The utilization of sensible waste heat such as flue gas and industrial surplus heat is essential for energy saving.Supercritical CO2 power generation cycle is a promising way to be used in this field.In this paper,a new supercritical CO2 Rankine cycle coupled with an absorption refrigeration cycle is proposed,which consists of a reheating supercritical CO2 cycle,a mixed-effect LiBr-H2O absorption refrigeration cycle and solar subsystem including evacuated-tube collector and a hot water storage tank.The system has four variants according to the presence or absence of solar subsystem and net cooling energy output.The thermodynamic model of the proposed system was established and its performance was evaluated.The proposed system is able to realize cascade utilization of flue gas waste heat and efficient conversion of solar energy.It has much higher thermodynamic efficiency than the reference system (i.e.,the conventional supercritical CO2 Brayton cycle).Taking combined power and cooling system driven by flue gas waste heat and solar energy as an example,its thermal efficiency and exergy efficiency are 20.37％ and 54.18％ respectively,compared with the 14.74％ and 35.96％ of the reference system.Energy Utilization Diagrams (EUD) are implemented to investigate the irreversible losses and variation of the exergy destruction in the energy conversion process.Parametric analysis in two key parameters is conducted to provide guidance for the system optimal design.