Claims
- 1. An electrically conductive, fuel cell fluid flow field plate comprising:
(a) a first major surface; (b) a second major surface, opposite to said first major surface; and (c) at least one substantially straight channel formed in said first major surface, wherein said at least one channel has an open width less than about 0.75 millimeter and a length that extends substantially between two opposing edges of said fluid flow field plate.
- 2. The fluid flow field plate of claim 1 wherein said fuel cell is a solid polymer fuel cell.
- 3. The fluid flow field plate of claim 1 wherein said plate comprises a plurality of substantially straight parallel channels separated by lands, wherein each of said plurality of channels has an open width less than about 0.75 millimeter and extends substantially between two opposing edges of said fluid flow field plate.
- 4. The fluid flow field plate of claim 3 wherein each one of said plurality of channels has about the same length.
- 5. The fluid flow field plate of claim 3 wherein each one of said plurality of channels having an open width of less than about 0.75 millimeter has an open width of about 0.5 millimeter.
- 6. The fluid flow field plate of claim 3 wherein each one of said lands comprises a substantially flat surface parallel to the plane of said first major surface.
- 7. The fluid flow field plate of claim 6 wherein said lands have rounded edges with a radius of curvature of at least 0.15 millimeter next to adjacent ones of said channels.
- 8. The fluid flow field plate of claim 3 wherein each one of said lands comprises a convex ridge.
- 9. The fluid flow field plate of claim 3 wherein at least one of said lands has a flat surface with a width between about 0.5 millimeter and 0.9 millimeter.
- 10. The fluid flow field plate of claim 3 wherein the thickness of said flow field plate is no greater than about 0.8 millimeter.
- 11. The fluid flow field plate of claim 9 wherein said at least one channel has a maximum depth of about 0.4 millimeter.
- 12. The fluid flow field plate of claim 3 further comprising at least one channel formed in said second major surface.
- 13. The fluid flow field plate of claim 11 wherein the thickness of said flow field plate is no greater than about 1.1 millimeters.
- 14. The fluid flow field plate of claim 12 wherein at least one of said plurality of parallel substantially straight channels has a depth of about 0.25 millimeter and said second channel has a depth of about 0.4 millimeter.
- 15. The fluid flow field plate of claim 3 wherein at least one of said plurality of parallel substantially straight channels has a substantially semicircular cross-sectional area with a radius less than about 0.4 millimeter.
- 16. The fluid flow field plate of claim 3 wherein at least one of said plurality of parallel substantially straight channels has a substantially semicircular cross-sectional area with a radius of less than about 0.25 millimeter.
- 17. The fluid flow field plate of claim 3 wherein at least one of said plurality of channels has a flat base and opposing side walls diverging outwardly from said base towards said open width.
- 18. The fluid flow field plate of claim 3 wherein said fluid flow field plate comprises expanded graphite.
- 19. The fluid flow field plate of claim 18 wherein said plate is impregnated with a resin.
- 20. The fluid flow field plate of claim 3 wherein said fluid flow field plate has a web thickness between about 0.35 millimeter and about 0.6 millimeter.
- 21. The fluid flow field plate of claim 3 wherein said fluid flow field plate has a web thickness of about 0.4 millimeter.
- 22. An electrically conductive, fuel cell fluid flow field plate comprising:
(a) a first major surface; (b) a second major surface, opposite to said first major surface; and (c) a plurality of parallel, substantially straight channels formed in at least one of said first and second major surfaces, wherein at least one of said plurality of channels has a length to cross-sectional area ratio of between about 2180:1 to about 6200:1.
- 23. The fluid flow field plate of claim 22 wherein each one of said plurality of channels has a length to cross-sectional area ratio of about 2190:1.
- 24. The fluid flow field plate of claim 22 wherein each one of said plurality of channels has a length to cross-sectional area ratio of about 6180:1.
- 25. The fluid flow field plate of claim 22 wherein said plurality of channels define a channel area having a length to width ratio greater than about 3:1 and less than 48:1.
- 26. The fluid flow field plate of claim 24 wherein said length to width ratio is about 12:1.
- 27. An electrochemical fuel cell comprising:
(a) a fuel flow field plate comprising:
(1) a first major surface; (2) a second major surface, opposite to said first major surface; and (3) at least one substantially straight channel formed in said first major surface, wherein said at least one channel has an open width less than about 0.75 millimeter and a length that extends substantially between two opposing edges of said fluid flow field plate. (b) an oxidant flow field plate with opposing first and second major surfaces; and (c) a membrane electrode assembly interposed between said first major surfaces of said fuel and oxidant flow field plates.
- 28. The electrochemical fuel cell of claim 27 wherein said at least one fuel channel is one of a plurality of parallel fuel channels separated by lands.
- 29. The electrochemical fuel cell of claim 28 wherein at least one of said plurality of fuel channels has a width of about 0.5 millimeter.
- 30. The electrochemical fuel cell of claim 28 wherein said membrane electrode assembly has a thickness of less than about 0.35 millimeter.
- 31. The electrochemical fuel cell of claim 28 further comprising a plurality of parallel straight oxidant channels formed in said first major surface of said oxidant flow field plate, and said plurality of oxidant channels extend from an oxidant inlet to an oxidant outlet, wherein at least one of said plurality of oxidant channels has an open width less than about 0.85 millimeter.
- 32. The electrochemical fuel cell of claim 31 wherein said plurality of fuel channels are oriented parallel to said plurality of oxidant channels.
- 33. The electrochemical fuel cell of claim 31 wherein each one of said plurality of oxidant channels has an open width of about 0.85 millimeter.
- 34. The electrochemical fuel cell of claim 31 wherein each of said lands separating adjacent ones of said plurality fuel channels, has a width of about 0.85 millimeter and wherein each of said lands separating adjacent ones of said plurality of oxidant channels has a width of about 0.5 millimeter.
- 35. The electrochemical fuel cell of claim 31 wherein the center of each of said plurality of fuel channels is aligned with the center of one of said plurality of oxidant channels.
- 36. The electrochemical fuel cell of claim 27 wherein said fuel cell is one of a plurality of fuel cells arranged in a stack and coolant channels are provided between said second major surfaces of adjacent ones of said fuel and oxidant flow field plates.
- 37. The electrochemical fuel cell of claim 36 wherein said coolant channels are formed in one of said second major surfaces of said fuel and oxidant flow field plates.
- 38. The electrochemical fuel cell of claim 31 wherein said fuel cell is oriented such that said oxidant and fuel channels are substantially horizontal for draining, in the direction of the fluid flow, liquids which may accumulate within said channels.
- 39. The electrochemical fuel cell of claim 31 wherein said oxidant and fuel channels have a length of about 600 millimeters.
- 40. The electrochemical fuel cell of claim 36 further comprising internal fuel and oxidant internal manifolds formed by aligned and fluidly sealed openings provided in said fuel flow field plate, said oxidant flow field plate and said membrane electrode assembly.
- 41. The electrochemical fuel cell of claim 40 wherein said fuel and oxidant manifolds extend substantially horizontally through said stack.
- 42. The electrochemical fuel cell of claim 41 wherein each one of said fuel manifolds has a low point which is lower than a lowest one of said fuel channels and each one of said oxidant manifolds has a low point which is lower than a lowest one of said oxidant channels.
- 43. An electrochemical fuel cell comprising:
(a) a fuel flow field plate comprising:
(1) a first major surface; (2) a second major surface, opposite to said first major surface; and (3) a plurality of parallel substantially straight fuel channels formed in said first major surface wherein said at least one channel has an open width less than about 0.75 millimeter and a length that extends substantially between two opposing edges of said fluid flow field plate, of said fuel flow field plate, said fuel channels extending from a fuel inlet to a fuel outlet; (b) an oxidant flow field plate comprising:
(1) a first major surface; (2) a second major surface, opposite to said first major surface; and (3) a plurality of parallel substantially straight oxidant channels formed in said first major surface wherein said at least one channel has an open width less than about 0.75 millimeter and a length that extends substantially between two opposing edges of said fluid flow field plate, of said oxidant flow field plate, said oxidant channels extending from an oxidant inlet to an oxidant outlet; (c) a membrane electrode assembly interposed between said first major surfaces of said fuel and oxidant flow field plates; wherein operating said fuel cell at a current density greater than about 500 mA/cm2 creates a pressure differential between the inlets and outlets of said oxidant and fuel channels of between about 138 millibars and about 400 millibars.
- 44. A method of making the fluid flow field plate of claim 1, said method comprising:
(a) providing a sheet of compressible, electrically conductive sheet material having two oppositely facing major surfaces; and (b) embossing said first major surface to form said at least one open-faced channel.
- 45. The method of claim 44 wherein a roller embossing machine is used to emboss said sheet material.
- 46. The method of claim 45 wherein said roller embossing machine further comprises cutters mounted on a roller for cutting said sheet to a desired shape.
- 47. The method of claim 44 wherein said sheet comprises expanded graphite.
- 48. The method of claim 47 further comprising impregnating said sheet with a resin after embossing.
- 49. The method of claim 44 further comprising forming at least one opening in said sheet and forming a fluid passage between said opening and said channel.
- 50. The method of claim 44 wherein said embossing compresses said sheet such that the thinnest portions of said sheet have a web thickness of between about 0.35 millimeter and 0.6 millimeter.
- 51. A method of making the fluid flow field plate of claim 1, said method comprising:
(a) providing a mold for forming said plate wherein said mold provides channels on a major surface of said plate and sealing areas which circumscribe an area defined by said channels; (b) depositing an electrically conductive material into said mold; (c) molding said electrically conductive material until it is molded into the shape defined by said mold; and (d) removing a molded plate from said mold.
- 52. The method of claim 51 wherein said electrically conductive material is a composite material comprising carbon or graphite.
- 53. The method of claim 51 wherein said molding process is a compression molding process.
- 54. The method of claim 51 wherein said molding process is an injection molding process.
- 55. The method of claim 54 wherein said electrically conductive material comprises a thermosetting resin.
- 56. The method of claim 54 wherein said electrically conductive material comprises a thermoplastic resin.
CROSS-REFERENCE TO RELATED APPLICATION(S)
[0001] The present application is a continuation of U.S. patent application Ser. No. 09,223,356 filed Dec. 30, 1998 entitled “Fuel Cell Fluid Flow Field Plate and Methods of Making Fuel Cell Flow Field Plates”, which is hereby incorporated by reference herein in its entirety.
Continuations (1)
|
Number |
Date |
Country |
Parent |
09223356 |
Dec 1998 |
US |
Child |
09999510 |
Oct 2001 |
US |