초록 ▼

A keep warm system for a fuel cell, power plant ( 10 ), typically of the PEM type, prevents freeze-sensitive portions of the power plant, such as the cell stack assembly (CSA) ( 12 ) and the water management system ( 28, 30 ), from freezing under extreme cold external temperatures, during extended s

A keep warm system for a fuel cell, power plant ( 10 ), typically of the PEM type, prevents freeze-sensitive portions of the power plant, such as the cell stack assembly (CSA) ( 12 ) and the water management system ( 28, 30 ), from freezing under extreme cold external temperatures, during extended storage (CSA shut-down) periods. Pre-stored and pressurized fuel, typically hydrogen ( 25 ), normally used to fuel the anode ( 16 ) of the CSA, is used as fuel for a catalytic oxidation reaction at a catalytic burner ( 66 ) to produce heated gas that convectively passes in heat exchange relation with the freeze sensitive portions ( 12, 28, 30 ) of the power plant ( 10 ). The convective flow of the heated gases induces the air flow to the burner ( 66 ), obviating the need for parasitic electrical loads. Thermal insulating means ( 64 ) substantially enclose the freeze-sensitive CSA ( 12 ) and/or the water management system ( 28, 30 ), and the convective flow of the heated gas from the catalytic burner ( 66 ), to improve system thermal efficiency.

대표청구항 ▼

1. A keep warm system to provide freeze protection for a fuel cell power plant ( 10 ), comprising:a. a fuel cell stack assembly (CSA) ( 12 ) including an anode ( 16 ), a cathode ( 18 ), an electrolyte ( 14 ), and a cooler ( 20 );b. fuel supply means ( 25 ) for providing a supply of fuel, at least so

1. A keep warm system to provide freeze protection for a fuel cell power plant ( 10 ), comprising:a. a fuel cell stack assembly (CSA) ( 12 ) including an anode ( 16 ), a cathode ( 18 ), an electrolyte ( 14 ), and a cooler ( 20 );b. fuel supply means ( 25 ) for providing a supply of fuel, at least some of the fuel being supplied as reactant to the anode ( 16 );c. a source of oxidant reactant ( 22 ) operatively supplied to the cathode ( 18 );d. a water management system ( 30 , 28 ) operatively connected to the cooler ( 20 ) of the CSA ( 12 );e. thermal insulating means ( 64 ) enclosing at least one of the CSA ( 12 ) and the water management system ( 30 , 28 ) for providing thermal insulation thereof; andf. catalytic fuel burner means ( 66 ) operatively connected to the fuel supply means ( 25 ) and to the source of oxidant reactant ( 22 ) for catalytically reacting the fuel and oxidant and providing a source of heat, the burner means ( 66 ) being disposed and operative to supply heated gas into the thermal insulating enclosure means ( 64 ), and to the at least one of the CSA ( 12 ) and the water management system ( 30 , 28 ) in the thermal insulating enclosure means ( 64 ), thereby to prevent freezing of water in freeze-sensitive parts of the fuel cell power plant. 2. The keep-warm system of claim 1 wherein the catalytic burner means ( 66 ) includes a catalytic surface ( 72 ) for combustively reacting the fuel in the presence of oxidant in a flameless manner to release heat only in a thermal range less than about 1000° F. 3. The keep-warm system of claim 2 wherein the heat released by catalytic combustion at the catalytic burner means ( 66 ) is in the thermal range of about 200°-700° F. 4. The keep-warm system of claim 2 wherein the source of oxidant reactant ( 22 ) is ambient air, the air being supplied to the catalytic burner means ( 66 ) and mixed with fuel from the fuel supply means ( 25 ) for combustively reacting the mixture in the presence of the catalytic surface ( 72 ) to release heat. 5. The keep-warm system of claim 1 wherein the fuel supply means ( 25 ) comprises a container of hydrogen stored under pressure. 6. The keep-warm system of claim 1 wherein both the CSA ( 12 ) and the water management system ( 28 , 30 ) are substantially enclosed by the thermal insulating means ( 64 ). 7. The keep-warm system of claim 4 wherein the electrolyte ( 14 ) of the CSA ( 12 ) is a proton exchange membrane (PEM), the fuel from the fuel supply means ( 25 ) is hydrogen, and the heat released by catalytic combustion at the catalytic burner means ( 66 ) is in the thermal range of about 200°-700° F. 8. In a fuel cell power plant ( 10 ) having a fuel cell stack assembly (GSA) ( 12 ) including an anode ( 16 ), a cathode ( 18 ), and an electrolyte ( 14 ), a fuel supply ( 25 ) for providing fuel to at least the anode ( 16 ), a source of oxidant reactant ( 22 ) for supplying at least the cathode ( 18 ), and a water management system ( 30 , 28 ) operatively connected to the CSA ( 12 ), the method of preventing freezing of water in freeze-sensitive parts of the fuel cell power plant ( 10 ) during shutdown, comprising the steps of:a. selectively flowing ( 62 , 63 , 69 , 67 ) fuel ( 25 ) and oxidant ( 22 ) to a catalytic fuel burner ( 66 ) during shutdown for catalytic combustion to provide heated gas;b. convectively flowing the heated gas into heat transfer relation with the freeze-sensitive parts of the fuel cell power plant ( 10 ) to provide heat thereto; andc. thermally insulating the freeze-sensitive parts of the fuel cell power plant ( 10 ) including the heated gas flowing in heat transfer relation therewith. 9. The method of claim 8 wherein the step of selectively flowing fuel and oxidant to a catalytic fuel burner provides heated gas in a thermal range of about 200°-700° F. 10. The method of claim 8 wherein the step of thermally insulating the freeze-sensitive parts of the fuel cell power plant ( 10 ) c omprises thermally insulating both the GSA ( 12 ) and the water management system ( 28 , 30 ). 11. A keep-warm system to provide freeze protection for a fuel cell power plant ( 10 ), comprising:a. a fuel cell stack assembly (GSA) ( 12 ) including an anode ( 16 ), a cathode ( 18 ), and an electrolyte ( 14 );b. fuel supply means ( 25 ) for providing a supply of fuel, at least some of the fuel being supplied as reactant to the anode ( 16 );c. a source of oxidant reactant ( 22 ) operatively supplied to the cathode ( 18 );d. a water management system ( 30 , 28 ) operatively connected to the GSA ( 12 );e. thermal insulating means ( 64 ) enclosing at least one of the GSA ( 12 ) and the water management system ( 30 , 28 ) for providing thermal insulation thereof; andf. catalytic fuel burner means ( 66 ) operatively connected to the fuel supply means ( 25 ) and to the source of oxidant reactant ( 22 ) for catalytically reacting the fuel and oxidant and providing a source of heat, the burner means ( 66 ) being disposed and operative to supply heated gas into the thermal insulating enclosure means ( 64 ), and to the at least one of the GSA ( 12 ) and the water management system ( 30 , 28 ) in the thermal insulating enclosure means ( 64 ), thereby to prevent freezing of water in freeze-sensitive parts of the fuel cell power plant. 12. The keep-warm system of claim 11 wherein the catalytic burner means ( 66 ) includes a catalytic surface ( 72 ) for combustively reacting the fuel in the presence of oxidant in a flameless manner to release heat only in a thermal range less than about 1000° F. 13. The keep-warm system of claim 12 wherein the catalytic burner means ( 66 ) is separate from the GSA ( 12 ). 14. The keep-warm system of claim 13 wherein the CSA ( 12 ) includes a cooler ( 20 ) and the water management system ( 30 , 28 ) is operatively connected to the cooler ( 20 ) of the GSA ( 12 ). 15. The keep-warm system of claim 12 wherein the heat released by catalytic combustion at the catalytic burner means ( 66 ) is in the thermal range of about 200°-700° F. 16. The keep-warm system of claim 12 wherein the source of oxidant reactant ( 22 ) is ambient air, the air being supplied to the catalytic burner means ( 66 ) and mixed with fuel from the fuel supply means ( 25 ) for combustively reacting the mixture in the presence of the catalytic surface ( 72 ) to release heat. 17. The keep-warm system of claim 11 wherein the fuel supply means ( 25 ) comprises a container of hydrogen stored under pressure. 18. The keep-warm system of claim 11 wherein both the CSA ( 12 ) and the water management system ( 28 , 30 ) are substantially enclosed by the thermal insulating means ( 64 ). 19. The keep-warm system of claim 11 wherein, for a system scaled commensurately with a consumption by catalytic fuel burner means ( 66 ) of not more than about 0.014 pph of hydrogen for about a 75 kw PEM fuel cell stack assembly, the insulation value of the thermal insulating means ( 64 ), as determined by at least the “R” value and thickness of said thermal insulating means, is sufficient to prevent freezing of water in freeze-sensitive parts of the plant for at least several days at external temperatures as low as −40° C. 20. The keep-warm system of claim 19 wherein the electrolyte ( 14 ) of the CSA ( 12 ) is a proton exchange membrane (PEM), the fuel from the fuel supply means ( 25 ) is hydrogen, and the heat released by catalytic combustion at the catalytic burner means ( 66 ) is in the thermal range of about 200°-700° F.