Direct production of olefins from syngas with ultrahigh carbon efficiency
![Catalytic performance for direct syngas conversion to olefins. a Comparison of catalytic performance among Na-Ru/SiO2 and other previously reported catalysts. (a: C2–4= selectivity). b Detailed product distribution (including CO2) and ASF distribution of hydrocarbons over Na-Ru/SiO2 catalyst. c Product selectivity, CO conversion and olefins yield at different H2/CO ratios in syngas over Na-Ru/SiO2 catalyst at 533 K, 3000 mL·gcat.−1·h−1, and 1.0 MPa. d Product selectivity, CO conversion and olefins yield at different space velocities over Na-Ru/SiO2 catalyst at 533 K, H2/CO ratio of 2 and 1.0 MPa. e Stability test for Na-2%Ru(P)/SiO2 catalyst. f Reaction rate of CO and product selectivity at different Na/Ru molar ratios. Reaction conditions: 533 K, 1.0 MPa, 3000 mL·gcat.−1·h−1, H2/CO ratio of 2. Credit: Nature Communications (2022). DOI: 10.1038/s41467-022-33715-w Direct production of olefins from syngas with ultrahigh carbon efficiency](https://scx1.b-cdn.net/csz/news/800a/2022/direct-production-of-o.jpg)
Olefins are key building blocks to manufacture a wide range of value-added products such as polymers, lubricants, plasticizers, drugs, detergent and cosmetics.
Syngas conversion serves as a competitive strategy to produce olefins from nonpetroleum resources. However, the goal to achieve desirable olefins selectivity with limited undesired C1 by-products remains challenging.
Recently, a research team led by Prof. Zhong Liangshu from the Shanghai Advanced Research Institute (SARI) of the Chinese Academy of Sciences has reported a non-classical Fischer-Tropsch to olefins (FTO) process, which can realize 80.1% olefins selectivity with ultralow total selectivity of CH4 and CO2 (<5%) at CO conversion of 45.8%.
The results were published in Nature Communications on Oct. 10.
The researchers prepared a silica-supported Ru nanoparticles catalyst with sodium (Na) as promoter (denoted as Na-Ru/SiO2), which was highly active for FTO reaction but very inactive for water-gas-shift (WGS) reaction.
They further found that the Ru metal was the active phase, and the Na promoter could suppress the reactivity of chemisorbed H atoms on Ru surface sites while greatly promote the production of olefins, especially for long-chain α-olefins, whose fraction in olefins distribution reached up to 74.5%.
No obvious deactivation was observed within 550 hours and the pellet catalyst also exhibited excellent catalytic performance in a pilot-scale reactor, suggesting promising practical applications.
The results of this work demonstrate that the modified-metallic Ru can effectively tune the dominated product distribution from traditional paraffins to value-added olefins. The as-obtained catalytic performance exhibits the highest olefins (especially for long-chain α-olefins) selectivity and yield together with the lowest fraction of undesired C1 by-products including CH4 and CO2, which outperforms the reported results under all the CO conversion levels in previous references.
More information: Hailing Yu et al, Direct production of olefins from syngas with ultrahigh carbon efficiency, Nature Communications (2022). DOI: 10.1038/s41467-022-33715-w
Journal information: Nature Communications
Provided by Chinese Academy of Sciences