Chinese Journal of Catalysis ›› 2026, Vol. 83: 419-431.DOI: 10.1016/S1872-2067(26)64965-0
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Cheng Raoa,b, Mengyu Qiana,b, Songyun Taoa,b, Huaiyuan Wanga,b, Dan Hec,*(
), Jun Yed, Hai Liud, Xiangguang Yanga,b, Yibo Zhanga,b,*(
)
Received:2025-08-19
Accepted:2025-10-27
Online:2026-04-18
Published:2026-03-04
Contact:
Dan He, Yibo Zhang
Supported by:Cheng Rao, Mengyu Qian, Songyun Tao, Huaiyuan Wang, Dan He, Jun Ye, Hai Liu, Xiangguang Yang, Yibo Zhang. Synergistic enhancement of methane combustion over Pd/CeO2 via single-atom Ni doping: Boosting Pd4+ and oxygen vacancies[J]. Chinese Journal of Catalysis, 2026, 83: 419-431.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(26)64965-0
Fig. 1. XRD patterns (a,b) and Raman patterns (c) of Pd/Ni1-CeO2 and related catalysts. High-resolution transmission electron microscope and spherical aberration electron microscopy images of CeO2 (d?f) and Ni1-CeO2 (g?i) catalysts.
Fig. 2. Spherical aberration electron microscopy images and the EDS mapping of Pd, Ni, Ce and O for Pd/CeO2 (a?f) and Pd/Ni1-CeO2 (g?l) catalysts and correspondingly mapping images.
Fig. 3. (a) Normalized Ni K-edge XANES spectra. (b) Fourier transforms of k3-weighted Ni K-edge EXAFS spectra for Pd/Ni1-CeO2, Ni foil, and NiO. (c) EXAFS spectrum fitting result of Pd/Ni1-CeO2 in R space. EXAFS wavelets transform images of Ni foil (d), NiO (e), and Pd/Ni1-CeO2 (f).
| Sample | Shell | CNa | R b (Å) | σ2 c (Å2) | ΔE0 d (eV) | R factor |
|---|---|---|---|---|---|---|
| Ni-foil | Ni-Ni | 12.0 | 2.485 ± 0.002 | 0.0062 | 7.7 | 0.0010 |
| NiO | Ni-O | 6.0±0.8 | 2.097 ± 0.014 | 0.0076 | 5.1 | 0.0057 |
| Ni-Ni | 12.5±1.0 | 2.948 ± 0.006 | 0.0076 | 1.1 | ||
| Pd/Ni1-CeO2 | Ni-O | 3.5±0.1 | 2.049 ± 0.002 | 0.0044 | ‒2.4 | 0.0046 |
| Ni-Ce | 1.1±0.1 | 3.046 ± 0.008 | 0.0022 | 0.3 |
Table 1 EXAFS fitting parameters at the Ni K-edge for various samples.
| Sample | Shell | CNa | R b (Å) | σ2 c (Å2) | ΔE0 d (eV) | R factor |
|---|---|---|---|---|---|---|
| Ni-foil | Ni-Ni | 12.0 | 2.485 ± 0.002 | 0.0062 | 7.7 | 0.0010 |
| NiO | Ni-O | 6.0±0.8 | 2.097 ± 0.014 | 0.0076 | 5.1 | 0.0057 |
| Ni-Ni | 12.5±1.0 | 2.948 ± 0.006 | 0.0076 | 1.1 | ||
| Pd/Ni1-CeO2 | Ni-O | 3.5±0.1 | 2.049 ± 0.002 | 0.0044 | ‒2.4 | 0.0046 |
| Ni-Ce | 1.1±0.1 | 3.046 ± 0.008 | 0.0022 | 0.3 |
Fig. 4. Catalytic activities of CeO2, Pd/CeO2 and Pd/Ni1-CeO2 catalysts. The conversion rate of methane at different temperatures (a), the activation energy (b), the reaction order of methane (c) and oxygen for catalytic methane combustion (d).
Fig. 5. (a) Methane oxidation activity under cyclic testing of Pd/Ni1-CeO2 catalyst. Stability test at 400 °C for 130 h (b), stability test against 5 vol% H2O (c) and stability test against 5 × 10-6 SO2 (d).
Fig. 6. Ni 2p (a), Pd 3d (b), O 1s (c) and Ce 3d (d) XPS spectra of CeO2, Ni1-CeO2, Pd/CeO2 and Pd/Ni1-CeO2 catalysts. The optimized computational models (e) and the differential charge density of Pd/Ni1-CeO2 (f) are illustrated. Color scheme: Pd, grey; Ce, chartreuse; Ni, purple; O, red; C, brown and H, white. The yellow and cyan areas represent the regions of electron gain and loss, respectively.
Fig. 8. In-situ DRIFTS study of CH4 adsorption and oxidation at 350 °C for different durations. Pd/CeO2 (1% CH4/Ar) (a), Pd/CeO2 (1% CH4/Air) (b), Pd/Ni1-CeO2 (1% CH4/Ar) (c) and Pd/Ni1-CeO2 (1% CH4/Air) (d). (e) DFT simulations of methane activation and the energy barriers over Pd/CeO2 and Pd/Ni1-CeO2. (initial state (IS), adsorbed state (*CH4), transition state (TS), and final state (*CH3+H). Color scheme: Pd, grey; Ce, chartreuse; Ni, purple; O, red; C, brown and H, white.
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