Granted Patent B2

US 7,332,240 · App. 10/628,318 · Granted Feb 19, 2008

Abstract

Claims (110)

1. A device configured to convert a hydrogenous fuel source to electrical energy, said device comprising:

an electrochemical conversion assembly configured to partition said device into first and second flow field regions;

a first reactant input and a first product output in communication with said first flow field region;

a first diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said first flow field region and said electrochemical conversion assembly;

a second reactant input and a second product output in communication with said second flow field region; and

a second diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said second flow field region and said electrochemical conversion assembly, wherein

said device is configured such that at least one of said first and second diffusion media comprise a region subject to relatively high H 2 O concentrations and a region subject to relatively low H 2 O concentrations,

a mesoporous layer is carried along at least a portion of a major face of one of said first and second diffusion media substrates and comprises a hydrophilic carbonaceous component and a hydrophobic component, and

said mesoporous layer occupies a substantially greater portion of one of said high H 2 O region and said low H 2 O region relative to the other of said high H 2 O region and said low H 2 O region, wherein

(1) at least one of said first and second diffusion media substrate comprises an increased thickness portion and a reduced thickness portion and said mesoporous layer is carried along only said reduced thickness portion of at least one of said first and second diffusion media substrates and/or (2) said mesoporous layer at least partially infiltrates at least one of said first and second diffusion media substrates to a depth of greater than zero μm to about 10 μm in said high H 2 O regions and a depth of greater than 0 μm to about 25 μm in said low H 2 O regions; and

said hydrophilic carbonaceous component comprises a moderate surface area carbon characterized by mean particle size of between about 15 nm and about 70 nm in said high H 2 O regions.

2. A device as claimed in claim 1 wherein said mesoporous layer is substantially confined to one of said high H 2 O region and said low H 2 O region.

3. A device as claimed in claim 1 wherein said mesoporous layer is configured to enhance H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer.

4. A device as claimed in claim 1 wherein said mesoporous layer occupies a substantially greater portion of said high H 2 O region.

5. A device as claimed in claim 1 wherein said mesoporous layer occupies a substantially greater portion of said high H 2 O region and is configured to enhance H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer.

6. A device as claimed in claim 1 wherein said mesoporous layer is configured to diminish H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer.

7. A device as claimed in claim 6 wherein said mesoporous layer occupies a substantially greater portion of said low H 2 O region.

8. A device as claimed in claim 1 wherein said mesoporous layer occupies a substantially greater portion of said low H 2 O region and is configured to diminish H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer.

9. A device as claimed in claim 1 wherein:

said electrochemical conversion assembly defines an anode side of said device and a cathode side of said device;

said first reactant input and said first product output are in communication with said anode side of said device;

said second reactant input and said second product output are in communication with said cathode side of said device.

10. A device as claimed in claim 9 wherein:

said mesoporous layer is configured to enhance H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer;

said region subject to relatively high H 2 O concentrations is proximate said second product output in communication with said cathode side of said device; and

said mesoporous layer occupies a substantially greater portion of said high H 2 O region proximate said second product output.

11. A device as claimed in claim 9 wherein:

said mesoporous layer is configured to enhance H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer;

said region subject to relatively high H 2 O concentrations is configured to allow said first reactant input in communication with said anode side of said device to flow through said region of high H 2 O concentration; and

said mesoporous layer occupies a substantially greater portion of said high H 2 O region proximate said first reactant input.

12. A device as claimed in claim 9 wherein:

said mesoporous layer is configured to diminish H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer;

said region subject to relatively low H 2 O concentrations is proximate said second reactant input in communication with said cathode side of said device; and

said mesoporous layer occupies a substantially greater portion of said low H 2 O region proximate said second reactant input.

13. A device as claimed in claim 9 wherein:

said mesoporous layer is configured to diminish H 2 O transfer properties of at least one of said first and second diffusion media substrates along said portion of said major face occupied by said mesoporous layer;

said region subject to relatively low H 2 O concentrations is configured to allow said first product output in communication with said anode side of said device to flow through said region of low H 2 O concentration; and

said mesoporous layer occupies a substantially greater portion of said low H 2 O region.

14. A device as claimed in claim 1 wherein a plurality of said mesoporous layers are carried along respective portions of a major face of one of said first and second diffusion media substrates.

15. A device as claimed in claim 14 wherein:

a mesoporous layer configured to enhance H 2 O transfer properties of at least one of said first and second diffusion media substrates occupies a substantially greater portion of said high H 2 O region; and

a mesoporous layer configured to diminish H 2 O transfer properties of said diffusion media substrate occupies a substantially greater portion of said low H 2 O region.

16. A device as claimed in claim 1 wherein a difference in thickness of said substrate introduced said reduced thickness portion of said substrate is sufficient to accommodate for an increase in diffusion media thickness introduced by said mesoporous layer.

17. A device as claimed in claim 1 wherein said diffusion media substrates comprises a carbonaceous fibrous matrix.

18. A device as claimed in claim 1 wherein said hydrophobic component of said mesoporous layer comprises a fluorinated polymer.

19. A device as claimed in claim 1 wherein said hydrophilic carbonaceous component of said mesoporous layer is selected from carbon black, graphite, carbon fibers, carbon fullerenes, carbon nanotubes, and combinations thereof.

20. A device as claimed in claim 1 wherein said moderate surface area carbon is characterized by a surface area of between about 60 m 2 /g and about 300 m 2 /g.

21. A device as claimed in claim 1 wherein said hydrophilic carbonaceous component comprises a high surface area carbon characterized by a surface area of above about 750 m 2 /g and a mean particle size of less than about 20 nm in said low H 2 O regions.

22. A device as claimed in claim 1 wherein said mesoporous layer comprises about 80 wt % of said carbonaceous component in said high H 2 O region.

23. A device as claimed in claim 1 wherein said mesoporous layer comprises between about 75 wt % and about 85 wt % of said carbonaceous component in said high H 2 O region.

24. A device as claimed in claim 1 wherein said mesoporous layer comprises between about 90 wt % and about 95 w % of said carbonaceous component in said low H 2 O region.

25. A device as claimed in claim 1 wherein said mesoporous layer defines a thickness of from greater than 0 μm to about 20 μm in said high H 2 O regions.

26. A device as claimed in claim 1 wherein said mesoporous layer defines a thickness of between about 10 μm and about 40 μm in said low H 2 O regions.

27. A device as claimed in claim 1 wherein said mesoporous layer infiltrates at least one of said first and second diffusion media substrates to a depth of from greater than 0 μm to about 10 μm in said high H 2 O regions.

28. A device as claimed in claim 1 wherein said mesoporous layer infiltrates at least one of said first and second diffusion media substrates to a depth of from greater than 0 μm to about 25 μm in said low H 2 O regions.

29. A device as claimed in claim 1 wherein said device comprises a fuel cell.

30. A device as claimed in claim 29 wherein said device further comprises structure defining a vehicle powered by said fuel cell.

31. A device configured to convert a hydrogenous fuel source to electrical energy, said device comprising:

an electrochemical conversion assembly configured to partition said device into first and second flow field regions;

a first reactant input and a first product output in communication with said first flow field region;

a first diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said first flow field region and said electrochemical conversion assembly;

a second reactant input and a second product output in communication with said second flow field region; and

a second diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said second flow field region and said electrochemical conversion assembly, wherein

said device is configured such that at least one of said first and second diffusion media comprise a region subject to relatively high H 2 O concentrations and a region subject to relatively low H 2 O concentrations,

a mesoporous layer is carried along at least a portion of a major face of one of said first and second diffusion media substrates and comprises a hydrophilic carbonaceous component and a hydrophobic component,

at least one of said first and second diffusion media substrates comprises a relatively high porosity region and a relatively low porosity region,

said relatively high porosity region of said substrate occupies a substantially greater portion of said high H 2 O region and said relatively low porosity region of said substrate occupies a substantially greater portion of said low H 2 O region,

wherein

(1) at least one of said first and second diffusion media substrate comprises an increased thickness portion and a reduced thickness portion and said mesoporous layer is carried along only said reduced thickness portion of at least one of said first and second diffusion media substrates and/or (2) said mesoporous layer at least partially infiltrates at least one of said first and second diffusion media substrates to a depth of greater than zero μm to about 10 μm in said high H 2 O regions and a depth of greater than 0 μm to about 25 μm in said low H 2 O regions; and

said hydrophilic carbonaceous component comprises a moderate surface area carbon characterized by mean particle size of between about 15 nm and about 70 nm in said high H 2 O regions.

32. A device as claimed in claim 31 wherein said relatively high porosity region is characterized by a porosity of up to about 90%.

33. A device as claimed in claim 31 wherein said relatively low porosity region is characterized by a porosity of between about 70% and about 75%.

34. A device as claimed in claim 31 wherein said substrate is characterized by a porosity of above about 70% in said high H 2 O regions.

35. A device as claimed in claim 31 wherein said substrate is characterized by a porosity of between about 70% and about 75% in said low H 2 O regions.

36. A device as claimed in claim 31 wherein said substrate defines a thickness of between about 100 μm and about 300 μm in said high H 2 O regions.

37. A device as claimed in claim 31 wherein said substrate defines a thickness of between about 190 μm and about 300 μm in said low H 2 O regions.

38. A device as claimed in claim 31 wherein said substrate is characterized by a mean pore size of above about 20 μm in said high H 2 O regions.

39. A device as claimed in claim 31 wherein said substrate is characterized by a mean pore size of less than about 25 μm in said low H 2 O regions.

40. A device configured to convert a hydrogenous fuel source to electrical energy, said device comprising:

an electrochemical conversion assembly configured to partition said device into first and second flow field regions;

a first reactant input and a first product output in communication with said first flow field region;

a first diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said first flow field region and said electrochemical conversion assembly;

a second reactant input and a second product output in communication with said second flow field region; and

a second diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said second flow field region and said electrochemical conversion assembly, wherein

said device is configured such that at least one of said first and second diffusion media comprise a region subject to relatively high H 2 O concentrations and a region subject to relatively low H 2 O concentrations,

a mesoporous layer is carried along at least a portion of a major face of one of said first and second diffusion media substrates and comprises a hydrophilic carbonaceous component and a hydrophobic component,

said mesoporous layer occupies portions of said high H 2 O region and said low H 2 O region,

said mesoporous layer comprises a region of increased porosity relative to a remaining portion of said mesoporous layer,

said region of increased porosity of said mesoporous layer occupies a substantially greater portion of said high H 2 O region relative to said low H 2 O region, and

said remaining portion of said mesoporous layer occupies a substantially greater portion of said low H 2 O region relative to said high H 2 O region.

41. A device as claimed in claim 40 wherein said region of increased porosity of said mesoporous layer is defined by a plurality of megapores characterized by a pore size of between about 100 μm and about 500 μm.

42. A device configured to convert a hydrogenous fuel source to electrical energy, said device comprising:

an electrochemical conversion assembly configured to partition said device into first and second flow field regions;

a first reactant input and a first product output in communication with said first flow field region;

a first diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said first flow field region and said electrochemical conversion assembly;

a second reactant input and a second product output in communication with said second flow field region; and

a second diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said second flow field region and said electrochemical conversion assembly, wherein

said device is configured such that at least one of said first and second diffusion media comprise a region subject to relatively high H 2 O concentrations and a region subject to relatively low H 2 O concentrations,

a mesoporous layer is carried along at least a portion of a major face of one of said first and second diffusion media substrates and comprises a hydrophilic carbonaceous component and a hydrophobic component, said mesoporous layer at least partially infiltrates at least one of said first and second diffusion media substrates to a depth of greater than 0 μm to about 10 μm in said high H 2 O regions and a depth of greater than 0 μm to about 25 μm in said low H 2 O regions; and

said mesoporous layer occupies a substantially greater portion of one of said high H 2 O region and said low H 2 O region relative to the other of said high H 2 O region and said low H 2 O region.

43. A device configured to convert a hydrogenous fuel source to electrical energy, said device comprising:

an electrochemical conversion assembly configured to partition said device into first and second flow field regions;

a first reactant input and a first product output in communication with said first flow field region;

a first diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said first flow field region and said electrochemical conversion assembly;

a second reactant input and a second product output in communication with said second flow field region; and

a second diffusion media comprising a porous diffusion media substrate configured to pass multiphase reactants between said second flow field region and said electrochemical conversion assembly, wherein

said device is configured such that at least one of said first and second diffusion media comprise a region subject to relatively high H 2 O concentrations and a region subject to relatively low H 2 O concentrations,

a mesoporous layer is carried along at least a portion of a major face of one of said first and second diffusion media substrates and comprises a hydrophilic carbonaceous component and a hydrophobic component, said mesoporous layer at least partially infiltrates at least one of said first and second diffusion media substrates to a depth of greater than 0 μm to about 10 μm in said high H 2 O regions and a depth of greater than 0 μm to about 25 μm in said low H 2 O regions, and

at least one of said first and second diffusion media substrates comprises a relatively high porosity region and a relatively low porosity region,

said relatively high porosity region of said substrate occupies a substantially greater portion of said high H 2 O region and said relatively low porosity region of said substrate occupies a substantially greater portion of said low H 2 O region.

Assignments (13)