Abstract
Reactive capture of CO2(RCC) offers an integrated approach that combines CO2capture with its direct electrochemical conversion, eliminating the need for CO2release from the capture agent. By avoiding the pH, pressure, and temperature swings required for the release step, RCC has the potential to reduce both energy consumption and capital costs compared to the conventional sequential process of CO2capture, release, concentration, and conversion. Amines, widely used in industrial CO2capture, face challenges in RCC systems due to their incompatibility with transition metal catalysts as well as their tendency to promote electrode corrosion and parasitic hydrogen evolution. Identifying suitable combinations of amines and catalysts is therefore critical to enabling integrated CO2capture and conversion. This work systematically investigates the performance of four primary and four secondary amines for RCC on polycrystalline Cu catalysts. Among the eight tested amines, only dimethylamine showed no measurable Cu corrosion near the open circuit potential. In contrast, ammonia, methylamine, ethylamine, monoethanolamine, diethylamine, diethanolamine, and piperazine all induced Cu corrosion. Corrosion rates correlate with the pKaand steric hindrance of the amines, highlighting key parameters for catalyst–amine codesign. Grand canonical DFT calculations indicate a correlation between the adsorption strength of protonated amines, their pKa, and the extent of Cu corrosion, suggesting that both the surface binding of protonated amines and the lability of their protons play critical roles in corrosion acceleration near open circuit potentials. These finding suggest that amines with high pKavalues and weak binding of their protonated forms to Cu surfaces are preferred, as they offer better corrosion resistance.
| Original language | English |
|---|---|
| Pages (from-to) | 16009-16019 |
| Number of pages | 11 |
| Journal | Journal of Physical Chemistry C |
| Volume | 129 |
| Issue number | 36 |
| DOIs | |
| State | Published - Sep 11 2025 |
Funding
This work was supported as part of the Center for Closing the Carbon Cycle, an Energy Frontier Research Center funded by the U.S. Department of Energy, Office of Science, Basic Energy Sciences under Award Number DE-SC0023427. Our calculations utilized resources of Perlmutter of the National Energy Research Scientific Computing Center (NERSC) under Contract DE-AC02-05CH11231. Work by R.D.R. and C.H. was conducted under the auspices of the U.S. Department of Energy by Lawrence Livermore National Laboratory under Contract DE-AC52-07NA27344. LLNL release number: LLNL-JRNL-2005401.
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