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recompression cycles. Compressor designs were developed for a 500 MWth S-CO2 recompression cycle. The main compressor achieves an operating point total-to-static efficiency of 90.4 % and the recompressing compressor achieves 91.4 %. Further work can continue once these areas have been developed, including transient analysis, the effects of impurities on the system, and investigation of cycles which operate on other working fluids. Additionally, changes in the intermediate loop, the arrangement of the reactor vessel, and in-core changes will affect the efficiency of the SFR. These include the option of diluent grading in the fuel, flattening of the core outlet temperature profile, choosing Rankine or S-CO2 for the balance of plant, and heat exchanger design. All these have been evaluated for their impact on plant efficiency. It has been determined that the S-CO2 recompression cycle can provide efficiency benefits over conventional Rankine cycles for SFRs with core outlet temperatures at or above 510 oC. With the S-CO2 cycle, SFRs can achieve thermal efficiencies of ~42 %. Thesis Co-supervisor: Prof. Michael J. Driscoll Title: Professor Emeritus of Nuclear Science and Engineering Thesis Co-supervisor: Prof. Neil E. Todreas Title: Professor Emeritus of Nuclear Science and Engineering Thesis Co-supervisor: Dr. Pavel Hejzlar Title: Principal Research Scientist 4PDF Image | Supercritical Carbon Dioxide Cycle Analysis
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