Apr 8, 2025
2:30pm - 2:45pm
Summit, Level 4, Room 422
Dominic Ross1,Maxwell Goldman1,Aditya Prajapati1,Michell Marufu1,Jonathan Davis1,Jongmin Lee2,Michael Troksa1,Sarah Baker1,Po-Ya Abel Chuang3,Christopher Hahn1
Lawrence Livermore National Laboratory1,Paul Scherrer Institut2,University of California, Merced3
Dominic Ross1,Maxwell Goldman1,Aditya Prajapati1,Michell Marufu1,Jonathan Davis1,Jongmin Lee2,Michael Troksa1,Sarah Baker1,Po-Ya Abel Chuang3,Christopher Hahn1
Lawrence Livermore National Laboratory1,Paul Scherrer Institut2,University of California, Merced3
The major barriers to practical implementation of CO
2 electrolyzers are alleviating failure modes induced by water and alkali cation crossover from the anolyte. Electrolyzer failure caused by flooding of the gas diffusion electrode (GDE) or salt precipitation typically occur within the first 24 hours of electrolysis. Water and salt crossover are partially driven by electro-osmotic diffusion, and are thus dependent on the identity of the cations in the anolyte. To understand water crossover and its consequent effects on electrolyzer durability and selectivity we used operando neutron radiography to directly image water crossover of CO
2 to CO and CO
2 to C
2H
4 electrolyzers. In the case of the CO
2 to CO electrolyzer, we observed the water crossover with different alkali cations under working conditions from 100 to 1000 mA cm
-2. We found that the tighter hydration sphere of Cs
+ enables crossover at lower current densities which is observed as water flooding through the GDE into the flow fields. The larger hydration sphere of K
+ leads to the need for larger current densities to drive water crossover, but solubility differences between the corresponding carbonate salts lead to more catastrophic flooding/precipitation while using KOH anolyte at high current densities. With the CO
2 to C
2H
4 electrolyzer, we imaged the effect of minutes long regenerative pulses on water crossover. We found that these low current density pulses improved electrolyzer lifetime by allowing water through the back of the gas diffusion electrode and subsequently drying it back out. These results demonstrate the importance of direct operando understanding water crossover in order to tailor the catalyst microenvironment for electrolyzer scale-up and durability.
This work was conducted under the auspices of the U.S. Department of Energy by Lawrence Livermore National Laboratory (LLNL) under Contract DE-AC52-07NA27344.