Publication | Open Access
Efficient conversion of syngas to linear α-olefins by phase-pure χ-Fe5C2
74
Citations
35
References
2024
Year
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.
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