Synergistic electrode design for efficient CO<sub>2</sub> electrolysis to multicarbon products at elevated temperatures.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 41680197.
- Also identified by DOI 10.1038/s41467-026-69506-w and PMC identifier 13009509.
- Licence recorded as CC BY-NC-ND.
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Abstract
Electrocatalytic CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) technology holds significant industrial potential. However, when faced with elevated-temperature environments caused by industrial-scale operations, the fundamental understanding of temperature-dependent CO<sub>2</sub>RR behavior in flow cells remains elusive. This study points out that elevated-temperature operation (>333 K) presents both challenges and opportunities for multi-carbon (C<sub>2+</sub>) production. While elevated temperature enhances reaction kinetics and reduces thermodynamic energy barriers, it simultaneously induces reconstruction of Cu-based catalyst, accelerates gas diffusion electrode flooding, and promotes *CO desorption together with hydrogen evolution reaction, collectively suppressing C<sub>2+</sub> product formation and compromising long-term reactor stability. Through rational design of hydrophobic-enhanced Pd-Cu<sub>2</sub>O/polytetrafluoroethylene (PTFE)/Ag tandem electrodes, we overcome these challenges. Leveraging thermal reduced C-C coupling barriers, the optimized electrode achieves >70% Faradaic efficiency of C<sub>2+</sub> across industrially relevant current densities (200-1000 mA cm<sup>-2</sup>) at 348 K. This strategy converts elevated temperature adversity into a kinetic and thermodynamic advantage, boosting C<sub>2+</sub> cathodic energy efficiency by 1.3 times compared to ambient operation, establishing a promising paradigm for industrially viable CO<sub>2</sub> electrolysis.