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

Journal Article (2024)
Author(s)

Peng Wang (CHN Energy, Eindhoven University of Technology)

Fu Kuo Chiang (CHN Energy)

Jiachun Chai (Eindhoven University of Technology, CHN Energy)

A. Iulian Dugulan (TU Delft - RST/Fundamental Aspects of Materials and Energy, TU Delft - RID/TS/Instrumenten groep)

Juan Dong (CHN Energy)

Wei Chen (Eindhoven University of Technology)

Robin J.P. Broos (Eindhoven University of Technology)

Zhuowu Men (CHN Energy)

Emiel J.M. Hensen (Eindhoven University of Technology)

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DOI related publication
https://doi.org/10.1038/s41586-024-08078-5 Final published version
More Info
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Publication Year
2024
Language
English
Issue number
8037
Volume number
635
Pages (from-to)
102-107
Downloads counter
315
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Abstract

Oil has long been the dominant feedstock for producing fuels and chemicals, but coal, natural gas and biomass are increasingly explored alternatives. Their conversion first generates syngas, a mixture of CO and H2, 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. 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 CO2 waste that leads to a low carbon utilization efficiency. The efficiency is further compromised by substantially fewer of the converted carbon atoms ending up as valuable C5–C10 LAOs than are found in the C2–C4 olefins that dominate the product mixtures. 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, is stable for 200 h, and produces desired C2–C10 LAOs and unwanted CO2 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.