Methods, apparatus, and systems for producing hydrogen from a fuel
View Patent ↗Methods and apparatus for producing hydrogen with reforming catalysts. The reforming catalysts may be platinum group metals on a support material, and they may be located in a reforming reaction zone of a primary reactor. The support material may be an oxidic support having a ceria and zirconia promoter, or may include a neodymium stabilizer. The support material may also include at least one Group IA, Group IIA, manganese, or iron metal promoter. The primary reactor may have a first and second reforming reaction zones, where upstream catalysts located in the first reforming reaction zone and downstream catalysts located in the second reforming reaction zone may be selected to perform optimally under the conditions in their respective reforming reaction zone.
1. A fuel cell system comprising:
an autothermal reactor for producing hydrogen gas from a fuel, said autothermal reactor comprising:
a reactant mixture inlet for a reactant mixture comprising a hydrocarbon fuel, oxygen, and steam and a product gas outlet;
a first reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said first reforming reaction zone proximate to said reactant mixture inlet, said first reforming reaction zone including an upstream reforming catalyst disposed therein, said upstream reforming catalyst comprising a platinum group metal on a support material, wherein said support material comprises an oxidic support, a promoter comprising ceria and zirconia, and a stabilizing material comprising lanthanum, neodymium, and combinations thereof, said platinum group metal consisting essentially of platinum and rhodium in a platinum-to-rhodium ratio sufficient to lower a light-off temperature of said upstream reforming catalyst below that of a substantially platinum-free rhodium based catalyst; and
a second reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said second reforming reaction zone downstream from said first reforming reaction zone, said second reforming reaction zone proximate to said first reforming reaction zone, and said second reforming reaction zone proximate to said product gas outlet, said second reforming reaction zone including a downstream reforming catalyst disposed therein, said downstream reforming catalyst comprising a platinum group metal on an oxidic support material and a first promoter comprising at least one Group I, manganese, or iron metal and a second promoter comprising ceria zirconia, said platinum group metal consisting essentially of rhodium, said upstream reforming catalyst having a faster light-off ability than said downstream reforming catalyst, said first reforming reaction zone at a higher temperature than said second reforming reaction zone, wherein said hydrogen gas, carbon dioxide, and carbon monoxide from said first and second reforming reaction zones exit through said product gas outlet;
a water-gas shift reactor positioned after said autothermal reactor, said hydrogen gas, carbon dioxide, and carbon monoxide from said product gas outlet being a feed stream for said water-gas shift reactor, a portion of said carbon monoxide being converted into carbon dioxide in said water-gas shift reactor forming a carbon monoxide purged product stream containing said hydrogen; and
a fuel cell stack positioned after said water-gas shift reactor, said carbon monoxide purged product stream containing said hydrogen being a feed stream for said fuel cell stack.
2. The apparatus as claimed in claim 1 wherein said first reforming reaction zone has a concentration of fuel that is higher than a concentration of fuel in said second reforming reaction zone.
3. The apparatus as claimed in claim 1 wherein said first and second reaction zones are defined by a monolithic structure.
4. The apparatus as claimed in claim 3 wherein said monolithic structure is made from ceramic, metal, open-cell ceramic foam, open-cell metal foam and combinations thereof.
5. The apparatus as claimed in claim 1 wherein said first reaction zone is defined by a first monolithic structure, and wherein said second reaction zone is defined by a second monolithic structure.
6. The apparatus as claimed in claim 1 wherein said ratio of platinum to rhodium is between 1:10 and 10:1.
7. The apparatus as claimed in claim 6 wherein said ratio of platinum to rhodium is between 1:3 and 3:1.
8. The apparatus as claimed in claim 1 wherein said oxidic support is alumina.
9. The apparatus as claimed in claim 1 wherein said stabilizing material is present in an amount of about 1% to about 8% by weight of said support material.
10. The apparatus as claimed in claim 9 wherein said oxidic support is alumina.
11. The apparatus as claimed in claim 1 wherein said promoter in said upstream reforming catalyst comprises between about 10% and about 60% by weight of said support material.
12. The apparatus of claim 1 wherein a ratio of ceria to zirconia is between about 80:20 to about 20:80.
13. The apparatus of claim 1 wherein an atomic ratio of the Group IA, manganese, or iron metal promoter to rhodium is between about 10:1 to about 2:1.
14. The apparatus of claim 1 wherein said oxidic support of said downstream reforming catalyst further comprises about 10 to about 60% of a ceria zirconia promoter.
15. The apparatus of claim 1 wherein said oxidic support of said downstream reforming catalyst further comprises about 1 to about 8% of a stabilizing material comprising lanthanum, neodymium, and combinations thereof.
16. A fuel cell system comprising:
a fuel cell stack provided with a source of hydrogen gas; and
a fuel processing system for providing said hydrogen gas, said fuel processing system comprising an autothermal primary reactor and a water-gas shift reactor wherein:
said autothermal primary reactor has a reactant mixture inlet for a reactant mixture comprising a hydrocarbon fuel, oxygen, and steam and a product gas outlet,
said autothermal primary reactor has a first reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said first reforming reaction zone proximate to said reactant mixture inlet,
said autothermal primary reactor has a second reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said second reforming reaction zone downstream from said first reforming reaction zone, said second reforming reaction zone proximate to said first reforming reaction zone, and said second reforming reaction zone proximate to said product gas outlet such that a product gas stream exiting said first reforming reaction zone subsequently enters said second reforming reaction zone,
said autothermal primary reactor has at least one upstream reforming catalyst, said upstream reforming catalyst comprised of a platinum group metal on a support material, wherein said support material comprises an oxidic support, a promoter comprising ceria and zirconia, and a stabilizing material comprising lanthanum, neodymium, and combinations thereof, said platinum group metal consisting essentially of platinum and rhodium in said first reforming reaction zone with a ratio of platinum to rhodium to lower a light-off temperature of said upstream reforming catalyst below that of a substantially platinum-free rhodium based reforming catalyst, and
said autothermal primary reactor has at least one downstream reforming catalyst in said second reforming reaction zone, said downstream reforming catalyst comprising a platinum group metal on an oxidic support material and a first promoter comprising at least one Group I, manganese, or iron metal and a second promoter comprising ceria zirconia, said platinum group metal consisting essentially of rhodium, said upstream reforming catalyst having a faster light-off ability than said downstream reforming catalyst, said first reforming reaction zone at a higher temperature than said second reforming reaction zone, and wherein said hydrogen gas, carbon dioxide, and carbon monoxide from said first and second reforming reaction zones exit through said product gas outlet;
said water-gas shift reactor being positioned after said autothermal reactor, said hydrogen gas, carbon dioxide, and carbon monoxide from said product gas outlet being a feed stream for said water-gas shift reactor, a portion of said carbon monoxide being converted into carbon dioxide in said water-gas shift reactor forming a carbon monoxide purged product stream containing said hydrogen; and
said fuel cell stack positioned after said water-gas shift reactor, said carbon monoxide purged product stream containing said hydrogen being a feed stream for said fuel cell stack.
17. The fuel cell system as claimed in claim 16 wherein said ratio of platinum to rhodium is between 1:10 and 10:1.
18. The fuel cell system as claimed in claim 17 wherein said ratio of platinum to rhodium is between 1:3 and 3:1.
19. The fuel cell of claim 16 wherein an atomic ratio of the Group IA, manganese, or iron metal promoter to rhodium is between about 10:1 to about 2:1.
20. The fuel cell of claim 16 wherein said oxidic support of said downstream reforming catalyst further comprises about 10 to about 60% of a ceria zirconia promoter.
21. The fuel cell of claim 16 wherein said oxidic support of said downstream reforming catalyst further comprises about 1 to about 8% of a stabilizing material comprising lanthanum, neodymium, and combinations thereof.
22. A vehicle comprising:
a vehicle body;
at least one fuel cell stack provided with a source of hydrogen gas, wherein said at least one fuel cell stack at least partially provides said vehicle body with motive power; and
a fuel processing system for providing said hydrogen gas, said fuel processing system comprising an autothermal primary reactor and a water-gas shift reactor wherein:
said autothermal primary reactor has a reactant mixture inlet for a reactant mixture comprising a hydrocarbon fuel, oxygen, and steam and a product gas outlet,
said autothermal primary reactor has a first reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said first reforming reaction zone proximate to said reactant mixture inlet,
said autothermal primary reactor has a second reforming reaction zone for reacting said reactant mixture to produce said hydrogen gas, said second reforming reaction zone downstream from said first reforming reaction zone, said second reforming reaction zone proximate to said first reforming reaction zone, and said second reforming reaction zone proximate to said product gas outlet such that a product gas stream exiting said first reforming reaction zone subsequently enters said second reforming reaction zone,
said autothermal primary reactor has at least one upstream reforming catalyst, said upstream reforming catalyst comprised of a platinum group metal on a support material, wherein said support material comprises an oxidic support, a promoter comprising ceria and zirconia, and a stabilizing material comprising lanthanum, neodymium, and combinations thereof, said platinum group metal consisting essentially of platinum and rhodium in said first reforming reaction zone with a ratio of platinum to rhodium to lower a light-off temperature of said upstream reforming catalyst below that of a substantially platinum-free rhodium based reforming catalyst, and
said autothermal primary reactor has at least one downstream reforming catalyst in said second reforming reaction zone, said downstream reforming catalyst comprising a platinum group metal on an oxidic support material and a first promoter comprising at least one Group I, manganese, or iron metal and a second promoter comprising ceria zirconia, said platinum group metal consisting essentially of rhodium, said upstream reforming catalyst having a faster light-off ability than said downstream reforming catalyst, said first reforming reaction zone at a higher temperature than said second reforming reaction zone, and wherein said hydrogen gas, carbon dioxide, and carbon monoxide from said first and second reforming reaction zones exit through said product gas outlet;
said water-gas shift reactor being positioned after said autothermal reactor, said hydrogen gas, carbon dioxide, and carbon monoxide from said product gas outlet being a feed stream for said water-gas shift reactor, a portion of said carbon monoxide being converted into carbon dioxide in said water-gas shift reactor forming a carbon monoxide purged product stream containing said hydrogen; and
said fuel cell stack positioned after said water-gas shift reactor, said carbon monoxide purged product stream containing said hydrogen being a feed stream for said fuel cell stack.
23. The vehicle as claimed in claim 22 wherein said ratio of platinum to rhodium is between 1:10 and 10:1.
24. The vehicle as claimed in claim 23 wherein said ratio of platinum to rhodium is between 1:3 and 3:1.
25. The vehicle of claim 22 wherein an atomic ratio of the Group IA, manganese, or iron metal promoter to rhodium is between about 10:1 to about 2:1.
26. The vehicle of claim 22 wherein said oxidic support of said downstream reforming catalyst further comprises about 10 to about 60% of a ceria zirconia promoter.
27. The vehicle of claim 22 wherein said oxidic support of said downstream reforming catalyst further comprises about 1 to about 8% of a stabilizing material comprising lanthanum, neodymium, and combinations thereof.