초록 ▼

Interconnection layouts are described that are particularly effective in the construction of a steam reformer/fuel cell combination for providing domestic heat and/or hot water as well as electricity. A distinguishing feature of the interconnections is that they permit the operator to optimize the e

Interconnection layouts are described that are particularly effective in the construction of a steam reformer/fuel cell combination for providing domestic heat and/or hot water as well as electricity. A distinguishing feature of the interconnections is that they permit the operator to optimize the efficiency of operation of the integrated system, and provide a higher efficiency at optimum operation compared to prior art designs. Combinations of reformer/fuel cell systems with conventional furnaces or boilers are also described.

대표청구항 ▼

1. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from the hydrogen-rich reformate; a second fluid loop for controlling the temperature of the fuel cell stack; a t

1. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from the hydrogen-rich reformate; a second fluid loop for controlling the temperature of the fuel cell stack; a third fluid loop for removing heat from at least one of the first and second loops for use in a cogenerative application; and a local control area network for controlling the distribution of heat for use in cogenerative applications according to individual dwelling usage. 2. The cogeneration system of claim 1 further comprising:a fuel processor assembly, wherein steam is supplied by the first fluid loop, the fuel processor assembly comprising a burner for burning a fuel to supply energy for a reforming reaction to produce the hydrogen-rich reformate and a fuel processor exhaust from which heat is captured for transfer to a cogenerative use. 3. The cogeneration system of claim 1 further comprising:a fuel cell coolant circulating in the second fluid loop, wherein the fuel cell coolant and the hydrogen-rich reformate are in heat exchange to maintain a fixed temperature difference in order to reduce mechanical stress in the fuel cell stack. 4. The cogeneration system of claim 3, wherein the fixed temperature difference is achieved before the fuel cell coolant and the hydrogen-rich reformate enter the fuel cell stack.5. The cogeneration system of claim 1 further comprising:a fuel cell coolant circulating in the second fluid loop, wherein the fuel cell coolant and the hydrogen-rich reformate are in heat exchange to maintain a difference within a set range of temperatures in order to reduce mechanical stress in the fuel cell stack. 6. The cogeneration system of claim 5, wherein the difference within a set range of temperatures is achieved before the fuel cell coolant and the hydrogen-rich reformate enter the fuel cell stack.7. The cogeneration system of claim 1 further comprising:a fuel processor assembly for producing the hydrogen-rich reformate using an air blower and an exhaust which is used in a cogenerative application; wherein the fuel processor exhaust is in a heat exchange relationship with the first fluid loop and the air from the air blower entering the fuel processor assembly. 8. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from the hydrogen-rich reformate; a second fluid loop for controlling the temperature of the fuel cell stack; a third fluid loop for removing heat from at least one of the first and second loops for use in a cogenerative application; and, a wide control area network for controlling the distribution of heat for use in cogenerative applications according to multiple dwelling usage. 9. The cogeneration system of claim 1 further comprising:a fourth fluid loop for the heating of potable water; wherein the third fluid loop carries a fluid for providing space heating. 10. The cogeneration system of claim 1, wherein heat is extracted by the third fluid loop from at least one source in addition to the exhaust.11. The cogeneration system of claim 10, wherein the additional heat source is selected from the group consisting of the hydrogen-rich reformate, a reformer, power electronics, a furnace and a boiler.12. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from the hydrogen-rich reformate; a third fluid loop for removing heat from at least one of the first and second loops for use in a cogenerative application; a fourth fluid loop for providing heat for potable hot water; and a condensing radiator for recovering water from the cogeneration system exhaust and releasing heat from the exhaust into at least one of the fourth fluid loop and the second fluid loop; wherein the second fluid loop is in a heat exchange relationship with the third fluid loop to recover and utilize heat extracted from the cogeneration system in a cogenerative application. 13. The cogeneration system of claim 12, wherein the condensing radiator has a first zone in which heat is transferred to a fluid loop providing space heating and a second zone in which heat is transferred to a supply of potable water.14. The cogeneration system of claim 13 further comprising:heat transfer coils; wherein the water condensed from the exhaust flows over the heat transfer coils and is collected for return to the cogeneration system. 15. The cogeneration system of claim 2 further comprising:a furnace for providing heat for at least one of space heating and potable water heating. 16. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from a hydrogen-rich reformate; a second fluid loop for controlling the temperature of the fuel cell stack; and a third fluid loop for removing heat from at least one of the first and second loops for use in a cogenertive application a fuel processor assembly, wherein steam is supplied by the first fluid loop, the fuel processor assembly comprising a burner for burning a fuel to supply energy for a reforming reaction to produce the hydrogen-rich reformate and a fuel processor exhaust from which heat is captured for transfer to a cogenerative use; a furnace for providing heat for at least one of space heating and potable water heating; and, a controller for providing sufficient heat for at least one of space heating and potable water heating by selectively activating at least one of the furnace, the fuel cell stack and the fuel processor assembly. 17. A cogeneration system comprising:a first fluid loop for providing steam to a fuel reforming reaction to produce a hydrogen-rich reformate; a fuel cell stack for generating electricity from a hydrogen-rich reformate; a second fluid loop for controlling the temperature of the fuel cell stack; and a third fluid loop for removing heat from at least one of the first and second loops for use in a cogenertive application; means for cooling the second fluid loop; and a controller for selectively activating the means for cooling the second fluid loop when space heating is not being provided by the system. 18. The cogeneration system of claim 1 further comprising:a furnace for providing supplemental heat to the third fluid loop for use in at least one of space heating, potable water heating, and provision of startup heating to the cogeneration system. 19. The cogeneration system of claim 18, wherein the furnace is connected in parallel with the third fluid loop.20. The cogeneration system of claim 18, wherein the furnace is connected in series with the third fluid loop.