초록 ▼

Passive water management techniques are provided in an air-breathing direct oxidation fuel cell system. A highly hydrophobic component with sub-micrometer wide pores is laminated to the catalyzed membrane electrolyte on the cathode side. This component blocks liquid water from traveling out of the c

Passive water management techniques are provided in an air-breathing direct oxidation fuel cell system. A highly hydrophobic component with sub-micrometer wide pores is laminated to the catalyzed membrane electrolyte on the cathode side. This component blocks liquid water from traveling out of the cathode and instead causes the water to be driven through the polymer membrane electrolyte to the cell anode. The air-breathing direct oxidation fuel cell also includes a layer of cathode backing and additional cathode filter components on an exterior aspect of the cell cathode which lessen the water vapor escape rate from the cell cathode. The combination of the well laminated hydrophobic microporous layer, the thicker backing and the added filter layer, together defines a cathode structure of unique water management capacity, that enables to operate a DMFC with direct, controlled rate supply of neat (100%) methanol, without the need for any external supply or pumping of water. The cell anode is provided with a hydrophilic backing layer. When the water is driven through the polymer membrane electrolyte from the cell cathode to the cell anode chamber, it is available for the anodic reaction, and any excess water is carried out along CO2 ventilation channels to the outside environment.

대표청구항 ▼

What is claimed is: 1. A membrane electrode assembly for use in an associated direct oxidation fuel cell, comprising: (A) a protonically conductive, electronically non-conductive membrane electrolyte, having an anode aspect and a cathode aspect; (B) an anode catalyst disposed in contact with said a

What is claimed is: 1. A membrane electrode assembly for use in an associated direct oxidation fuel cell, comprising: (A) a protonically conductive, electronically non-conductive membrane electrolyte, having an anode aspect and a cathode aspect; (B) an anode catalyst disposed in contact with said anode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (C) a cathode catalyst that is suitable for oxygen electro-reduction reactions being disposed in contact with said cathode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (D) a hydrophobic cathode element having a cathode filter being a layer of expanded PTFE disposed on said cathode catalyst for effectively confining and redirecting water produced in said reactions across the protonically-conductive membrane for complete anodic oxidation, without any external supply or external redirection of water; and (E) an anode diffusion layer that is in contact with the anode catalyst on membrane electrolyte. 2. The membrane electrode assembly as defined in claim 1 wherein said protonically-conductive membrane electrolyte is a thin ionomeric membrane, whereby a higher flux of water flows from the cathode aspect back to the anode aspect through the membrane electrolyte at given water repelling characteristics of the microporous material means. 3. The membrane electrode assembly as defined in claim 2 wherein said water repelling characteristics are sufficient to supply enough water for anodic reactions to occur with a supply of 100% methanol to the anode. 4. The membrane electrode assembly as set forth in claim 2 wherein said protonically conductive membrane is of a thickness that is greater than 50 micrometers. 5. The membrane electrode assembly as set forth in claim 1 wherein the protonically conductive, electronically non-conductive membrane electrolyte is comprised of polyperfluorosulfonic acid. 6. The membrane electrode assembly as set forth in claim 1 wherein the protonically conductive, electronically non-conductive membrane electrolyte has a thickness of less than 0.007 inches. 7. The membrane electrode assembly as set forth in claim 1 wherein the protonically conductive, electronically non-conductive membrane has a thickness of between 0.002 and 0.007 inches. 8. The membrane electrode assembly as set forth in claim 1 wherein the anode catalyst is comprised of a supported or unsupported alloy of platinum and ruthenium. 9. The membrane electrode assembly as set forth in claim 1 wherein the cathode catalyst is comprised of supported or unsupported platinum. 10. The membrane electrode assembly as set forth in claim 1 further comprising a cathode diffusion layer that is substantially comprised of one or more sheets of carbon paper or carbon cloth. 11. The membrane electrode assembly as set forth in claim 10 wherein said cathode filter is substantially comprised of high surface area carbon particles intermixed-with said expanded PTFE. 12. The membrane electrode assembly as set forth in claim 11 wherein said cathode filter includes micropores of a diameter of between about 1.0 μm and 0.1 μm. 13. The membrane electrode assembly as set forth in claim 11 wherein said cathode filter achieves a permeability of water driven across the protonically conductive membrane by hydrostatic pressure of not less than 50 μg/(s cm2 atm). 14. The membrane electrode assembly as defined in claim 13 wherein said cathode filter achieves a water vapor escaping rate away from the membrane electrode assembly which is smaller than the water production rate of the associated fuel cell reactions. 15. The membrane electrode assembly as defined in claim 1 further comprising said cathode filter being laminated onto said cathode catalyst by steam pressing techniques. 16. The membrane electrode assembly as set forth in claim 1 wherein the anode diffusion layer is comprised of one or more sheets of carbon paper or carbon cloth. 17. The membrane electrode assembly as set forth in claim 1 wherein the anode diffusion layer is hydrophilic. 18. The membrane electrode assembly as set forth in claim 1 wherein the aspect of the anode diffusion layer which is in contact with the membrane electrolyte further comprises means for encouraging the elimination of anodically generated gas. 19. The membrane electrode assembly as set forth in claim 1 wherein the aspect of the anode diffusion layer which is in contact with the membrane electrolyte further comprises carbon dioxide router means for encouraging gas to travel away from the anode aspect of the membrane electrode assembly out of the fuel cell. 20. The membrane electrode assembly as set forth in claim 19 wherein carbon dioxide is released through a gap adjacent to the anode diffusion layer on an aspect of the anode diffusion layer that is opposite the anode catalyst of the membrane electrolyte, in such a manner that the carbon dioxide is vented to the ambient environment via a tortuous path. 21. The membrane electrode assembly as set forth in claim 1 wherein the fuel is delivered to the anode through a fuel permeable material. 22. The membrane electrode assembly as set forth in claim 21 wherein the fuel permeable material is a polymer. 23. The membrane electrode assembly as set forth in claim 21 wherein the fuel permeable material is at least partially comprised of at least one of silicone or porous PTFE. 24. The membrane electrode assembly as set forth in claim 21 wherein the fuel permeable material is at least partially comprised of polyperfluorosulfonic acid. 25. The membrane electrode assembly as set forth in claim 21 wherein the fuel permeable material is a porous, solid plate. 26. The membrane electrode assembly as defined in claim 1 wherein said protonically conductive membrane is a membrane of intrinsic protonic conductivity. 27. A direct oxidation fuel cell, comprising: (A) a membrane electrolyte intimately interfacing with a catalyst layer along each of membrane's major surfaces, being a catalyzed membrane electrolyte, having an anode aspect and a cathode aspect; (B) an anode catalyst is disposed in contact with an anode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (C) a cathode catalyst that is suitable for oxygen electro-reduction reactions which is disposed in contact with a cathode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (D) a cathode filter of expanded PTFE for driving water produced in said reactions across the protonically-conductive membrane electrolyte towards said anode aspect, said cathode filter being disposed generally adjacent the cathode catalyst of the membrane electrolyte; (E) an anode diffusion layer that is contact with the anode catalyst on membrane electrolyte; and (F) a load coupled across said fuel cell. 28. The direct oxidation fuel cell as defined in claim 27 further comprising a hydrophilic anode diffusion layer. 29. The direct oxidation fuel cell as defined in claim 27 wherein said membrane electrolyte includes a membrane of intrinsic protonic conductivity. 30. A direct oxidation fuel cell system comprised of: (A) a membrane electrode assembly including: i. a protonically conductive, electronically non-conductive membrane electrolyte; ii. an anode catalyst that is disposed in contact with an anode aspect of the protonically conductive membrane electrolyte; iii. a cathode catalyst that is suitable for oxygen electro reduction reactions which is disposed in contact with a cathode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; iv. a hydrophobic cathode filter of expanded PTFE having means for driving water produced in said reactions across the protonically-conductive electronically non-conductive membrane electrolyte towards said anode aspect, said cathode filter being disposed generally adjacent the cathode catalyst of the membrane electrolyte that; and v. an anode diffusion layer that is contact with the protonically conductive, membrane electrolyte; (B) a housing; (C) a means for making electrical connections; (D) a means for introducing fuel to the fuel cell; (B) a fuel source; and (F) an oxygen source. 31. The direct oxidation fuel cell system of claim 30, wherein the oxygen source is ambient air. 32. The direct oxidation fuel cell system as defined in claim 30 wherein said protonically conductive membrane is a membrane of intrinsic protonic conductivity. 33. A membrane electrode assembly for use in an associated direct oxidation fuel cell, comprising: (A) a protonically conductive, electronically non-conductive membrane electrolyte, having an anode aspect and a cathode aspect; (B) an anode catalyst disposed in contact with said anode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (C) a cathode catalyst that is suitable for oxygen electro-reduction reactions being disposed in contact with said cathode aspect of the protonically conductive, electronically non-conductive membrane electrolyte; (D) a hydrophobic cathode element comprising a cathode filter including a layer of expanded PTFE whereby water evaporation rate in the cathode is limited, said cathode filter being disposed on said cathode catalyst for effectively confining and redirecting water produced in said reactions across the protonically-conductive membrane for complete anodic oxidation, without any external supply or external redirection of water; and (E) an anode diffusion layer that is in contact with the anode catalyst on membrane electrolyte.