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. 2025 Jan 16;16(1):736.
doi: 10.1038/s41467-025-56161-w.

Tunning valence state of cobalt centers in Cu/Co-CoO1-x for significantly boosting water-gas shift reaction

Affiliations

Tunning valence state of cobalt centers in Cu/Co-CoO1-x for significantly boosting water-gas shift reaction

Xing-Chi Li et al. Nat Commun. .

Abstract

Dual active sites with synergistic valence state regulation under oxidizing and reducing conditions are essential for catalytic reactions with step-wise mechanisms to modulate the complex adsorption sites of reactant molecules on the surfaces of heterogeneous catalysts with maximized catalytic performances, but it has been rarely explored. In this work, uniformly dispersed CuCo alloy and CoO nanosheet composite catalysts with dual active sites are constructed, which shows huge boost in activity for catalyzing water-gas shift reaction (WGSR), with a record high reaction rate reaching 204.2 μmolCO gcat.-1 s-1 at 300 °C for Cu1Co9Ox amongst the reported Cu-based and Co-based catalysts. A synergistic mechanism is proposed that Coδ+ species can be easily reduced by CO adsorbed on Cu and Co0 can be oxidized by H2O. Systematic in situ characterization results reveal that the addition of Cu can regulate the redox properties of Co species and thus modulate the adsorption properties of catalysts. Particularly, doping of Cu0 sites weakens the affinity of the surface to CO or CO2 to a moderate level. Moreover, it also promotes the oxidation of *CO to *COOH and the desorption of the product CO2, reducing the carbon poisoning of the catalyst and thus increasing the reactivity. The results would provide guidance for the construction of novel heterogeneous catalyst with dual active sites and clarify its underlying reactivity enhancement mechanism induced by the tunning of valence state of metal centers for heterogeneous catalytic reactions.

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Conflict of interest statement

Competing interests: The authors declare no competing interests.

Figures

Fig. 1
Fig. 1. Catalytic performance of the CuaCobOx catalysts.
a Temperature-dependent activities of the catalysts (reaction atmosphere was 2%CO/10%H2O/88%N2). b Comparison of reaction rates with other catalysts of transition metals. c The long-term stability at a high GHSV (Cu1Co9Ox: 240 °C, GHSV = 140,000 mL g−1 h−1; Co3O4: 240 °C, GHSV = 42,000 mL g−1 h−1). d Arrhenius plots for activation energy, e CO reaction order and f H2O reaction order of Cu1Co9Ox and Co3O4 catalysts.
Fig. 2
Fig. 2. Characterizations of the CuaCobOx catalysts.
The aberration-corrected HAADF-STEM images and corresponding EDS elemental maps of ac Cu1Co9Ox and df Co3O4 after WGSR.
Fig. 3
Fig. 3. Structural evolution of the CuaCobOx catalysts.
a XRD patterns of the catalysts after WGSR. In situ XRD pattern of b Cu1Co9Ox and c Co3O4 catalysts. d H2-TPR, e H2-TPR after 5%H2/Ar reduction at 300 °C and f H2-TPR after WGSR of CuaCobOx catalysts. g CO-TPSR after WGSR of Cu1Co9Ox catalysts. h Schematic illustration of structure evolution of Cu1Co9Ox catalysts during WGSR.
Fig. 4
Fig. 4. Identification of electronic structures of the CuaCobOx catalysts under WGSR.
a Quasi in situ XANES and b EXAFS results of the Co3O4 and Cu1Co9Ox catalysts after WGSR. Quasi in situ XPS spectra of c Cu LMM, d Co 2p and e O 1s of the Co3O4 and Cu1Co9Ox catalysts after WGSR. f In situ Raman spectra of the Co3O4 and Cu1Co9Ox catalysts under WGSR condition (250 °C, 2%CO/3%H2O/Ar).
Fig. 5
Fig. 5. Investigation of actual active sites and mechanism of the CuaCobOx catalysts under WGSR.
In situ DRIFTS results of ac Co3O4 and df Cu1Co9Ox catalysts under 2%CO/3%H2O/He reaction atmosphere at different temperatures. g Gibbs Free energy diagram for COOR processes on the surface of Co-Cu alloy(100), Co(100) and CoO(110). Orange, blue, gray, green and purple atoms are corresponding to Co, Cu, C, O and H sites, respectively.
Fig. 6
Fig. 6. Investigation of mechanism and the valence shift between Co0 and Coδ+ to facilitate the H2O dissociation.
a CO surface reaction results of the Cu1Co9Ox catalyst. In situ DRIFTS results of b Co3O4 and c Cu1Co9Ox catalysts after switching gas mixture from 2%CO/3%H2O/He to 3%H2O/He at 240 °C. d NAP-XPS of Cu1Co9Ox catalysts under 2 mbar 10%CO/Ar and 2 mbar 5%H2O/Ar at 300 °C. In situ Raman spectra of e Cu1Co9Ox and f Co3O4 catalysts under 2%CO/Ar and 3%H2O/Ar at 300 °C. g Schematic illustration of the dual active centers for WGSR.

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