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of expansion units will have more crucial impact on the cycle efficiency than the efficiencies of compression units. 0.07 0.06 0.05 0.04 0.03 0.02 0.01 0 100 140 180 220 260 300 T expan. inlet [°C] 80% pump eff. 60% expan. eff. 80% pump eff. 70% 80% pump eff. 80% expan. eff. expan. eff. 200 bar gas 80 bar cond heater pressure ensing pressure 35 °C gas c 80% pump eff. 90% expan. eff. ooler outlet temperature Figure 3‐5 Carbon dioxide Brayton cycle efficiency vs. expansion inlet temperature against various expansion efficiencies (from EES, basic cycle without IHX) 0.07 0.06 0.05 0.04 0.03 0.02 0.01 0 100 140 180 220 260 300 T expan. inlet [°C] 60% 70% 80% 90% pump eff. 80% expan. eff. pump eff. 80% expan. eff. pump eff. 80% expan. eff. pump eff. 80% expan. eff. 200 bar gas heater pressure 80 bar condensing pressure 35 °C gas cooler outlet temperature Figure 3‐6 Carbon dioxide Brayton cycle efficiency vs. expansion inlet temperature against various pump efficiencies (from EES, basic cycle without IHX) 27 th thPDF Image | Thermodynamic Cycles using Carbon Dioxide
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