Fuel cell system with degradation protected anode
View Patent ↗A method of operating a fuel cell including an anode, a cathode, a first passage, and a second passage, wherein the anode is disposed in the first passage and the cathode in the second passage including producing a non-explosive gaseous feed consisting of (i) at least one oxidizable component having a greater tendency to undergo oxidation relative to the anode, and (ii) a remainder which is the predominant component in the gaseous feed consisting essentially of water vapor; and introducing the non-explosive gaseous feed to the first passage to form a first gaseous feed stream flowing through the first passage when the anode realizes a temperature effective to facilitate deteriorative oxidation of the anode in the presence of an oxidizing agent. The non-explosive gaseous feed is provided to mitigate or prevent anode oxidation and the formation of potentially explosive gaseous mixtures.
1. A method of operating a fuel cell including an anode, a cathode, a first passage, and a second passage, wherein the anode is disposed in the first passage and the cathode is disposed in the second passage, comprising:
(i) producing a non-explosive gaseous feed consisting of (i) at least one oxidizable component having a greater tendency to undergo oxidation relative to the anode, and (ii) a remainder, wherein the remainder is the predominant component in the gaseous feed and consists essentially of water vapor; and
(ii) introducing the non-explosive gaseous feed to the first passage to form a first gaseous stream flowing through the first passage when the anode realizes a temperature effective to facilitate deteriorative oxidation of the anode in the presence of an oxidizing agent.
2. The method as claimed in claim 1 , wherein the concentration of the water vapor in the gaseous feed is greater than 50% by volume based on the total volume of the gaseous feed.
3. The method as claimed in claim 2 , wherein the concentration of the at least one oxidizable component is less than the minimum concentration necessary to render the gaseous feed potentially explosive at the effective temperature.
4. The method as claimed in claim 2 , wherein the concentration of the at least one oxidizable component is less than the lower flammability limit of the at least one oxidizable component.
5. The method as claimed in claim 2 , wherein the concentration of the at least one oxidizable component is effective to mitigate deteriorative oxidation of the anode.
6. The method as claimed in claim 5 , wherein the concentration of the at least one oxidizable component is effective to substantially prevent deteriorative oxidation of the anode.
7. The method as claimed in claim 6 , wherein the at least one oxidizable component is selected from the group consisting of hydrogen, alcohols, aldehydes, ketones, esters, organic acids, ammonia, hydrazine, and hydrocarbons.
8. The method as claimed in claim 7 , further comprising evaporating an aqueous mixture consisting essentially of water and the at least one oxidizable component to produce the gaseous feed.
9. The method as claimed in claim 8 , wherein the anode comprises nickel.
10. The method as claimed in claim 9 , wherein the effective temperature is 400° C.
11. The method as claimed in claim 10 , further comprising flowing a second gaseous stream through the second passage, the second gaseous stream including oxygen, while contemporaneously flowing the first gaseous stream through the first passage.
12. The method as claimed in claim 11 , wherein the at least one oxidizable component is methanol and the concentration of methanol in the aqueous solution is less than about 2.4% by weight based on the total weight of the aqueous solution.
13. The method as claimed in claim 1 , wherein the anode is heated from temperatures lower than the effective temperature to the effective temperature.
14. The method as claimed in claim 1 , wherein, below the effective temperature, the anode does not realize deteriorative oxidation in the presence of an oxidizing agent.
15. A method of operating a fuel cell including an anode, a cathode, a first passage, and a second passage, wherein the anode is disposed in the first passage and the cathode is disposed in the second passage, comprising:
producing a non-explosive gaseous feed consisting of (i) at least one oxidizable component having a greater tendency to undergo oxidation relative to the anode, and (ii) a remainder, wherein the remainder is the predominant component in the gaseous feed and consists essentially of water vapor;
introducing the non-explosive gaseous feed to the first passage to form a first gaseous stream flowing through the first passage when the anode realizes a temperature effective to facilitate deteriorative oxidation of the anode in the presence of an oxidizing agent; and
evaporating an aqueous mixture consisting essentially of water and the at least one oxidizable component to produce the gaseous feed.
16. The method as claimed in claim 15 , wherein the concentration of the water vapor in the gaseous feed is greater than 50% by volume based on the total volume of the gaseous feed.
17. The method as claimed in claim 16 , wherein the concentration of the at least one oxidizable component is less than the minimum concentration necessary to render the gaseous feed potentially explosive at the effective temperature.
18. The method as claimed in claim 16 , wherein the concentration of the at least one oxidizable component is less than the lower flammability limit of the at least one oxidizable component.
19. The method as claimed in claim 16 , wherein the concentration of the at least one oxidizable component is effective to mitigate deteriorative oxidation of the anode.
20. The method as claimed in claim 19 , wherein the concentration of the at least one oxidizable component is effective to substantially prevent deteriorative oxidation of the anode.
21. The method as claimed in claim 20 , wherein the at least one oxidizable component is selected from the group consisting of hydrogen, alcohols, aldehydes, ketones, esters, organic acids, ammonia, hydrazine, and hydrocarbons.
22. The method as claimed in claim 15 , wherein the anode comprises nickel.
23. The method as claimed in claim 22 , wherein the effective temperature is 400° C.
24. The method as claimed in claim 23 , further comprising flowing a second gaseous stream through the second passage, the second gaseous stream including oxygen, while contemporaneously flowing the first gaseous stream through the first passage.
25. The method as claimed in claim 24 , wherein the at least one oxidizable component is methanol and the concentration of methanol in the aqueous solution is less than about 2.4% by weight based on the total weight of the aqueous solution.
26. The method as claimed in claim 15 , wherein the anode is heated from temperatures lower than the effective temperature to the effective temperature.
27. The method as claimed in claim 15 , wherein, below the effective temperature, the anode does not realize deteriorative oxidation in the presence of an oxidizing agent.
28. A method of operating a fuel cell including an anode, a cathode, a first passage, and a second passage, wherein the anode is disposed in the first passage and the cathode is disposed in the second passage, comprising:
producing a non-explosive gaseous feed consisting of (i) at least one oxidizable component having a greater tendency to undergo oxidation relative to the anode, and (ii) a remainder, wherein the remainder is the predominant component in the gaseous feed and consists essentially of water vapor;
introducing the non-explosive gaseous feed to the first passage to form a first gaseous stream flowing through the first passage when the anode realizes a temperature effective to facilitate deteriorative oxidation of the anode in the presence of an oxidizing agent; and
evaporating an aqueous mixture consisting essentially of water and the at least one oxidizable component to produce the gaseous feed;
wherein the at least one oxidizable component is selected from the group consisting of hydrogen, alcohols, aldehydes, ketones, esters, organic acids, ammonia, hydrazine, and hydrocarbons;
wherein the concentration of the at least one oxidizable component is effective to substantially prevent deteriorative oxidation of the anode;
wherein the concentration of the at least one oxidizable component is effective to mitigate deteriorative oxidation of the anode; and
wherein the concentration of the water vapor in the gaseous feed is greater than 50% by volume based on the total volume of the gaseous feed.
29. The method as claimed in claim 28 , wherein the anode comprises nickel.
30. The method as claimed in claim 29 , wherein the effective temperature is 400° C.
31. The method as claimed in claim 30 , further comprising flowing a second gaseous stream through the second passage, the second gaseous stream including oxygen, while contemporaneously flowing the first gaseous stream through the first passage.
32. The method as claimed in claim 31 , wherein the at least one oxidizable component is methanol and the concentration of methanol in the aqueous solution is less than about 2.4% by weight based on the total weight of the aqueous solution.