Exploring Bipolar Membranes for Electrochemical Carbon Capture

Abstract

Carbon dioxide (CO2) must be removed from the atmosphere to mitigate the negative effects of climate change. However, the most scalable methods for removing CO2 from the air require heat from fossil-fuel combustion to produce pure CO2 and continuously regenerate the sorbent. Bipolar-membrane electrodialysis (BPM-ED) is a promising technology that uses renewable electricity to dissociate water into acid and base to regenerate bicarbonate-based CO2 capture solutions, such as those used in chemical loops of direct-air-capture (DAC) processes, and also in direct-ocean capture (DOC) to promote atmospheric CO2 drawdown via decarbonization of the shallow ocean. However, a lack of understanding of the mechanisms of reactive carbon species transport in BPMs has precluded industrial-scale deployment of BPM-ED. In this study, we develop an experimentally-validated 1D model for the electrochemical regeneration of CO2 from bicarbonate-based carbon capture solutions and seawater using BPM-ED. Our experimental and computational results demonstrate that out-of-equilibrium buffer reactions within the BPM drive the formation of CO2 at the BPM/electrolyte interface with energy-intensities of less than 150 kJ mol-1. However, high rates of bubble formation increase the energy intensity of CO2 recovery at current densities >100 mA cm−2. Sensitivity analyses show that optimizing the BPM and bubble removal could enable CO2 recovery from bicarbonate solutions at energy intensities <100 kJ mol−1 and current densities >100 mA cm−2. These results provide design principles for industrial-scale CO2 recovery using BPM-ED.