Designing Cu<sup>0</sup>-Cu<sup>+</sup> dual sites for improved C-H bond fracture towards methanol steam reforming.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 38042907.
- Also identified by DOI 10.1038/s41467-023-43679-0 and PMC identifier 10693576.
- Licence recorded as CC BY.
- The licence permits redistribution, so the abstract is shown in full and the full text is available from the publisher.
Abstract
Copper-based catalysts serve as the predominant methanol steam reforming material although several fundamental issues remain ambiguous such as the identity of active center and the aspects of reaction mechanism. Herein, we prepare Cu/Cu(Al)O<sub>x</sub> catalysts with amorphous alumina-stabilized Cu<sub>2</sub>O adjoining Cu nanoparticle to provide Cu<sup>0</sup>-Cu<sup>+</sup> sites. The optimized catalyst exhibits 99.5% CH<sub>3</sub>OH conversion with a corresponding H<sub>2</sub> production rate of 110.8 μmol s<sup>-1</sup> g<sub>cat</sub><sup>-1</sup> with stability over 300 h at 240 °C. A binary function correlation between the CH<sub>3</sub>OH reaction rate and surface concentrations of Cu<sup>0</sup> and Cu<sup>+</sup> is established based on kinetic studies. Intrinsic active sites in the catalyst are investigated with in situ spectroscopy characterization and theoretical calculations. Namely, we find that important oxygen-containing intermediates (CH<sub>3</sub>O* and HCOO*) adsorb at Cu<sup>0</sup>-Cu<sup>+</sup> sites with a moderate adsorption strength, which promotes electron transfer from the catalyst to surface species and significantly reduces the reaction barrier of the C-H bond cleavage in CH<sub>3</sub>O* and HCOO* intermediates.