AI Article Synopsis

  • Oil has been a primary source for fuels and chemicals, but alternatives like coal, natural gas, and biomass are being explored, with syngas (a mix of CO and H) produced for further processing.
  • The Fischer-Tropsch (FT) chemistry is used to convert syngas into fuels and chemicals, but current methods face challenges in efficiently producing valuable chemicals like linear α-olefins (LAOs) and generate excess CO waste.
  • Research shows that using phase-pure χ-iron carbide as a catalyst can significantly improve the syngas conversion efficiency and stability, leading to higher yields of desirable LAOs while reducing CO waste under industrial conditions.

Article 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 H, 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 CO 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 C-C LAOs than are found in the C-C 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 (refs. ), is stable for 200 h, and produces desired C-C LAOs and unwanted CO 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.

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Source
http://www.ncbi.nlm.nih.gov/pmc/articles/PMC11541216PMC
http://dx.doi.org/10.1038/s41586-024-08078-5DOI Listing

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