초록 ▼

A device for converting chemical energy to electricity is provided, the device comprising a high temperature fuel cell with the ability for partially oxidizing and completely reforming fuel, and a low temperature fuel cell juxtaposed to said high temperature fuel cell so as to utilize remaining refo

A device for converting chemical energy to electricity is provided, the device comprising a high temperature fuel cell with the ability for partially oxidizing and completely reforming fuel, and a low temperature fuel cell juxtaposed to said high temperature fuel cell so as to utilize remaining reformed fuel from the high temperature fuel cell. Also provided is a method for producing electricity comprising directing fuel to a first fuel cell, completely oxidizing a first portion of the fuel and partially oxidizing a second portion of the fuel, directing the second fuel portion to a second fuel cell, allowing the first fuel cell to utilize the first portion of the fuel to produce electricity; and allowing the second fuel cell to utilize the second portion of the fuel to produce electricity.

대표청구항 ▼

1. A device for converting chemical energy to electricity, the device comprising: a) a high temperature fuel cell having a means for partially oxidizing fuel can completely reforming fuel where the high temperature fuel cell operates at a temperature between 800° C. and 1000° C.; and b) a low te

1. A device for converting chemical energy to electricity, the device comprising: a) a high temperature fuel cell having a means for partially oxidizing fuel can completely reforming fuel where the high temperature fuel cell operates at a temperature between 800° C. and 1000° C.; and b) a low temperature fuel cell juxtaposed to said high temperature fuel cell so as to utilize the reformed fuel from the high temperature fuel cell; wherein the high temperature fuel cell has anionic conducing electrolytes and the low temperature fuel cell has cationic conducting electrolytes. 2. The device as recited in claim 1 wherein the low temperature fuel cell operates between 80° C. and 90° C. 3. The device as recited in claim 1 wherein the means for partially oxidizing fuel reforms the fuel without completely oxidizing the fuel. 4. The device as recited in claim 3 wherein fuel is a hydrocarbon selected from the group consisting of methane, ethane, propane, butane, components of low sulfur gasoline, components of low sulfur diesel, or combinations thereof. 5. The device as recited in claim 1 wherein both fuel cells are air fired. 6. A method for producing electricity comprising: a) directing fuel to a first fuel cell; b) completely oxidizing a first portion of the fuel and partially oxidizing a second portion of the fuel; c) directing the second fuel portion to a second fuel cell; d) allowing the first fuel cell to utilize the first portion of the fuel to produce electricity where the first fuel cell operates at a temperature of between approximately 800° C and 1000° C.; and e) allowing the second fuel cell to utilize the second portion of the fuel to produce electricity. 7. The method as recited in claim 6 wherein the second fuel cell operates at a temperature of between approximately 80° C. and 90° C. 8. The method as recited in claim 6 wherein the first fuel cell has a solid oxide electrolyte. 9. The method as recited in claim 6 wherein the first fuel cell has anionic conducting electrolytes and the second fuel cell has cationic conducting electrolytes. 10. The method as recited in claim 6 wherein the fuel is a hydrocarbon selected from the group consisting of methane, ethane, propane, butane, components of low sulfur diesel, components of low sulfur gasoline, and combinations thereof. 11. The method as recited in claim 6 wherein the remaining reformed fuel from partially oxidized fuel is syngas. 12. The method as recited in claim 6 wherein complete fuel utilization is achieved without mixing fuel-derived carbon dioxide with air-derived stack gases. 13. The method as recited in claim 6 wherein both fuel cells are air fired. 14. The method as recited in claim 13 wherein an air:fuel equivalence ratio of less than approximately 1.5 is utilized.