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An example fuel cell arrangement includes a fuel cell stack configured to receive a supply fluid and to provide an exhaust fluid that has more thermal energy than the supply fluid. The arrangement also includes an ejector and a heat exchanger. The ejector is configured to direct at least some of the

An example fuel cell arrangement includes a fuel cell stack configured to receive a supply fluid and to provide an exhaust fluid that has more thermal energy than the supply fluid. The arrangement also includes an ejector and a heat exchanger. The ejector is configured to direct at least some of the exhaust fluid into the supply fluid. The heat exchanger is configured to increase thermal energy in the supply fluid using at least some of the exhaust fluid that was not directed into the supply fluid.

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1. A fuel cell arrangement comprising: a fuel cell stack configured to receive a supply fluid and to provide an exhaust fluid that has more thermal energy than the supply fluid;an ejector configured to separate the exhaust fluid into a first exhaust fluid stream and a second exhaust fluid stream, an

1. A fuel cell arrangement comprising: a fuel cell stack configured to receive a supply fluid and to provide an exhaust fluid that has more thermal energy than the supply fluid;an ejector configured to separate the exhaust fluid into a first exhaust fluid stream and a second exhaust fluid stream, and to direct the first exhaust fluid stream into the supply fluid, a mixture of the supply fluid and the first exhaust fluid stream being directly supplied from the ejector to the fuel cell stack;a heat exchanger configured to increases thermal energy in the supply fluid using the second stream of the exhaust fluid; andwherein the supply fluid and the exhaust fluid are air. 2. The fuel cell arrangement of claim 1, wherein the fuel cell stack comprises a plurality of solid oxide fuel cells. 3. The fuel cell arrangement of claim 1, wherein the mixture of the supply fluid and the first exhaust fluid stream is communicated to a plurality of cathodes in the fuel cell stack. 4. The fuel cell arrangement of claim 1, wherein the mixture of the supply fluid and the first exhaust fluid stream is at least 700 degrees Celsius just before entering the fuel cell stack. 5. The fuel cell arrangement of claim 1, wherein the heat exchanger comprises nickel. 6. The fuel cell arrangement of claim 1, wherein the first exhaust fluid stream is directed into the supply fluid at a location that is downstream from the heat exchanger. 7. The fuel cell arrangement of claim 1, wherein the second exhaust fluid stream is communicated through the heat exchanger to heat the supply fluid. 8. A thermal energy recycling method comprising: moving a supply fluid at a first temperature into a fuel cell stack;moving an exhaust fluid at a second temperature away from the fuel cell stack, the second temperature greater than the first temperature;transferring thermal energy from some of the exhaust fluid to the supply fluid within a heat exchanger;adding some of the exhaust fluid to the supply fluid after moving the supply fluid through the heat exchanger, the adding including entraining some of the exhaust fluid into the supply fluid using an ejector;directly supplying a mixture of the exhaust fluid and the supply fluid from the ejector to the fuel cell stack; andwherein the supply fluid and the exhaust fluid are air. 9. The fuel cell arrangement of claim 1 wherein the ejector directly receives the first exhaust fluid stream from the fuel cell stack. 10. The thermal energy recycling method of claim 8 wherein including entraining some of the exhaust fluid into the supply fluid using the ejector includes directly supplying some of the exhaust fluid from the fuel cell stack to the ejector.