staggered flow field plate, is structurally stronger under compressive load during the fuel cell operation.
A fuel cell flow field plate assembly comprising:
A method of making a flow field plate assembly comprising aligning and engaging the inner surface of a first flow field plate having an open inner channel formed thereon with the inner surface of a second flow field plate having an open inner channel formed thereon, whereby the engaged inner channels of each plate define a closed inner flow field channel such that the inner channel of the second plate overlaps the inner channel of the first plate essentially along its entire length.
A fuel cell flow field plate assembly comprising:
A method of making a flow field plate assembly comprising aligning and engaging the inner surface of a first corrugated flow field plate with the inner surface of a second staggered flow field plate, each of the inner surfaces having channels formed thereon, whereby the inner surface channels of each plate define a closed inner flow field, and whereby the staggered second flow field plate supports the first flow field plate against spreading under compressive load.
Dependencies are inferred from the claim text.
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Characterised by the form: corrugated or undulated
Collectors; Separators, e.g. bipolar separators; Interconnectors: characterised by the configuration of channels, e.g. by the flow field of the…
Characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant: characterised by grooves, e.g. their pitch or depth
Collectors; Separators, e.g. bipolar separators; Interconnectors: having heating or cooling means, e.g. heaters or coolant flow channels
Term end not estimated
The present invention relates to a flow field plate assembly for fuel cells. More particularly, the invention relates to a flow field plate assembly comprising two flow field plates that engage each other on their inner surfaces such that each inner channel on the inner surface of one plate overlaps an inner channel on the inner surface of the other plate essentially along its entire length. The present invention also relates to a flow field plate assembly comprising two flow field plates, one supporting the other against spreading under compressive load.
Fuel cell systems are currently being developed for numerous applications, such as automobiles and stationary power plants, where they will be used to economically deliver power with significant environmental benefits.
Preferred fuel cell types include solid polymer fuel cells that comprise a solid polymer electrolyte, otherwise referred to as an ion exchange membrane, and operate at relatively low temperatures. The membrane is disposed between two electrodes, namely a cathode and an anode, forming a membrane electrode assembly (“MEA”). Each electrode contains a catalyst layer, comprising an appropriate catalyst, located next to the solid polymer electrolyte. The catalyst induces the desired electrochemical reactions at the electrodes. During normal operation of a solid polymer electrolyte fuel cell, fuel is electrochemically oxidized at the anode catalyst, typically resulting in the generation of protons, electrons, and possibly other species depending on the fuel employed. The protons are conducted from the reaction sites at which they are generated, through the electrolyte, to electrochemically react with the oxidant at the cathode catalyst. The electrons pass through an external circuit, creating a flow of electricity.
FIG. 1 is an exploded side view of a conventional fuel cell assembly, showing one membrane electrode assembly and the corresponding reactant and coolant fluid flow field plates.
FIG. 2 is a perspective view of a flow field plate assembly showing two flow field plates aligned and assembled together in accordance with the present disclosure.
FIG. 3 is a cross-sectional view of the first flow field plate of FIG. 2.
FIG. 1 illustrates a conventional fuel cell assembly. For simplicity, a single cell, from a fuel cell stack is represented. It is to be understood that this represents a repeating unit of the fuel cell stack.
This repeating unit 1 includes one membrane electrode assembly (MEA) 2 interposed between a flow field plate 3 and a flow field plate in an adjacent unit (not shown), similar to plate 4. The MEA comprises a solid polymer ion exchange membrane 5 sandwiched between an anode 6 and a cathode 7. The anode 6 and cathode 7 each contain a fluid diffusion layer 8 and 9 respectively and a catalyst layer 10 and 11 respectively, on the sides facing the membrane 5. Fluid distribution layers 8 and 9 serve as electrically conductive backings and mechanical supports for catalyst layers 10, 11, but fluid distribution layers 8 and 9 also serve to distribute the reactants from the flow field plates to the catalyst layer. The reactants, typically hydrogen and oxygen or oxygen-containing air, are supplied to the flow field plates 3 and 4 and then delivered through the fluid distribution channels 13 and 12 of the flow fields to the surfaces of the fluid distribution layers 8 and 9.
As shown in FIG. 1 the flow field plate 4 contains channels 14 on the side facing the flat surface 15 of the flow field plate 3. The cooperating sides of the channel 14 and the flat surface 15 form a closed inner flow field channel for carrying a coolant fluid, typically water.