Design method for s-CO2 gas turbine power plants

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2-2 Regenerative Brayton system 11 1200 1150 1100 1050 1000 950 900 200 300 400 500 600 700 800 P3 [bar] 100 90 80 70 60 50 200 300 400 500 600 700 800 P3 [bar] (a) Turbine inlet temperature. (b) CO2 mass flow. 98.8 98.6 98.4 98.2 98 97.8 97.6 200 300 400 500 600 700 800 P3 [bar] 100 90 80 70 60 50 40 30 20 200 300 400 500 600 700 800 P3 [bar] (c) Regenerator power. (d) Regenerator effectiveness. Figure 2-3: Turbine inlet temperature, CO2 mass flow rate, regenerator power and effectiveness for the regenerative Brayton system as a function of the compressor discharge pressure (ηTR = 50%, T2 = 31.25◦C, P2 = 74 bar, ηTR = 93.4%, ηCM = 85%, ηHR = 90%, ∆PLS = 2%, ∆TPN = 10◦C). mass flow rate decreases since the specific work is larger with increasing pressure ratios and therefore a lower mass flow is required to produce the fixed power of 18.7 MW. Similarly, larger pressure ratios reduce the temperature difference between the regeneration cold and hot sides, reducing the regenerator power and, since the pinch is fixed, reducing the effectiveness as well. 2-2-1 Compressor suction temperature and discharge pressure effect This section presents the analysis of analyzes the effects of the compressor suction temperature combined with the discharge pressure on the system performance. A chart showing the variation of the turbine inlet temperature and regenerator load as a function of these two variables is presented in Figure 2-4. Figure 2-4a shows the TIT, which has a steep variation in its slope at suction temperatures close to the critical one due to the sudden change of the specific enthalpy in the critical region. Notice that reducing the compressor suction temperature to values lower than the critical point one not reduce the TIT, which remains almost constant. This is a consequence Master of Science Thesis J.S. Bahamonde Noriega Q ̇RG [MW] T4 [◦C] εRG [%] f [kg/s]

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