Abstract
In this paper, the S-CO2 cycle dynamic model considering the thermal inertia of the recuperator is constructed. The flow inertia is characterized by the total channel volume and the fluid volume flow. The heat transfer inertia is characterized by the heat transfer quantity and the thermal conductivity. The dynamic performances of the S-CO2 cycle under mass flow control and temperature control are compared. The changes of S-CO2 cycle dynamic performance parameters such as real-time efficiency and load change rate with the key design parameters of the recuperator are analyzed. The mathematical expression of S-CO2 cycle load change rate, fluid channel volume and thermal conductivity are fitted by multiple regression analysis method. The results show that the mass flow control is more effective. The efficiency loss is 0.72% and the load change rate is 10 %/min. When V=1.5V0 and kA=0.5kA0, the load change rate of S-CO2 cycle is the highest, which is 11.32 %/min.
Translated title of the contribution | Study on Characterization of Thermal Inertia of Recuperator Based on Analogy Idea and Its Influence on Load Change Rate of S-CO2 Cycle |
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Original language | Chinese (Traditional) |
Pages (from-to) | 1915-1921 |
Number of pages | 7 |
Journal | Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics |
Volume | 46 |
Issue number | 6 |
Publication status | Published - Jun 2025 |
Externally published | Yes |