Minimizing CoxMn1-xO content in a Co2C catalyst for low CO2 selectivity in Fischer-Tropsch synthesis to olefins

• CO 2 selectivity on a high Co 2 C content catalyst for FTO is as low as 3.86%. • High WGSR activity originates from Co x Mn 1-x O rather than Co 2 C. • Na promotion enhances WGSR on Co x Mn 1-x O, leading to high CO 2 selectivity. • CO 2 selectivity remains low in Co 2 C-rich catalysts, even with Na increased to 0.8%. The Co 2 C-based catalyst is a promising candidate for the Fischer-Tropsch to olefins reaction. However, it consistently exhibits high CO 2 selectivity (∼40 %), and the origin of the high activity in the water–gas-shift reaction is not well-understood. In this study, Co 2 C catalysts constructed with the same elemental compositions but using the melting and co-precipitation methods resulted in drastic differences in CO 2 selectivity − one at 3.8 % and the other at 35.3 %. A detailed structural study revealed that the presence of Co x Mn 1-x O instead of Co 2 C is responsible for the elevated CO 2 selectivity. Interestingly, Co x Mn 1-x O alone demonstrates limited CO 2 selectivity, but when promoted with Na, its WGSR activity is greatly enhanced. Conversely, the catalysts maintained consistently low CO 2 selectivity even with improved Na content, as long as a high fraction of Co 2 C is present. This finding is important for designing Co 2 C-based catalysts that can achieve high olefin selectivity while minimizing undesirable CO 2 emissions.

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Publication Details

Journal
Journal of Catalysis
Published
2024-11-23
DOI
https://doi.org/10.1016/j.jcat.2024.115856
Citations
1
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.11

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article

Minimizing CoxMn1-xO content in a Co2C catalyst for low CO2 selectivity in Fischer-Tropsch synthesis to olefins

Xiaojun Lu, Diane Hildebrandt, Jiabing Chen, Jiayin Liang et al.
1 citations
Journal of Catalysis
Catalysts for Methane Reforming
0.11
article

Minimizing CoxMn1-xO content in a Co2C catalyst for low CO2 selectivity in Fischer-Tropsch synthesis to olefins

Xiaojun Lu, Diane Hildebrandt, Jiabing Chen, Jiayin Liang, Xinying Liu, Yiwen Liu, Yibo Tang, Sheng Zhan, Mengheng Wang
article en
1 citations

Abstract

• CO 2 selectivity on a high Co 2 C content catalyst for FTO is as low as 3.86%. • High WGSR activity originates from Co x Mn 1-x O rather than Co 2 C. • Na promotion enhances WGSR on Co x Mn 1-x O, leading to high CO 2 selectivity. • CO 2 selectivity remains low in Co 2 C-rich catalysts, even with Na increased to 0.8%. The Co 2 C-based catalyst is a promising candidate for the Fischer-Tropsch to olefins reaction. However, it consistently exhibits high CO 2 selectivity (∼40 %), and the origin of the high activity in the water–gas-shift reaction is not well-understood. In this study, Co 2 C catalysts constructed with the same elemental compositions but using the melting and co-precipitation methods resulted in drastic differences in CO 2 selectivity − one at 3.8 % and the other at 35.3 %. A detailed structural study revealed that the presence of Co x Mn 1-x O instead of Co 2 C is responsible for the elevated CO 2 selectivity. Interestingly, Co x Mn 1-x O alone demonstrates limited CO 2 selectivity, but when promoted with Na, its WGSR activity is greatly enhanced. Conversely, the catalysts maintained consistently low CO 2 selectivity even with improved Na content, as long as a high fraction of Co 2 C is present. This finding is important for designing Co 2 C-based catalysts that can achieve high olefin selectivity while minimizing undesirable CO 2 emissions.

Journal of CatalysisVol. 441
Rutgers, The State University of New Jersey (US), African Leadership Institute (ZA), Wuhan Institute of Technology (CN)
Wuhan Institute of Technology, Key Technologies Research and Development Program, National Key Research and Development Program of China
Openalex Percentile: Top 65%
Catalysts for Methane Reforming
0.11
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