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Figure 5.1: The arrangement of components in the SFR balance of plant Figure 5.2: The design choices affecting efficiency that are considered in this study Figure 5.3: STEAM PRO 16 diagram of the Rankine Cycle Figure 5.4: Efficiency comparison with PCHEs for both the P-IHX and S-IHX Figure 5.5: Efficiency comparison with a PCHE for the P-IHX and a shell-and-tube S-IHX. Figure 5.6: Efficiency comparison with a shell-and-tube P-IHX and a PCHE for the S-IHX. Figure 5.7: Efficiency comparison with shell-and-tube heat exchangers for both the P-IHX and S-IHX. Figure 5.8: Efficiency comparison with no intermediate loop and a PCHE IHX Figure 5.9: Efficiency comparison with no intermediate loop and a shell-and-tube IHX Figure 5.10: Cost of JSFR steam generator for varying steam pressures Figure B.1: The RGRC input file Figure B.2: The beginning of an RGRC output file Figure C.1: The input file ihxNa_hyb.in with representative values Figure C.2: The output file ihxNa_hyb.out with representative values Figure D.1: The SoSaT input file, matching the steam generator of the JSFR Figure D.2: The SoSaT output file Figure D.3: The placement of the central downcomer in SoSaT 11PDF Image | Supercritical Carbon Dioxide Cycle Analysis
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