NiFe<sub>2</sub>O<sub>4</sub> spinel engineering for transcending the dilemma of activity-selectivity in CO<sub>2</sub> hydrogenation to ethanol.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 41353269.
- Also identified by DOI 10.1038/s41467-025-67269-4 and PMC identifier 12808233.
- Licence recorded as CC BY-NC-ND.
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Abstract
CO<sub>2</sub> hydrogenation to ethanol serves as a potential route for carbon neutrality and renewable energy utilization, while its practical application is severely limited by the activity-selectivity trade-off. This challenge primarily arises from the difficulty of C-C coupling and the occurrence of multiple side reactions. Herein, we design a NiFe<sub>2</sub>O<sub>4</sub> spinel-modified Fe<sub>2</sub>O<sub>3</sub> catalyst via a solid-state co-precipitation method, achieving a high CO<sub>2</sub> conversion rate of 49.3% with an ethanol space-time yield of 883.7 mg·g<sub>cat.</sub><sup>-1</sup>· h<sup>-1</sup>. Further mechanism investigation reveals that the incorporation of NiFe<sub>2</sub>O<sub>4</sub> spinel benefits the formation of active Fe<sub>5</sub>C<sub>2</sub> phase. Meanwhile, the interfacial sites between NiFe<sub>2</sub>O<sub>4</sub> and Fe<sub>2</sub>O<sub>3</sub> endow the catalyst with superior hydrogenation ability, which effectively inhibits excessive carbon chain growth and promotes the orientated synthesis of ethanol. This work proposes an inspiring NiFe<sub>2</sub>O<sub>4</sub> spinel engineering method for the efficient production of multi-carbon oxygenates from CO<sub>2</sub> hydrogenation.