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The present invention relates to fuel cells and components used within a fuel cell. Heat transfer appendages are described that improve fuel cell thermal management. Each heat transfer appendage is arranged on an external portion of a bi-polar plate and permits conductive heat transfer between inner

The present invention relates to fuel cells and components used within a fuel cell. Heat transfer appendages are described that improve fuel cell thermal management. Each heat transfer appendage is arranged on an external portion of a bi-polar plate and permits conductive heat transfer between inner portions of the bi-polar plate and outer portions of the bi-polar plate proximate to the appendage. The heat transfer appendage may be used for heating or cooling inner portions of a fuel cell stack. Improved thermal management provided by cooling the heat transfer appendages also permits new channel field designs that distribute the reactant gases to a membrane electrode assembly. Flow buffers are described that improve delivery of reactant gases and removal of reaction products. Single plate bi-polar plates may also include staggered channel designs that reduce the thickness of the single plate.

대표청구항 ▼

What is claimed is: 1. A fuel cell for producing electrical energy, the fuel cell comprising: a fuel cell stack including a) a set of single plate solid metal substrate bi-polar plates, each bi-polar plate in the fuel cell stack comprising i) a first channel field disposed on a first face of the bi

What is claimed is: 1. A fuel cell for producing electrical energy, the fuel cell comprising: a fuel cell stack including a) a set of single plate solid metal substrate bi-polar plates, each bi-polar plate in the fuel cell stack comprising i) a first channel field disposed on a first face of the bi-polar plate and including a set of channels configured to distribute hydrogen, ii) a second channel field disposed on a second face of the bi-polar plate and including a second set of channels configured to distribute oxygen, wherein a channel included in the first channel field has an overlapping channel depth that extends past a channel depth for a channel included in the second channel field, iii) a first manifold that extends through the bi-polar plate from the first face to the second face and configured to deliver a gas to the first channel field or receive a gas from the first channel field; iv) a first flow buffer formed as a trough into the first face of the bi-polar plate and configured to receive a first gaseous flow from a first channel in the first set of channels and a second gaseous flow from a second channel in the first set of channels and to output the first and second gaseous flows in the first set of channels to a third channel in the first set of channels, wherein the flow buffer is configured to reduce a pressure difference between the first and second gaseous flows in the first set of channels before outputting the first and second gaseous flows to the third channel in the first set of channels; v) a second flow buffer formed as a trough into the second face of the bi-polar plate, positioned at least partially opposite to the first flow buffer formed into the first face of the bi-polar plate, and configured to receive a first gaseous flow from a first channel in the second set of channels and a second gaseous flow from a second channel in the second set of channels and to output the first and second gaseous flows in the second set of channels to a third channel in the second set of channels, wherein the second flow buffer is configured to reduce a pressure difference between the first and second gaseous flows in the second set of channels before outputting the first and second gaseous flows to the third channel in the second set of channels, and b) a membrane electrode assembly disposed between two bi-polar plates, the membrane electrode assembly including a hydrogen catalyst, an oxygen catalyst and an ion conductive membrane that electrically isolates the hydrogen catalyst from the oxygen catalyst. 2. The fuel cell of claim 1 further comprising a heat transfer appendage arranged outside the first channel field and in conductive thermal communication with the solid metal substrate bi-polar plate wherein the heat transfer appendage is configured to sink heat from the substrate between the first channel field and the second channel field to the heat transfer appendage in a direction parallel to the first face. 3. The fuel cell of claim 2 wherein the heat transfer appendage has a smaller thickness than a thickness for the substrate between the first face and the second face. 4. The fuel cell of claim 2 wherein adjacent bi-polar plates in the fuel cell stack are arranged such that heat transfer appendages on the adjacent bi-polar plates form a channel for a heat or cooling media to pass through. 5. The fuel cell of claim 2 wherein the heat transfer appendage comprises a material common to the substrate. 6. The fuel cell of claim 4 wherein the heat transfer appendage is integral with the substrate. 7. The fuel cell of claim 2 wherein the heat transfer appendage is arranged on a side or edge of the bi-polar plate. 8. The fuel cell of claim 2 wherein the heat transfer appendage substantially spans a side of the bi-polar plate that does not include an intake or output manifold. 9. The fuel cell of claim 1 wherein the substrate comprises a thermal conductance greater than 1W/mK. 10. The fuel cell of claim 1 wherein a bi-polar plate in the stack comprises a coating that increases electrical conductance of the bi-polar plate. 11. The fuel cell of claim 10 wherein the substrate is coated with an electrically conductive metal alloy, ceramic alloy or polymeric material. 12. The fuel cell of claim 10 wherein a bi-polar plate comprises a planar electrical resistance less than about 100 mOhm cm2. 13. The fuel cell of claim 1 wherein the first channel field is configured to distribute hydrogen to a gas distribution layer included in a membrane electrode assembly that includes the hydrogen catalyst. 14. The fuel cell of claim 13 wherein the second channel field is configured to distribute oxygen to a gas distribution layer included in the membrane electrode assembly that includes the oxygen catalyst. 15. The fuel cell of claim 14 wherein the second channel field is configured to distribute oxygen in a direction that counters a direction of hydrogen distribution by the first channel field. 16. The fuel cell of claim 15 wherein the second channel field is configured to distribute oxygen in parallel to the gas distribution layer that includes the oxygen catalyst. 17. The fuel cell of claim 1 wherein the fuel cell is configured to generate less than about 200 watts. 18. The fuel cell of claim 1 wherein a first bi-polar plate and a second bi-polar plate in the set of bi-polar plates each include a different manifold arrangement. 19. A fuel cell for producing electrical energy, the fuel cell comprising: a fuel cell stack including a) a set of single plate solid metal substrate bi-polar plates, each bi-polar plate comprising: i) a first channel field disposed on a first face of the substrate and a second channel field disposed on a second face of the substrate, the first channel field including a set of channels configured to distribute fuel and the second channel field including a second set of channels configured to distribute oxidant, ii) a first manifold that extends through the bi-polar plate from the first face to the second face and configured to deliver a gas to the first channel field or receive a gas from the first channel field; iii) a first manifold channel that opens to the first manifold on the second face, the first manifold channel traversing the substrate from the first face to the second face, and configured to communicate gas between the first manifold on the second face and the first channel field on the first face, wherein the first manifold channel of a first bi-polar plate is offset laterally from the first manifold channel of a second adjacent bi-polar plate such that the first manifold channels of the first and second bi-polar plates do not substantially align; iv) a first flow buffer formed as a trough into the substrate on the first face and configured to receive a first gaseous flow from a first channel in the first set of channels and a second gaseous flow from a second channel in the first set of channels and to output the first and second gaseous flows in the first set of channels to a third channel in the first set of channels, wherein the flow buffer is configured to reduce a pressure difference between the first and second gaseous flows in the first set of channels before outputting the first and second gaseous flows to the third channel in the first set of channels; v) a second flow buffer formed as a trough into the substrate on the second face and configured to receive a first gaseous flow from a first channel in the second set of channels and a second gaseous flow from a second channel in the second set of channels and to output the first and second gaseous flows in the second set of channels to a third channel in the second set of channels, wherein the second flow buffer is configured to reduce a pressure difference between the first and second gaseous flows in the second set of channels before outputting the first and second gaseous flows to the third channel in the second set of channels, and vi) a non-porous heat transfer appendage in conductive thermal communication with the substrate and arranged outside the first and second channel fields and b) a membrane electrode assembly disposed between two bi-polar plates, the membrane electrode assembly including an anode catalyst, a cathode catalyst and an ion conductive membrane that electrically isolates the anode catalyst from the cathode catalyst. 20. The fuel cell of claim 19 wherein the heat transfer appendage is configured to sink heat from the substrate between the first channel field and the second channel field to the heat transfer appendage in a direction parallel to the first face. 21. The fuel cell of claim 19 wherein the heat transfer appendage has a smaller thickness than a thickness for the substrate between the first face and the second face. 22. The fuel cell of claim 19 wherein adjacent bi-polar plates in the fuel cell stack are arranged such that heat transfer appendages on the adjacent bi-polar plates form a channel for a heat or cooling medium to pass through. 23. The fuel cell of claim 19 wherein the heat transfer appendage is integral with the substrate. 24. The fuel cell of claim 19 wherein the heat transfer appendage is ananged on a side or edge of the plate. 25. The fuel cell of claim 19 wherein the heat transfer appendage substantially spans a side of the bi-polar plate that does not include an intake or output manifold. 26. The fuel cell of claim 19 wherein the substrate comprises a thermal conductance greater than 1W/mK. 27. The fuel cell of claim 19 wherein the fuel cell includes more than ten membrane electrode assembly layers and has an overall package thickness less than one centimeter. 28. The fuel cell of claim 19 wherein the first bi-polar plate and the second bi-polar plate each include a different manifold arrangement. 29. The fuel cell of claim 19 further comprising: a thermal catalyst disposed in contact with or in proximity to the non-porous heat transfer appendage and that generates heat with exposure to a heating medium. 30. The fuel cell of claim 29 wherein the thermal catalyst is disposed on the one or more heat transfer appendages of the bi-polar plates. 31. The fuel cell of claim 29 wherein the heat transfer appendage has a smaller thickness than a thickness of the substrate between the first face and the second face. 32. The fuel cell of claim 29 wherein the thermal catalyst is packed in the vicinity of the heat transfer appendage. 33. The fuel cell of claim 29 wherein the heating medium comprises a hydrocarbon fuel source provided to a fuel processor that separates hydrogen from the hydrocarbon fuel source and provides the hydrogen to the fuel cell. 34. The fuel cell of claim 33 wherein the hydrocarbon fuel source is routed from an exhaust of a fuel processor. 35. The fuel cell of claim 29 wherein the thermal catalyst comprises platinum. 36. The fuel cell of claim 29 wherein the heat transfer appendage is configured to sink heat from substrate between the first channel field and the second channel field to the heat transfer appendage in a direction parallel to the first face. 37. The fuel cell of claim 19 wherein the fuel cell is a direct methanol fuel cell and the fuel comprises liquid methanol. 38. The fuel cell of claim 29 further comprising: a second manifold that extends through the bi-polar plate from the first face to the second face and configured to deliver a gas to the second channel field or receive a gas from the second channel field; a second manifold channel that opens to the second manifold on the first face, traverses the bi-polar plate from the second face to the first face, and is configured to communicate gas between the second manifold on the first face and the second channel field on the second face; a first sealing area on the first face that peripherally surrounds each of the first channel field, the first manifold and the second manifold on the first face, thereby isolating them from each other, whereby the first sealing area extends between and isolates a portion of the second manifold channel on the first face from the first channel field, and the first sealing area further extends between and isolates a portion of the first manifold channel on the first face from the first manifold; and a second sealing area on the second face that peripherally surrounds each of the second channel field, the first manifold and the second manifold on the second face, thereby isolating them from each other, whereby the second sealing area extends between and isolates a portion of the first manifold channel on the second face from the second channel field, and the second sealing area further extends between and isolates a portion of the second manifold channel on the second face from the second manifold; wherein the non-porous heat transfer appendage is arranged laterally external to the first and second sealing areas.