Abstract
The electrochemical conversion of captured CO2 – also known as reactive capture – offers a promising approach to produce renewable carbon monoxide (CO) while bypass the energy and cost-intensive CO2 capture, purification and pressurization processes at large scale. However, current reactive capture systems suffer from low CO selectivity (< 50 %) and productivity (< 100 mA cm⁻2) due to the lack of efficient electrocatalysts and limited CO2 availability at the reactive interfaces. Here, we develop a coupled catalyst and microenvironment strategy to overcome these barriers. Employing Ni single-atom catalysts with a high density of reactive sites (Ni loading up to 3.0 wt%), together with enhanced CO2 regeneration and transport to the catalyst via local hydrophobicity control, we achieved efficient CO production with a Faradaic efficiency of 68 % at 100 mA cm⁻2 with stable performance maintained over 100 h in a hydroxide-mediated reactive capture system. The system achieved a CO energy efficiency of 27 % and an energy intensity of 37.7 GJ ton⁻¹CO, outperforming the best reported amine- and hydroxide-based reactive capture processes operating at ambient temperature and pressure.
| Original language | English |
|---|---|
| Article number | 126068 |
| Journal | Applied Catalysis B: Environmental |
| Volume | 383 |
| DOIs | |
| State | Published - Apr 2026 |
| Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2025 The Authors
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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SDG 13 Climate Action
Keywords
- CO reduction
- CO regeneration
- Microenvironment control
- Ni single-atom catalyst
- Reactive capture
ASJC Scopus subject areas
- Catalysis
- General Environmental Science
- Process Chemistry and Technology
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