Insights into the Mechanism of High CO<sub>2</sub> Selectivity over Co<sub>2</sub>C-Based Fischer–Tropsch to Olefins

The reasons for the too high CO2 selectivity (near 50 C %) in Co2C-based Fischer–Tropsch to olefins (FTO) are not clear. Water–gas-shift (WGS) side reaction is thought to be responsible for this, but in-depth research is lacking. Here, we revealed the mechanism of the too high CO2 selectivity in Co2C-based FTO. Kinetic studies showed that WGS reaction was more likely to occur than the hydrocarbon production reaction. In addition, a too severe WGS reaction would result in the formation of an H2-enriched and CO-deficient environment on the catalyst surface, which was not favorable for the generation of light olefins. Catalyst characterization results proved that the severe WGS reaction could also lead to the transformation of prismatic Co2C to spherical Co2C. Theoretical calculations demonstrated that prismatic Co2C (020) and Co2C (101) facets were dominant crystal facets for both FTO and WGS reactions. Furthermore, in situ diffuse reflectance infrared Fourier transform spectroscopy experiments found that the H2O produced in FTO completely participated in the WGS reaction. This clearly revealed why the CO2 selectivity was close to 50 C % in FTO. Therefore, we believed that accelerating the desorption of H2O on the catalyst surface and preventing its readsorption are the key elements for inhibiting CO2 formation in FTO.

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Publication Details

Journal
ACS Catalysis
Published
2025-04-15
DOI
https://doi.org/10.1021/acscatal.4c06992
Citations
8
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
3.11

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article

Insights into the Mechanism of High CO2 Selectivity over Co2C-Based Fischer–Tropsch to Olefins

Wenjie Xiang, Chuanhui Zhang, Hao Huang, Jinhu Wu et al.
8 citations
ACS Catalysis
Catalysts for Methane Reforming
3.11
article

Insights into the Mechanism of High CO2 Selectivity over Co2C-Based Fischer–Tropsch to Olefins

Wenjie Xiang, Chuanhui Zhang, Hao Huang, Jinhu Wu, Chao Feng, Noritatsu Tsubaki, Guangbo Liu, Da Wang, Zhihao Liu, Song Chen
article en
8 citations

Abstract

The reasons for the too high CO2 selectivity (near 50 C %) in Co2C-based Fischer–Tropsch to olefins (FTO) are not clear. Water–gas-shift (WGS) side reaction is thought to be responsible for this, but in-depth research is lacking. Here, we revealed the mechanism of the too high CO2 selectivity in Co2C-based FTO. Kinetic studies showed that WGS reaction was more likely to occur than the hydrocarbon production reaction. In addition, a too severe WGS reaction would result in the formation of an H2-enriched and CO-deficient environment on the catalyst surface, which was not favorable for the generation of light olefins. Catalyst characterization results proved that the severe WGS reaction could also lead to the transformation of prismatic Co2C to spherical Co2C. Theoretical calculations demonstrated that prismatic Co2C (020) and Co2C (101) facets were dominant crystal facets for both FTO and WGS reactions. Furthermore, in situ diffuse reflectance infrared Fourier transform spectroscopy experiments found that the H2O produced in FTO completely participated in the WGS reaction. This clearly revealed why the CO2 selectivity was close to 50 C % in FTO. Therefore, we believed that accelerating the desorption of H2O on the catalyst surface and preventing its readsorption are the key elements for inhibiting CO2 formation in FTO.

ACS CatalysisVol. 15(9)
Qingdao University (CN), Energy Institute (GB), Chinese Academy of Sciences (CN), Division of Materials Science and Engineering (AU), Shandong Lianxing Energy Group (China) (CN), Qingdao Institute of Bioenergy and Bioprocess Technology (CN), University of Toyama (JP)
National Natural Science Foundation of China
Zero hunger
Openalex Percentile: Top 8%
Catalysts for Methane Reforming
3.11
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