Chinese Journal of Catalysis ›› 2026, Vol. 84: 61-73.DOI: 10.1016/S1872-2067(26)65003-6
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Xintong Lva, Zhengchang Weia, Xin Denga, Yuchao Chaia, Guangjun Wua(
), Landong Lia,b(
)
Received:2025-10-29
Accepted:2025-11-24
Online:2026-05-18
Published:2026-04-16
Contact:
*E-mail: wuguangjun@nankai.edu.cn (G. Wu),Supported by:Xintong Lv, Zhengchang Wei, Xin Deng, Yuchao Chai, Guangjun Wu, Landong Li. Isolated Pt sites anchored by skeletal Fe in MFI zeolite nanosheets towards productive propane dehydrogenation[J]. Chinese Journal of Catalysis, 2026, 84: 61-73.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(26)65003-6
Fig. 1. Electron microscopy analyses of 0.3Pt2Fe@NS catalyst with Fe loading of 1.85 wt% and Pt loading of 0.14 wt%. (a-c) Aberration-corrected HAADF-STEM images. (d,e) High-magnification iDPC-STEM images viewed along the orientation of [010] with detailed zoomed-in areas processed high dynamic images and line scan intensity profiles of atoms as distance: Fe and Pt atoms marked by yellow dash circle and red arrows. (f) Elemental mappings for Si, O, Fe, and Pt.
Fig. 2. Characterization of as-prepared PtFe bimetallic catalysts. (a) H2-TPR profiles. (b) Pyridine-adsorbed IR spectra at 350 °C. (c) In-situ DRIFT spectra of CO adsorption on fresh (solid line) and reduced (dashed line) samples. Fe K-edge XANES (d) and EXAFS (e) spectra of 0.3Pt2Fe@NS sample under different treatment (F, R, S represent fresh, reduced, and spent sample after 30 h of PDH reaction, respectively). (f) Full-range EXAFS WT 2D plots for Fe-foil, Fe2O3, and 0.3Pt2Fe@NS catalyst.
Fig. 3. (a,b) Catalytic performance of various PtFe bimetallic catalysts. Reaction conditions: 0.1 g of catalyst, atmospheric pressure, C3H8/N2 = 1/2, WHSV = 15 h-1, 550 °C. (c) Experimental Arrhenius relationship for PDH reaction. Catalytic performance of 0.3Pt2Fe@NS under various reaction conditions (ambient pressure, 550 °C) (d) and under various WHSVs (ambient pressure, 550 °C, pure C3H8 feeding) (e). (f) Recyclability of 0.3Pt2Fe@NS. Upon the completion of a cycle, the catalyst was calcinated in a 20% O2/N2 atmosphere with linear heating to 550 °C and holding for another 3 h. (g) Comparison of the catalytic performance with reported systems in literature: Productivity of C3H6 versus deactivation rate, numbers adjacent to symbols correspond to the row numbers in Table S3.
Fig. 4. Color-mapping spectra of in-situ C3H8-DRIFT spectra in the C-H stretching vibration region and the hydroxyl region on 0.3Pt2Fe@NS (a), 0.3Pt/2Fe@NS (b), and 0.3Pt2Fe/NS (c) catalysts. MS signals of C3H8, C3H6, CH4, and H2 (m/z = 41, 29, 16, and 2) in TPSR experiments for 0.3Pt2Fe@NS (d), 0.3Pt/2Fe@NS (e), and 0.3Pt2Fe/NS (f) catalysts. Pulse reactions for propane conversion (g) and C3H8-D2 exchange reactions (h) over 0.3Pt2Fe@NS (i), 0.3Pt/2Fe@NS (ii), and 0.3Pt2Fe/NS (iii) catalysts.
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