Resumen
This paper presents performance analysis results on supercritical carbon dioxide (sCO2" role="presentation">??????2sCO2
s
C
O
2
) re-compression Brayton cycle. Monthly exergy destruction analysis was conducted to find the effects of different ambient and water temperatures on the performance of the system. The results reveal that the gas cooler is the major source of exergy destruction in the system. The total exergy destruction has the lowest value of 390.1 kW" role="presentation">390.1 kW390.1 kW
390.1
kW
when the compressor inlet temperature is near the critical point (at 35" role="presentation">3535
35
°C) and the compressor outlet pressure is comparatively low (24 MPa" role="presentation">24 MPa24 MPa
24
MPa
). The optimum mass fraction (x) and efficiency of the cycle increase with turbine inlet temperature. The highest efficiency of 49% is obtained at the mass fraction of x = 0.74 and turbine inlet temperature of 700 °C. For predicting the cost of the system, the total heat transfer area coefficient (UATotal" role="presentation">??????????????UATotal
U
A
T
o
t
a
l
) and size parameter (SP) are used. The UATotal" role="presentation">??????????????UATotal
U
A
T
o
t
a
l
value has the maximum for the split mass fraction of 0.74 corresponding to the maximum value of thermal efficiency. The SP value for the turbine is 0.212 dm at the turbine inlet temperature of 700 °C and it increases with increasing turbine inlet temperature. However the SP values of the main compressor and re-compressor increase with increasing compressor inlet temperature.