Efficient conversion of syngas to linear α-olefins by phase-pure χ-Fe5C2

Oil has long been the dominant feedstock for producing fuels and chemicals, but coal, natural gas and biomass are increasingly explored alternatives<sup>1-3</sup>. Their conversion first generates syngas, a mixture of CO and H<sub>2</sub>, which is then processed further using Fischer-Tropsch (FT) chemistry. However, although commercial FT technology for fuel production is established, using it to access valuable chemicals remains challenging. A case in point is linear α-olefins (LAOs), which are important chemical intermediates obtained by ethylene oligomerization at present<sup>4-8</sup>. The commercial high-temperature FT process and the FT-to-olefin process under development at present both convert syngas directly to LAOs, but also generate much CO<sub>2</sub> waste that leads to a low carbon utilization efficiency<sup>9-14</sup>. The efficiency is further compromised by substantially fewer of the converted carbon atoms ending up as valuable C<sub>5</sub>-C<sub>10</sub> LAOs than are found in the C<sub>2</sub>-C<sub>4</sub> olefins that dominate the product mixtures<sup>9-14</sup>. Here we show that the use of the original phase-pure χ-iron carbide can minimize these syngas conversion problems: tailored and optimized for the process of FT to LAOs, this catalyst exhibits an activity at 290 °C that is 1-2 orders higher than dedicated FT-to-olefin catalysts can achieve above 320 °C (refs. <sup>12-15</sup>), is stable for 200 h, and produces desired C<sub>2</sub>-C<sub>10</sub> LAOs and unwanted CO<sub>2</sub> with carbon-based selectivities of 51% and 9% under industrially relevant conditions. This higher catalytic performance, persisting over a wide temperature range (250-320 °C), demonstrates the potential of the system for developing a practically relevant technology.

Authors

Institutions

Publication Details

Journal
Nature
Published
2024-10-16
DOI
https://doi.org/10.1038/s41586-024-08078-5
Citations
81
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
8.66

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Efficient conversion of syngas to linear α-olefins by phase-pure χ-Fe5C2

Robin J. P. Broos, Yijun Lv, Ivo A. W. Filot, Fu‐Kuo Chiang et al.
81 citations
Nature
Catalysts for Methane Reforming
8.66
article

Efficient conversion of syngas to linear α-olefins by phase-pure χ-Fe5C2

Robin J. P. Broos, Yijun Lv, Ivo A. W. Filot, Fu‐Kuo Chiang, Jiachun Chai, A. Iulian Dugulan, Bo Feng, Rongming Wang, Emiel J. M. Hensen, Zhuowu Men, Wei Chen, Peng Wang, Yuanjun Song, Quan Lin, Juan Dong
article en
81 citations

Abstract

Oil has long been the dominant feedstock for producing fuels and chemicals, but coal, natural gas and biomass are increasingly explored alternatives<sup>1-3</sup>. Their conversion first generates syngas, a mixture of CO and H<sub>2</sub>, which is then processed further using Fischer-Tropsch (FT) chemistry. However, although commercial FT technology for fuel production is established, using it to access valuable chemicals remains challenging. A case in point is linear α-olefins (LAOs), which are important chemical intermediates obtained by ethylene oligomerization at present<sup>4-8</sup>. The commercial high-temperature FT process and the FT-to-olefin process under development at present both convert syngas directly to LAOs, but also generate much CO<sub>2</sub> waste that leads to a low carbon utilization efficiency<sup>9-14</sup>. The efficiency is further compromised by substantially fewer of the converted carbon atoms ending up as valuable C<sub>5</sub>-C<sub>10</sub> LAOs than are found in the C<sub>2</sub>-C<sub>4</sub> olefins that dominate the product mixtures<sup>9-14</sup>. Here we show that the use of the original phase-pure χ-iron carbide can minimize these syngas conversion problems: tailored and optimized for the process of FT to LAOs, this catalyst exhibits an activity at 290 °C that is 1-2 orders higher than dedicated FT-to-olefin catalysts can achieve above 320 °C (refs. <sup>12-15</sup>), is stable for 200 h, and produces desired C<sub>2</sub>-C<sub>10</sub> LAOs and unwanted CO<sub>2</sub> with carbon-based selectivities of 51% and 9% under industrially relevant conditions. This higher catalytic performance, persisting over a wide temperature range (250-320 °C), demonstrates the potential of the system for developing a practically relevant technology.

NatureVol. 635(8037)
National Institute of Clean and Low-Carbon Energy (CN), Tianjin Energy Investment Group (China) (CN), CHN Energy (China), Eindhoven University of Technology (NL), University of Science and Technology Beijing (CN), Delft University of Technology (NL)
National Natural Science Foundation of China, Nederlandse Organisatie voor Wetenschappelijk Onderzoek, National Institute of Clean-and-Low-Carbon Energy, National Key Research and Development Program of China
Openalex Percentile: Top 1%
Catalysts for Methane Reforming
8.66
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.