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stream are at 800°C and are therefore used as the heat source for the high temperature recuperating heat exchanger. The oxygen stream is further cooled to near ambient conditions in the low temperature recuperative heat exchanger, which preheats the incoming water. A little over 10% of the hydrogen and carbon dioxide stream is mixed with the incoming water and carbon dioxide and the remaining 90% go through the Sabatier reactor where it is converted to methane and water. The water is condensed in the condenser/separator and mixed with fresh water (main water stream). The methane with some hydrogen and water vapor is discharged out at the vapor side of the condenser/separator. The ratio of hydrogen flow to the combined inlet carbon dioxide and carbon monoxide flow was set to 3.5 by adjusting the water inflow. Figure 14. Process flow diagram of Sabatier process with co-electrolysis without heat recuperation 4. Co-electrolysis integrated Sabatier process: without heat recuperation option The integrated model of Sabatier and co-electrolysis processes was modified in which no heat recuperation option is included. The model is shown in Figure 14. This was done to determine the maximum amount or power that would be needed to make the Sabatier and co-electrolysis integrated process work. Water, carbon dioxide, and 16 American Institute of Aeronautics and AstronauticsPDF Image | CO2 and Steam Co-Electrolysis for Resource Utilization in Space
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