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10 Proc IMechE Part A: J Power and Energy 0(0) As shown in Figure 13(a), the specific volume– pressure curve obtained by ideal gas model is almost consistent with that of real gas property when compressed air reaches supercritical condition (P > 3.85 MPa, T > 132.83 K), thus the expansion processes obtained by the two models are nearly the same and result in similar flow structure and path line distribution in Figures 9 and 10. In Figure 13(b), the specific heat capacity at constant pressure CP increases with the increase of tempera- ture for ideal gas model. However, it decreases with the increase of temperature when real gas property is adopted. In ideal gas model, static entropy and enthalpy are calculated from CP by equations (20) Figure 12. Comparison of rotor outlet parameters between real gas property and ideal gas model: (a) inlet-to-exit total tem- perature ratio; (b) inlet-to-exit total pressure ratio; (c) Mach number; (d) static entropy temperature ratio. Figure 13. Comparison of thermodynamic parameters between real gas property and ideal gas model: (a) variation of specific volume with pressure; (b) variation of CP with temperature.PDF Image | radial turbine supercritical compressed air energy storage
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