Facet-engineered CeO2 supports tune single-atom Ru catalysts for biomass conversion.
Ru1/CeO2-C achieves 86.9% yield of 2-butanol with high catalytic activity.
(100) facets create more oxygen vacancies and stronger metal–support interactions.
Enhanced hydrogen transfer and C–C cleavage improve reaction efficiency.
Provides a strategy to design high-performance catalysts for biomass upgrading.
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| Zhang S., Liu F., Zhang Y., et al. (2026). CeO2 facet-directed interfacial engineering in Ru1/CeO2 catalysts for efficient 2-butanol production from levulinic acid. The Innovation Energy 3:100156. https://doi.org/10.59717/j.xinn-energy.2026.100156 |
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(A) Schematic illustration of the preparation process for Ru1CeO2 catalysts via facet engineering and photodeposition. (B) XRD patterns of CeO2 supports and Ru1CeO2 catalysts. (C) N2-sorption isotherms and (D) pore size distribution curves of catalysts. (E) SEM images, (F&G) TEM images, and (k) AC-HAADF-STEM image and elemental mapping of Ru1CeO2-C. (H) SEM images, (I&J) TEM images, and (l) AC-HAADF-STEM image and elemental mapping of Ru1CeO2-S.
In situ CO-DRIFTS of (A) Ru1CeO2-C and (B) Ru1CeO2-S. (C) Ru K-edge XANES spectra and (D) FT-EXAFS spectra of Ru1CeO2-C and Ru1CeO2-S, with Ru foil and RuO2 provided as references. (E) EXAFS fitting curves at the Ru K-edge for both catalysts. R-space fitting results of the EXAFS spectra for (F) Ru1CeO2-C and (G) Ru1CeO2-S. Calculated work functions of (H) Ru1CeO2-C and (I) Ru1CeO2-S.
(A) Ce 3d XPS spectra, (B) O 1s XPS spectra, (C) Ru 3p XPS spectra, (D) Raman spectra, (E) EPR spectra, and (F) Py-FTIR spectra of samples.
(A) Proposed reaction pathway for LA hydrodeoxygenation to 2-butanol. (B) Conversion of LA over different catalysts. Time evolution of product distributions in LA hydrodeoxygenation over (C) Ru1CeO2-C and (D) Ru1CeO2-S catalysts. Determination of apparent reaction orders with respect to (E) GVL concentration and (F) H2 pressure during GVL hydrodeoxygenation. (G) Apparent reaction orders with respect to H2 pressure in 1,4-PDO hydrodeoxygenation. (H) Catalytic activity of Ru1CeO2-C and Ru1CeO2-S for the conversion of key reaction intermediates. (I) Substrate scope evaluation: catalytic conversion of various levulinates over Ru1CeO2-C. (J) Recycling tests of Ru1CeO2-C in the catalytic GVL hydrodeoxygenation (Reaction conditions: 0.07 g catalyst, 0.14 g GVL, 8.65 mL IPA, 190 °C, 5 MPa H2, and 8 h).
(A) Comparison of TON and TOF for Ru1CeO2-C and Ru1CeO2-S catalysts in LA hydrodeoxygenation. Apparent activation energy of (B) Ru1CeO2-C and (C) Ru1CeO2-S catalysts in GVL hydrodeoxygenation. In situ DRIFTS of the interaction/reaction (D) between Ru1CeO2-C and 1,4-PDO, (E) between Ru1CeO2-S and 1,4-PDO, (F) between catalysts and 1,4-PDO at 60 min, (Gg) between IPA and Ru1CeO2-C, (H) between IPA and Ru1CeO2-S, and (I) between catalysts and IPA at 60 min.
(A) Calculated energy profiles for GVL ring-opening reaction on Ru1CeO2-C (100) and Ru1CeO2-S (111) surfaces. (B) Projected density of state (PDOS) for Ru1CeO2 catalysts and electron transfer analysis. (C) Optimized geometric configurations for GVL-ring-opening reactions.