Carbon capture via electrochemically mediated alkaline absorption: Lab-scale continuous operation
Meng Shi, Sara Vallejo Castaño, Qingdian Shu, Michele Tedesco, Philipp Kuntke, H.V.M. Hamelers, Philip Loldrup Fosbøl
Abstract
Energy-efficient capture technologies need to be deployed by 2050 to abate global warming caused by excessive carbon dioxide (CO 2 ) emissions. CO 2 capture using alkaline solutions and absorbent regeneration mediated through bipolar membrane electrodialysis (BMED) have been tested previously as a standalone technology. However, the continuous operation of an integrated system remains largely unclear. Here, a bench-scale study was conducted using an integrated prototype to analyze the performance of CO 2 capture and electrochemical regeneration using potassium hydroxide (KOH) aqueous solution. A wide range of current densities from 150 to 1000 A/m 2 was applied to demonstrate the continuous operation of the CO 2 capture system emphasizing the stability in attainable high rich carbon loading and CO 2 desorption. The electrochemical regeneration module achieved CO 2 desorption efficiency of 70% and absorbent recovery up to 89% under industrial relevant current densities of 500–1000 A/m 2 . The absorbent recovery has been identified to be a result of the combined effect of load ratio and rich carbon loading. The observed inefficient CO 2 separation indicates significant potential to enhance energy efficiency. These results represent a pivotal step forward in electrochemically mediated CO 2 capture technology, with promising potential for rapid industrial scale-up in the near future.