Commercialization of emerging power-to-X conversion technologies
requires efficient integration and recovery of heat and waste within
existing chemical plants. The electrochemical reduction of CO2 fits such a scope, yet current research largely neglects
the prospect of elevated temperature operation, which is likely to
occur due to Joule heating and cooling constraints. Here, we set out
to investigate the performance of liquid-fed CO2 electrolyzers
at temperatures of up to 85 °Ca threshold that exacerbates
commonly met stability issues and leads to electrolyzer failure. To
prevent the latter, our study first explores the interrelationships
between elevated temperature operation, evaporation, gas solubility,
electro-wetting, and how they affect performance. At 25 °C, unity
selectivity to formate is demonstrated over the course of 24 h. However,
at 85 °C, we show that fine optimization of differential pressure
(28–40 mbar) has to be carried out to stabilize performance.
Ultimately, a faradaic efficiency of 64% could be maintained after
24 h of electrolysis at −100 mA cm–2a
68% improvement relative to the nonoptimized system. The substrate-dependent
rate of performance decline at 85 °C, which is not distinguishable
at ambient temperatures, underscores the necessity for a tailored
system and differential pressure control for CO2 electrolysis
at elevated temperatures.