Thermo-economic analysis and optimization of a cascade transcritical carbon dioxide cycle driven by the waste heat of gas turbine and cold energy of liquefied natural gas

In this paper, a cascade transcritical carbon dioxide cycle is proposed to utilize the waste heat of gas turbine and the cold energy of liquefied natural gas (LNG). In the proposed system, the carbon dioxide of the bottom cycle and the top cycle are condensed at different pressures by LNG. Meanwhile, the LNG absorbs heat from carbon dioxide at different temperatures, leading to smaller temperature difference. The detailed models are established and the simulation results are discussed from the viewpoints of thermodynamics and economics. Under the design condition, the exergy destruction of the low-pressure condenser is the largest, followed by the high-pressure condenser. The investment cost of the high-temperature turbine is the highest. The exergy efficiency of the proposed cascade transcritical CO2 cycle first rises then drops as the split ratio and the pressure of high-pressure condenser increase. Moreover, the system exergy efficiency would increase as the inlet temperature of high-temperature turbine rises and decrease as the pressure of low-pressure condenser rises. Finally, the optimization results indicate that the maximum exergy efficiency of the proposed cascade transcritical carbon di -oxide cycle is 49.24%. The net power output of the optimal case is 15.53 MW, which is 6.14 MW higher than the reference system.

Automated summary

This paper proposes a cascade transcritical carbon dioxide cycle to utilize waste heat from a gas turbine and the cold energy of liquefied natural gas (LNG). Detailed models and simulation results are analyzed from the perspectives of thermodynamics and economics. The optimization results show that the maximum exergy efficiency of the proposed cascade transcritical CO2 cycle is 49.24%.