Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7161828 | Energy Conversion and Management | 2015 | 11 Pages |
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)
Authors
Mehdi Zeyghami, Fardin Khalili,