Mechanistic Insights into Synergistic Enhancement of Linear α-Olefins Selectivity over Ca–Na Modified Fe<sub>5</sub>C<sub>2</sub>–ZnO Catalysts in CO Hydrogenation

Selective synthesis of long-chain linear α-olefins (LAOs) from syngas remains a fundamental challenge due to competitive hydrogenation and water–gas shift (WGS) reactions. Herein, we report that CaO- and Na2O-promoted Fe5C2–ZnO catalyst (FeZnCaNa) demonstrates prominent performance and stability in CO hydrogenation to LAOs, which achieved 97.4% of CO conversion, 73.7% of LAOs in C4+ olefins with LAOs space-time yield of 304.4 mg·gcat–1·h–1 at 320 °C, 2.0 MPa. Comparative studies of modification with other alkaline earth metals (Mg, Sr, and Ba) underscored the unique promotional role of Ca in enhancing LAOs yield. The characterizations revealed that CaO accelerated the transformation of ZnFe2O4 into dispersed χ-Fe5C2 domains anchored at the ZnO interface. These iron carbide domains served as the principal active sites for the CO dissociation and C–C coupling. The Ca–Na–ZnO matrix modulated surface basicity, facilitating olefin desorption, and suppressing secondary hydrogenation. The ratio of olefin/paraffin attained 4.5, 58.6% of α-olefins in hydrocarbons, and suppressed CH4 selectivity to 8.1%. In situ spectroscopic analyses further explained that CaO–Na2O incorporation promoted CHx formation, thereby accelerating chain propagation. The catalyst also exhibited a reduced CO2 selectivity of 30.5%, attributed to the attenuated WGS activity resulting from decreased H2O adsorption during hydrocarbon formation. This study uncovers a dual-site mechanism, offering insights for designing efficient Fe-based catalysts for viable syngas-to-olefins conversion.

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Publication Details

Journal
ACS Catalysis
Published
2025-09-19
DOI
https://doi.org/10.1021/acscatal.5c04615
Citations
3
Primary Topic
Catalysts for Methane Reforming
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article
Field-Weighted Citation Impact
1.17
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article

Mechanistic Insights into Synergistic Enhancement of Linear α-Olefins Selectivity over Ca–Na Modified Fe5C2–ZnO Catalysts in CO Hydrogenation

Qiwen Sun, Hengxuan Zhang, Zixing Shi, Junjie Liu et al.
3 citations
ACS Catalysis
Catalysts for Methane Reforming
1.17
article

Mechanistic Insights into Synergistic Enhancement of Linear α-Olefins Selectivity over Ca–Na Modified Fe5C2–ZnO Catalysts in CO Hydrogenation

Qiwen Sun, Hengxuan Zhang, Zixing Shi, Junjie Liu, Jiancheng Wang, Yan Sun
article en
3 citations

Abstract

Selective synthesis of long-chain linear α-olefins (LAOs) from syngas remains a fundamental challenge due to competitive hydrogenation and water–gas shift (WGS) reactions. Herein, we report that CaO- and Na2O-promoted Fe5C2–ZnO catalyst (FeZnCaNa) demonstrates prominent performance and stability in CO hydrogenation to LAOs, which achieved 97.4% of CO conversion, 73.7% of LAOs in C4+ olefins with LAOs space-time yield of 304.4 mg·gcat–1·h–1 at 320 °C, 2.0 MPa. Comparative studies of modification with other alkaline earth metals (Mg, Sr, and Ba) underscored the unique promotional role of Ca in enhancing LAOs yield. The characterizations revealed that CaO accelerated the transformation of ZnFe2O4 into dispersed χ-Fe5C2 domains anchored at the ZnO interface. These iron carbide domains served as the principal active sites for the CO dissociation and C–C coupling. The Ca–Na–ZnO matrix modulated surface basicity, facilitating olefin desorption, and suppressing secondary hydrogenation. The ratio of olefin/paraffin attained 4.5, 58.6% of α-olefins in hydrocarbons, and suppressed CH4 selectivity to 8.1%. In situ spectroscopic analyses further explained that CaO–Na2O incorporation promoted CHx formation, thereby accelerating chain propagation. The catalyst also exhibited a reduced CO2 selectivity of 30.5%, attributed to the attenuated WGS activity resulting from decreased H2O adsorption during hydrocarbon formation. This study uncovers a dual-site mechanism, offering insights for designing efficient Fe-based catalysts for viable syngas-to-olefins conversion.

ACS CatalysisVol. 15(19)
Ocean Energy (Norway) (NO), Taiyuan University of Technology (CN)
Openalex Percentile: Top 21%
Catalysts for Methane Reforming
1.17
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