Chinese Journal of Catalysis ›› 2025, Vol. 68: 366-375.DOI: 10.1016/S1872-2067(24)60188-9
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Miao Zhanga, Limin Zhanga, Mingrui Wanga, Guanghui Zhanga,*(), Chunshan Songa,b, Xinwen Guoa,*(
)
Received:
2024-08-31
Accepted:
2024-10-30
Online:
2025-01-18
Published:
2025-01-02
Contact:
* E-mail: Supported by:
Miao Zhang, Limin Zhang, Mingrui Wang, Guanghui Zhang, Chunshan Song, Xinwen Guo. The electronic interaction of encapsulating graphene layers with FeCo alloy promotes efficient CO2 Hydrogenation to light olefins[J]. Chinese Journal of Catalysis, 2025, 68: 366-375.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(24)60188-9
Fig. 1. Synthesis and microscopic analysis of Fe-based catalysts. (A) Schematic illustration of the synthesis of the samples. TEM and HRTEM images of fresh FeCoK@C (B,E), FeCoK-1 (C,F), and FeCoK-2 (D,G) catalysts.
Fig. 2. Structural characterizations of fresh catalysts. (A) XRD patterns of fresh Fe-based catalysts. C 1s (B) and Fe 2p (C) XPS spectra of fresh catalysts.
Fig. 3. Surface chemical properties of activated catalysts. C 1s (A) and Fe 2p (B) XPS spectra of activated FeCoK@C, FeCoK-1 and FeCoK-2. (C) CO2-TPD profiles of all activated Fe-based catalysts.
Fig. 4. Catalytic performances of the catalysts. (A) CO2 conversion and product selectivity over different Fe-based catalysts in CO2 hydrogenation. (B) C2-4= STY, C2-4 O/P, and chain growth factor α of different Fe-based catalysts. (C) Comparison between C2-4= STY over FeCoK@C and other Fe-based catalysts in previous reports. (D) Catalytic performance of FeCoK@C for 100 h stability test. Reaction conditions: 320 °C, 3.0 MPa, space velocity = 18000 mL·g-1·h-1, H2/CO2/N2 = 9/3/2, TOS = 8 h.
Fig. 6. Structural characterizations of spent catalysts and comparison of carburizing rates of catalysts from in-situ XRD during CO2 hydrogenation. (A) XRD patterns of spent catalysts. (B) The intensity ratio of the XRD peaks at 43.5° and 44.7° during CO2 hydrogenation. C 1s (C) and Fe 2p (D) XPS spectra of spent catalysts.
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