Boosting Selectivity toward Long-Chain α-Olefins in CO <sub>2</sub> Hydrogenation through Strengthening ZnO–Fe Interactions with Favorable Iron Phase Regulation for Fischer–Tropsch Synthesis

Developing excellent catalysts for CO<sub>2</sub> hydrogenation to long-chain linear α-olefins (LAOs) offers a promising route toward value-added chemicals. However, it remains a considerable challenge to achieve high CO<sub>2</sub> conversion along with superior selectivity to LAOs. In this study, we prepared a series of Zn-modified iron-based catalysts using urea precipitation for the CO<sub>2</sub> hydrogenation reaction, and they exhibited a much higher selectivity to C<sub>4+</sub> LAOs of 61.7%, with a CO<sub>2</sub> conversion of 38.5%, over Fe2Zn1-U catalyst, compared to the selectivity of 50.5% over Fe2Zn1-A catalyst with same elemental composition prepared using ammonia precipitation. A lower selectivity to methane was obtained, from 13.7% to 8.8%. Moreover, this process resulted in a record-breaking space-time yield (STY) of 0.544 g<sub>C4+LAOs</sub>·g<sub>cat</sub> <sup>-1</sup>·h<sup>-1</sup>. HRTEM characterization over spent catalysts showed that Fe2Zn1-U exhibited smaller-size mixed iron-phase particles (Fe<sub>3</sub>O<sub>4</sub>, χ-Fe<sub>5</sub>C<sub>2</sub>, and θ-Fe<sub>3</sub>C) where the ZnO phase was more homogeneously dispersed and had stronger interactions with Fe species compared to the observations for Fe2Zn1-A. In situ XPS analysis suggested that this structure promoted Zn-to-Fe electron donation along with intimate interaction over Fe2Zn1-U. XANES spectra demonstrated a more difficult reduction of Fe species with weaker Fe-C coordination for carburization, thereby resulting in a higher Fe<sub>3</sub>O<sub>4</sub> content in spent Fe2Zn1-U. In situ IR spectroscopy under reaction conditions confirmed that significantly more surface species of CO*, HCOO<sup>-</sup>, *HCO, *CH <sub><i>x</i></sub> , and *CCH were present over the Fe2Zn1-U catalyst, derived from strengthened synergistic catalysis between ZnO, Fe<sub>3</sub>O<sub>4</sub>, and iron carbides. Also, Mössbauer spectroscopy analysis revealed that more θ-Fe<sub>3</sub>C phase was observed over spent Fe2Zn1-U, which was beneficial for carbon-carbon coupling, owing to its wavy protrusion structure, demonstrated by DFT calculations to be like *C<sub>5</sub>H<sub>10</sub> and *C<sub>6</sub>H<sub>12</sub> coupling with *CH<sub>2</sub> species, showing a much lower energy barrier to form longer α-olefins. In addition, it was found that the introduction of Cu could enhance the CO<sub>2</sub> conversion, selectivity to LAOs, and catalyst stability. As a result, the Fe3Zn1-U-12Cu catalyst gave stable production of LAOs with a high selectivity from CO<sub>2</sub> hydrogenation over 400 h reaction time on stream.

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Journal
JACS Au
Published
2026-03-03
DOI
https://doi.org/10.1021/jacsau.5c01605
Primary Topic
Catalysts for Methane Reforming
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article
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article

Boosting Selectivity toward Long-Chain α-Olefins in CO 2 Hydrogenation through Strengthening ZnO–Fe Interactions with Favorable Iron Phase Regulation for Fischer–Tropsch Synthesis

Zhangshi Li, Huan He, X. L. Liu, Yong Li et al.
JACS Au
Catalysts for Methane Reforming
article

Boosting Selectivity toward Long-Chain α-Olefins in CO 2 Hydrogenation through Strengthening ZnO–Fe Interactions with Favorable Iron Phase Regulation for Fischer–Tropsch Synthesis

Zhangshi Li, Huan He, X. L. Liu, Yong Li, Changxu Wang, Jiayi Liu, Zhaobo Fan, Dezheng Li, Qiang Li, Siyang Yan, Guanze Nie, Bing Liu
article en

Abstract

Developing excellent catalysts for CO<sub>2</sub> hydrogenation to long-chain linear α-olefins (LAOs) offers a promising route toward value-added chemicals. However, it remains a considerable challenge to achieve high CO<sub>2</sub> conversion along with superior selectivity to LAOs. In this study, we prepared a series of Zn-modified iron-based catalysts using urea precipitation for the CO<sub>2</sub> hydrogenation reaction, and they exhibited a much higher selectivity to C<sub>4+</sub> LAOs of 61.7%, with a CO<sub>2</sub> conversion of 38.5%, over Fe2Zn1-U catalyst, compared to the selectivity of 50.5% over Fe2Zn1-A catalyst with same elemental composition prepared using ammonia precipitation. A lower selectivity to methane was obtained, from 13.7% to 8.8%. Moreover, this process resulted in a record-breaking space-time yield (STY) of 0.544 g<sub>C4+LAOs</sub>·g<sub>cat</sub> <sup>-1</sup>·h<sup>-1</sup>. HRTEM characterization over spent catalysts showed that Fe2Zn1-U exhibited smaller-size mixed iron-phase particles (Fe<sub>3</sub>O<sub>4</sub>, χ-Fe<sub>5</sub>C<sub>2</sub>, and θ-Fe<sub>3</sub>C) where the ZnO phase was more homogeneously dispersed and had stronger interactions with Fe species compared to the observations for Fe2Zn1-A. In situ XPS analysis suggested that this structure promoted Zn-to-Fe electron donation along with intimate interaction over Fe2Zn1-U. XANES spectra demonstrated a more difficult reduction of Fe species with weaker Fe-C coordination for carburization, thereby resulting in a higher Fe<sub>3</sub>O<sub>4</sub> content in spent Fe2Zn1-U. In situ IR spectroscopy under reaction conditions confirmed that significantly more surface species of CO*, HCOO<sup>-</sup>, *HCO, *CH <sub><i>x</i></sub> , and *CCH were present over the Fe2Zn1-U catalyst, derived from strengthened synergistic catalysis between ZnO, Fe<sub>3</sub>O<sub>4</sub>, and iron carbides. Also, Mössbauer spectroscopy analysis revealed that more θ-Fe<sub>3</sub>C phase was observed over spent Fe2Zn1-U, which was beneficial for carbon-carbon coupling, owing to its wavy protrusion structure, demonstrated by DFT calculations to be like *C<sub>5</sub>H<sub>10</sub> and *C<sub>6</sub>H<sub>12</sub> coupling with *CH<sub>2</sub> species, showing a much lower energy barrier to form longer α-olefins. In addition, it was found that the introduction of Cu could enhance the CO<sub>2</sub> conversion, selectivity to LAOs, and catalyst stability. As a result, the Fe3Zn1-U-12Cu catalyst gave stable production of LAOs with a high selectivity from CO<sub>2</sub> hydrogenation over 400 h reaction time on stream.

JACS AuVol. 6(3)
Jiangnan University (CN), Dalian University of Technology (CN), Smart Material (Germany) (DE), Institute of Chemical Engineering (BG), State Key Laboratory of Fine Chemicals
Openalex Percentile: Top 37%
Catalysts for Methane Reforming
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