We demonstrate a carbon capture system based on pH swing cycles driven through proton-coupled electron transfer of sodium (3,3'-(phenazine-2,3-diylbis(oxy))bis(propane-1-sulfonate)) (DSPZ) molecules. Electrochemical reduction of DSPZ causes an increase of hydroxide concentration, which absorbs CO; subsequent electrochemical oxidation of the reduced DSPZ consumes the hydroxide, causing CO outgassing. The measured electrical work of separating CO from a binary mixture with N, at CO inlet partial pressures ranging from 0.1 to 0.5 bar, and releasing to a pure CO exit stream at 1.0 bar, was measured for electrical current densities of 20-150 mA cm. The work for separating CO from a 0.1 bar inlet and concentrating into a 1 bar exit is 61.3 kJ mol at a current density of 20 mA cm. Depending on the initial composition of the electrolyte, the molar cycle work for capture from 0.4 mbar extrapolates to 121-237 kJ mol at 20 mA cm. We also introduce an electrochemical rebalancing method that extends cell lifetime by recovering the initial electrolyte composition after it is perturbed by side reactions. We discuss the implications of these results for future low-energy electrochemical carbon capture devices.
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http://www.ncbi.nlm.nih.gov/pmc/articles/PMC9018824 | PMC |
http://dx.doi.org/10.1038/s41467-022-29791-7 | DOI Listing |
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