Referring to
Not all of the reformate is consumed by the electrochemical reactions inside the fuel cell stack 50. Instead, in accordance with some embodiments of the invention, the fuel cell stack 50 produces an anode exhaust flow (at its anode exhaust outlet 24), which contains residual fuel not consumed in the electrochemical reactions, as well as possible undesirable gases and byproducts (N2 and CO, as examples). For purposes of cleaning up the exhaust as well as producing thermal energy, the anode exhaust of the fuel cell stack 50 may be combusted with air 22 inside a combustor 20, otherwise called an oxidizer.
The heat that is generated by the combustor 20 may be used for such purposes as warming up the fuel cell 50 during its initial start up and supplemental heating (heating a water tank, for example). Therefore, the combustor 20 is part of an integrated exhaust combustor and thermal recovery assembly 11 of the fuel cell system 10. More specifically, in addition to the combustor 20, the assembly 11 includes thermal recovery devices, such as thermal exchangers 30 and 40, for purposes of recovering thermal energy from the heated exhaust flow 26 from the combustor 20 to improve the overall efficiency of the fuel cell system 10.
More specifically, in accordance with some embodiments of the invention, the combustor 20 is integrated with the thermal exchangers 30 and 40 so that there are no thermal barriers or excessive piping between the thermal exchangers 30 and 40 and the combustor 20. This arrangement serves to make the assembly behave like a condensing boiler and contributes to its relatively high additional thermal efficiency.
As a more specific example, in accordance with some embodiments of the invention, the thermal exchanger 30 is a coolant heat exchanger that is directly connected to receive the exhaust flow 26 from the combustor 20 for purposes of transferring thermal energy from the combustor's exhaust to a coolant that circulates through the fuel cell stack 50. Thus, the coolant may flow from a coolant system 60, through a coolant inlet 62 of the thermal exchanger 30, receive thermal energy from the heated exhaust flow 26 from the combustor 20, and then exit the thermal exchanger 30 to flow through an outlet 64 to a coolant inlet of the fuel cell stack 50. During the initial startup of the fuel cell stack 50, the fuel cell system 10 routes the coolant through the aforementioned path for purposes of warming up the stack 50. The coolant returns from the fuel cell stack 50 to a coolant inlet 65 of the coolant subsystem 60.
In accordance with some embodiments of the invention, the thermal exchanger 40 may form a condensing section of the assembly 11. In this regard, the thermal exchanger 40 may receive an exhaust flow 38 from the upstream thermal exchanger 30. The thermal exchanger 40 may receive a coolant via its coolant inlet 70 and output 72 from a coolant source (such as a water heater, for example). The coolant condenses water from the exhaust stream 38 to form a corresponding condensate, which may be removed from the assembly 11 via a condensate line 73. An exhaust 42 from the thermal exchanger 40 exits the assembly 11, in accordance with some embodiments of the invention.
The combustor 20 may take on numerous forms, depending on the particular embodiment of the invention. For example, in accordance with some embodiments of the invention, the combustor 20 may be an exhaust burner that mixes an anode exhaust flow with an oxidant (such as air) to create a substantially funnel-shaped flow, as described in U.S. patent application Ser. No. 11/311,695, entitled “FUEL CELL EXHAUST GAS BURNER,” which was filed on Dec. 19, 2005, and is hereby incorporated by reference. As another example, in accordance with some embodiments of the invention, the combustor 20 may be an oxidizer such as that described in U.S. patent application Ser. No. 11/022,330, entitled “OXIDIZER FOR A FUEL CELL SYSTEM,” which was filed on Dec. 23, 2004, and is hereby incorporated by reference in its entirety. Alternatively, the combustor 20 may be a flare or oxidizer of a conventional design, as can be appreciated by one of ordinary skill in the art. Thus, many variations and designs are possible for the combustor 20, depending on the particular embodiment of the invention.
In accordance with some embodiments of the invention, the thermal exchangers 30 and 40 may be a coiled or plate-type thermal exchangers, depending on the particular embodiment of the invention. As a more specific example, the thermal exchanger 40 may have a design similar to a reactant conditioner described in U.S. patent application Ser. No. 11/319,042, entitled “HUMIDIFYING A REACTANT FLOW OF A FUEL CELL SYSTEM,” which was filed on Dec. 27, 2005, and is hereby incorporated by reference in its entirety.
As also depicted in
Other variations are possible and are within the scope of the appended claims. For example, referring to
Other and/or different thermal recovery devices may be integrated with the combustor 20, in accordance with other embodiments of the invention.
While the invention has been disclosed with respect to a limited number of embodiments, those skilled in the art, having the benefit of this disclosure, will appreciate numerous modifications and variations therefrom. It is intended that the appended claims cover all such modifications and variations as fall within the true spirit and scope of the invention.
This application claims the benefit under 35 U.S.C. §119(e) to U.S. Provisional Application Ser. No. 60/793,893, entitled “INTEGRATED EXHAUST COMBUSTOR AND THERMAL RECOVERY FOR FUEL CELLS,” which was filed on Apr. 21, 2006, and is hereby incorporated by reference in its entirety.
Number | Date | Country | |
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60793893 | Apr 2006 | US |