Article ID Journal Published Year Pages File Type
7161828 Energy Conversion and Management 2015 11 Pages PDF
Abstract
It is shown that for the simple supercritical carbon dioxide cycle operating at hot source temperature equal 550 °C by employing 14.02 m2/kWe radiative cooler, it is possible to overcome the efficiency losses due to air cooling and the net output of the cycle improves by 5.0%. At hot source temperature equal 800 °C, the required radiative cooler area is 4.38 m2/kWe and respective performance improvement is equal 3.1%. For the recompression supercritical carbon dioxide cycle operating at hot source temperature equal 550 °C by employing 18.26 m2/kWe radiative cooler, it is possible to overcome the efficiency losses due to air cooling and the net output of the cycle improves by 7.5%. At hot source temperature equal 800 °C, the required radiative cooler area is 10.46 m2/kWe and respective performance improvement is equal 4.9%.
Related Topics
Physical Sciences and Engineering Energy Energy (General)
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