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Design method for s-CO2 gas turbine power plants

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Design method for s-CO2 gas turbine power plants ( design-method-s-co2-gas-turbine-power-plants )

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2-5 Overall comparison 31 the cooler, which is a similar result to that obtained in the regenerative Brayton system. However, in this case the pump shares a very small amount of the losses, which is expected since the compressibility of the CO2 is lower in the liquid phase that in the critical region, which reduces the compression work. 2-5 Overall comparison This section presents a comparison between the regenerative and the recompression Brayton systems in an attempt to identify the best features of each configuration. The Rankine configuration is not further considered, as explained in Section 2-4-2. The parameters in Table 2-2 regarding the characteristics of the components and the system are used in this section. The TIT, CO2 mass flow rate, regenerator power and regenerator effectiveness are calculated as a function of the discharge pressure. The results are presented in Figure 2-30. 1200 1100 1000 900 800 700 200 300 400 500 600 P3 [bar] Regenerative Recompression 160 140 120 100 80 60 200 300 400 500 600 P3 [bar] Regenerative Recompression (a) Turbine inlet temperature. (b) CO2 mass flow. 99 98 97 96 95 94 93 92 91 90 200 300 400 500 600 P3 [bar] Regenerative Recompression 1 Recompression 2 100 90 80 70 60 50 40 30 200 300 400 500 600 P3 [bar] Regenerative Recompression (c) Regenerator power. (d) Regenerator effectiveness. Figure 2-30: TIT, CO2 mass flow rate, regenerator power and effectiveness as a function of the compressor discharge pressure for the s-CO2 regenerative and recompression Brayton power systems (ηTR = 50%, T2 = 31.25◦C, P2 = 74 bar, ηTR = 93.4%, ηCM1 = 85%, ηCM2 = 85%, ηHR = 90%, ∆PLS = 2%, ∆TPN = 10◦C). The Brayton recompression system presents better characteristics than the Brayton regen- Master of Science Thesis J.S. Bahamonde Noriega Q ̇RG [MW] T4 [◦C] εRG [%] f [kg/s]

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