Fischer–Tropsch synthesis of olefin-rich liquid hydrocarbons from biomass-derived syngas over carbon-encapsulated iron carbide/iron nanoparticles catalyst

•Direct conversion of biosyngas to olefin-rich liquid hydrocarbons was reported.•Carbon-encapsulated iron carbide/iron catalyst showed high selectivity to olefins.•The formation mechanism of carbon-encapsulated iron carbide/iron was proposed.•The iron carbide/iron core of catalyst consisted of α-Fe,...

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Veröffentlicht in:Fuel (Guildford) 2017-04, Vol.193 (C), p.369-384
Hauptverfasser: Lu, Yongwu, Yan, Qiangu, Han, Jun, Cao, Baobao, Street, Jason, Yu, Fei
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Sprache:eng
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Zusammenfassung:•Direct conversion of biosyngas to olefin-rich liquid hydrocarbons was reported.•Carbon-encapsulated iron carbide/iron catalyst showed high selectivity to olefins.•The formation mechanism of carbon-encapsulated iron carbide/iron was proposed.•The iron carbide/iron core of catalyst consisted of α-Fe, θ-Fe3C, and Fe15.1C. Olefins are extensively used in the chemical industry as building blocks for manufacturing a wide range of products such as polymers, drugs, cosmetics, solvents, and detergents. Traditionally, olefins have been produced from thermal or catalytic cracking of petroleum-derived hydrocarbons, but environmental and economic concerns are urging exploration of alternative routes for their production from renewable sources. Herein, we report the synthesis of olefin-rich liquid hydrocarbons from biomass-derived syngas (biosyngas) via Fischer–Tropsch reaction by using carbon-encapsulated iron carbide/iron nanoparticles (CEICINs) catalysts. The CEICINs core-shell nanostructured catalysts typically constituted iron carbide/iron-core diameters of 6–30nm and graphite-shell thickness of 2–5nm, where the iron carbide/iron-core consisted of α-Fe, θ-Fe3C and Fe15.1C. The catalytic performance over CEICINs at mild reaction conditions (310°C, 1000psig, 3000h−1) showed that CO and H2 conversion was ∼87.5% and 85%, respectively. The C5+ liquid hydrocarbon selectivity was ∼65%, ∼44.8% of which was olefins. The liquid product formation rate was 0.12g/(gcat h) during the time-on-stream of 100h after achieving steady state. The volume percent of the oil phase in the liquid product was ∼60%. The higher reaction temperature led to the higher selectivity towards olefins, while the effect of biosyngas pressure was not a significant factor concerning olefin selectivity. Gas hourly space velocity (GHSV) had a negative effect on the formation of olefins due to the short-time contact of the reactant gas with the CEICINs catalyst. This work demonstrated the technical feasibility of the direct synthesis of olefin-rich liquid hydrocarbons by utilizing CEICINs catalysts from biosyngas via biomass gasification, biosyngas cleaning, and Fischer–Tropsch synthesis technology.
ISSN:0016-2361
1873-7153
DOI:10.1016/j.fuel.2016.12.061