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ADVANCED ENERGY SYSTEM WITH NUCLEAR REACTORS

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ADVANCED ENERGY SYSTEM WITH NUCLEAR REACTORS ( advanced-energy-system-with-nuclear-reactors )

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hydraulics and safety, material tests, operations, and maintenance obtained for or from Joyo and Monju. about 57 m about 57 m HX Fig. 12 Plant layout of indirect cycle Fig. 13 Bird’s-eye-view of the reactor building (b) Na-core-cooled S-CO2 gas-turbine indirect cycle plant Volume: 135,000 m3 (a) Conventional Na-core-cooled steam-turbine plant Volume: 160,000–170,000 m3 about 57 m about 57 m temperature greater than 40°C, wherein water serves as IV. WASTE HEFAigT. 1R4ECCoOmVpaEriRsoYn SofYpSlaTnEt vMolume in an S-CthOe2reinfdrigrecrtacnytcalendansdilaicsategaeml tausrbthineeacdyscolerbent. In contrast, Plant operation conditions of an S-CO2 FR are presented in Fig. 15. The pre-cooler and intercooler are cooled by seawater in the conventional cooling system and about 60% of the energy generated in the core is dissipated to the ocean as lukewarm water through this cooling. A new waste-heat recovery system was proposed for HTGRs using chemical and mechanical heat pump systems.4 The S-CO gas temperatures at the inlets of the low- 2 pressure and high-pressure compressors are 91°C and 69°C. Therefore, the waste heat at these temperatures is useful for cold heat supply through chemical and mechanical heat pump systems. The cold heat demand is high in urban areas such as for air conditioning. Two types of chemical heat pump systems exist: an adsorption refrigeration system and an absorption refrigeration system. The adsorption refrigeration system provides chilled water (<10°C) from a heat source with a 7 T:35.0 P:6.80 H:725.9 T:85.7 P:12.91 H:752.7 T:526.9 P:12.50 H:1315.9 Reactor or IHX T:387.8 P:12.80 H:1148.8 T:35.0 P:4.56 H:768.9 T:69.4 P : 6 . 8 4 H:790.2 T:91.4 P:4.60 H:836.6 High Pressure Compressor R & T Tu Re e u c R Re r r b cu u b ea V r V p p i a e e in n e er c c t s ss s e e & ra t o at o e el t l r o o r r Low Pressure Compressor Bypass Compressor Recuperator T:203.5 P:4.67 H:957.8 Fig. 15 Plant operation condition of a supercritical CO2 gas turbine fast reactor I IH H P & Pu X X& um mp p Generator Turbine T:192.1 P:12.86 H:913.9 T:Temperature(°C) P:Pressure(MPa) H:Specific EnthalpkyJ(/kg) Turbine & Compressor Efficiency: 90% Recuperator Efficiency: 95% Bypass Flow Fraction: 24.9% T:415.2 P:4.73 H:1192.6 Pre-cooler Intercooler about 68 m about 68 m about 51 m about 51 m

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