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Figure 7. Conceptual Plant Layout for a S-CO2 Power Conversion System With Two Separate Turbine/Generator Units and a Combined Turbine/Compressor Unit. ............................................................................................................................26 Figure 8. Conceptual Plant Layout for a S-CO2 Power Conversion System Showing a Pressurizer/Accumulator and an Emergency Core Cooling System. .........................27 Figure 9. Fuel Centerline Temperature at the Center of the Core as a Function of the Fuel Pin Diameter and the Coolant Fraction for 200 MWth. .............................................29 Figure 10. Cladding Temperature at the Center of the Core as a Function of the Fuel Pin Diameter and the Coolant Fraction for 200 MWth. ...................................................29 Figure 11. Average Core Pressure Drop as a Function of the Fuel Pin Diameter and the Coolant Fraction for 200 MWth.................................................................................30 Figure 12. Pumping Power Fraction as a Function of the Fuel Pin Diameter and the Coolant Fraction for 200 MWth.................................................................................30 Figure 13. Fuel Centerline Temperature at the Center of the Core as a Function of the Fuel Pin Diameter and the Coolant Fraction for 400 MWth. .............................................32 Figure 14. Cladding Temperature at the Center of the Core as a Function of the Fuel Pin Diameter and the Coolant Fraction for 400 MWth. ...................................................32 Figure 15. Average Core Pressure Drop as a Function of the Fuel Pin Diameter and the Coolant Fraction for 400 MWth.................................................................................33 Figure 16. Pumping Power Fraction as a Function of the Fuel Pin Diameter and the..................33 Figure 17. K-infinity as a Function of Operating History for a Power Density of 50 MW/MT, 20% CO2 Coolant, and Different Enrichments of UO2.........................35 Figure 18. keff as a Function of Operating History at 200 MW and 12.5% Enrichment. .............35 Figure 19. keff as a Function of Operating History at 200 MW and 12.0% Enrichment. .............36 Figure 20. Fuel Constituent Density as a Function of Operating History at 200 MW and 12.0% Enrichment. .....................................................................................................37 Figure 21. keff as a Function of Operating History at 400 MW and 12.0% Enrichment. .............37 Figure 22. Natural Circulation Results From Milone Compared With the SNL Lumped- Parameter Model. .......................................................................................................43 Figure 23. Natural Circulation Flow With Hot and Cold Legs.....................................................44 Figure 24. Lumped-Parameter Model of Natural Circulation Flow Through the Heat Rejection Heat Exchanger, Recuperator, and Reactor. ..............................................45 Figure 25. CD3-SC Model for a Reactor, Recuperator, and Heat Exchanger. .............................46 Figure 26. Schematic of the SNL S-CO2 Compression Loop Modified for Natural Circulation Flow Tests. ..............................................................................................47 Figure 27. Engineering Drawing of the S-CO2 Compression Loop With the Addition of a Head-Addition Heat Exchanger. ................................................................................48 Figure 28. Photo of the SNL S-CO2 Compression Loop. .............................................................48 6PDF Image | Supercritical CO2 Direct Cycle Gas Fast Reactor (SC-GFR)
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