کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
1744290 | 1522130 | 2016 | 11 صفحه PDF | دانلود رایگان |

• Multi-objective optimisation of a non-selective Rectisol™ unit for carbon capture.
• Heat integration opportunities are explored.
• Multi-stage refrigeration system optimisation within an Excel based MOO framework.
• Pocket exploitation based on the grand composite curve.
• CO2 condensation and pumping performs better than straightforward CO2 compression.
In the present work, a standalone Rectisol™ unit for carbon capture has been optimised with a Multi-Objective Optimisation (MOO) perspective. The energy penalty and carbon dioxide capture rate have been simultaneously optimised to get the best operating conditions for various carbon dioxide capture rates. The Rectisol™ process typically has high refrigeration demand. Hence, any optimisation of Rectisol™ is incomplete without simultaneous optimisation of the refrigeration system. Hence, in this work, the refrigeration system has also been optimised with the help of a separate algorithm. Two options for pressurising the captured carbon dioxide, i.e. by condensation and pumping the carbon dioxide (Case-I) and by compression (Case-II), have also been compared. The results show that Case-I performs better for low capture rates compared to Case-II. However, the relative difference between the two diminishes with increasing capture rates.
Journal: Journal of Cleaner Production - Volume 119, 15 April 2016, Pages 196–206