Research demonstrates efficient CO2 capture and electrochemical conversion in molten salts, highlighting potential for in-situ resource utilization on Mars.
This study employs a Li2CO3-CaCO3 molten salt system for CO2 capture from simulated Martian atmosphere (96% CO2, 2% N₂, 2% Ar) with simultaneous electrochemical conversion to carbon (C), carbon monoxide (CO), and oxygen (O2). Using an Fe-Ni alloy inert anode, we systematically investigated CO32 reduction mechanisms at the cathode, corrosion behavior of the Fe-Ni anode, oxygen evolution reactions, and temperature-dependent product distributions. Results demonstrate that cathodic CO32 reduction constitutes a diffusion-controlled irreversible process. Below 900°C, CO32 undergoes preferential reduction to solid carbon, where electrolysis at 880°C yields maximally graphitized carbon with an ID/IG ratio of 0.35. Above 900°C, CO formation dominates the reduction process, accounting for 36.5% of cathode gas at 930°C. The Fe-Ni alloy anode exhibits exceptional stability in molten salt, forming a protective Fe2O3-NiFe2O4 composite oxide layer during electrolysis that effectively safeguards the substrate. During anodic reactions, O2 discharge precedes CO32 oxidation, governed by O2 concentration gradients and diffusion kinetics within the molten salt, causing O2 concentration to increase with temperature until peaking at 83% at 880°C before declining markedly above 900°C.
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Xu et al. (2025) studied this question.
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