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Processes and systems for operating molten carbonate fuel cell systems are described herein. A process for operating a molten carbonate fuel cell system includes providing a hydrogen-containing stream comprising molecular hydrogen to an anode portion of a molten carbonate fuel cell; controlling a fl

Processes and systems for operating molten carbonate fuel cell systems are described herein. A process for operating a molten carbonate fuel cell system includes providing a hydrogen-containing stream comprising molecular hydrogen to an anode portion of a molten carbonate fuel cell; controlling a flow rate of the hydrogen-containing stream to the anode such that molecular hydrogen utilization in the anode is less than 50%; mixing anode exhaust comprising molecular hydrogen from the molten carbonate fuel cell with a hydrocarbon stream comprising hydrocarbons, contacting at least a portion of the mixture of anode exhaust and the hydrocarbon stream with a catalyst to produce a steam reforming feed; separating at least a portion of molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode.

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1. A process of operating a molten carbonate fuel cell, comprising: providing a hydrogen-containing stream comprising molecular hydrogen to an anode portion of a molten carbonate fuel cell;controlling a flow rate of the hydrogen-containing stream to the anode such that molecular hydrogen utilization

1. A process of operating a molten carbonate fuel cell, comprising: providing a hydrogen-containing stream comprising molecular hydrogen to an anode portion of a molten carbonate fuel cell;controlling a flow rate of the hydrogen-containing stream to the anode such that molecular hydrogen utilization in the anode is less than 50%;mixing anode exhaust comprising molecular hydrogen from the molten carbonate fuel cell with a hydrocarbon stream comprising hydrocarbons, wherein the anode exhaust mixed with the hydrocarbon stream has a temperature from 500° C. to 700° C.;contacting at least a portion of the mixture of anode exhaust and the hydrocarbon stream with a catalyst to produce a stream comprising one or more gaseous hydrocarbons, molecular hydrogen, and at least one carbon oxide;separating at least a portion of the molecular hydrogen from the stream comprising one or more gaseous hydrocarbons, molecular hydrogen, and at least one carbon oxide steam reforming feed; andproviding at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the hydrogen-containing stream comprising molecular hydrogen. 2. The process of claim 1, wherein the hydrogen-containing stream comprises at least 0.6 or at least about 0.95 mole fraction molecular hydrogen. 3. The process of claim 1, wherein at least some of the hydrocarbons of the hydrocarbon stream comprise one or more vaporizable hydrocarbons having a carbon number of at least 4. 4. The process of claim 1, further comprising feeding carbon dioxide to a cathode portion of the molten carbonate fuel cell in an amount such that partial pressure of carbon dioxide in a majority of the cathode portion of the molten carbonate fuel cell is higher than a partial pressure of carbon dioxide in a majority of an anode portion of the molten carbonate fuel cell. 5. The process of claim 4, wherein a difference between the partial pressure of carbon dioxide at the inlet or exhaust outlet of the cathode portion of the molten carbonate fuel cell and a partial pressure of carbon dioxide at the exhaust outlet of the anode portion of the molten carbonate fuel cell is at least 0.05 bara, or at least 0.1 bara, or at least 0.15 bara. 6. The process of claim 4, wherein at least a portion of the carbon dioxide provided to the cathode portion of the molten carbonate fuel cell is provided by a high temperature hydrogen-separation device. 7. The process of claim 1, further comprising, the steps of: separating at least a portion of a hydrogen-depleted gas stream comprising at least one of the carbon oxides and at least one of the gaseous hydrocarbons from the stream comprising one or more gaseous hydrocarbons, molecular hydrogen, and at least one carbon oxide, contacting at least a portion of the separated hydrogen-depleted stream with an oxidant to produce a heated stream, and providing at least a portion of the heat from the heated stream to the anode exhaust and/or to the hydrocarbon stream comprising hydrocarbons. 8. The process of claim 1, further comprising providing air and carbon dioxide to a cathode of the molten carbonate fuel cell, wherein the air comprises molecular oxygen, and controlling a flow rate of the air and/or carbon dioxide such that a molar ratio of carbon dioxide to molecular oxygen is at least 2. 9. The process of claim 1, further comprising mixing at least a portion of the molecular hydrogen provided to the molten carbonate anode with an oxidant at one or more anode electrodes in an anode of the molten carbonate fuel cell, and generating electricity from the molten carbonate fuel cell at an electrical power density of at least 0.1 W/cm2.