TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Method: The method further comprises: recycling at least a portion of the streams comprising gaseous or liquid products to form at least a portion of a cathode inlet stream; adjusting a composition of the anode exhaust, the portion of the anode exhaust before carbon dioxide is separated, the carbon dioxide-depleted gas stream, and/or the portion of the carbon dioxide-depleted gas stream before being used in the ammonia synthesis process; withdrawing, from a cathode exhaust, a gas stream comprising nitrogen; using at least a portion of the withdrawn gas stream comprising nitrogen as a source of nitrogen in the ammonia synthesis process; using at least a portion of the carbon dioxide-rich stream in a second synthesis process for forming an organic nitrogen-containing compound; and performing an effective amount of an endothermic reaction to maintain a temperature differential between an anode inlet and an anode outlet of less than or equal to 100 degrees C. The step of using at least a portion of the carbon dioxide-depleted gas stream comprises exposing the portion of the carbon dioxide-depleted gas stream to a catalyst under effective ammonia synthesis conditions. The exposing step further comprises forming at least one ammonia-containing stream and one or more streams comprising gaseous or liquid products. The step of adjusting the composition comprises performing a water gas shift process, and performing a separation to reduce a water content of the composition and/or performing a separation to reduce a carbon dioxide content of the composition. The second synthesis process further comprises using ammonia from the ammonia synthesis process to form the organic nitrogen-containing compound. Preferred Components: The streams comprising gaseous or liquid products include at least one stream comprising hydrogen and/or methane. The portion of the carbon dioxide-depleted gas stream is formed by separating a hydrogen-concentrated stream from the carbon dioxide-depleted gas stream, where the separated hydrogen-concentrated stream comprises at least 95 vol.% of hydrogen. The anode exhaust has a molar ratio of hydrogen: carbon monoxide of 3:1. The effective ammonia synthesis conditions comprise a pressure of 6-18 MPa and a temperature of 350-500 degrees C. The cathode inlet stream comprises exhaust from a combustion turbine. The molten carbonate fuel cell is operated at a thermal ratio of 0.25-1. An amount of the reformable fuel introduced into the anode and/or the internal reforming element associated with the anode provides a reformable fuel surplus ratio of 1.5. A ratio of net moles of syngas in the anode exhaust to moles of carbon dioxide in a cathode exhaust is 2. A fuel utilization in the anode is less than or equal to 50%, and a carbon dioxide utilization in the cathode is 60%. The molten carbonate fuel cell is operated to generate electrical power at a current density of 150 mA/cm2 and waste heat of 40 mW/cm2. The step of performing the endothermic reaction consumes 40% of the waste heat. An electrical efficiency for the molten carbonate fuel cell is 10-40%, and a total fuel cell efficiency for the molten carbonate fuel cell is 55%.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Components: The 90 vol.% of the reformable fuel is methane. EXAMPLE - No suitable example given.