کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
6474966 1424971 2017 16 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Fischer–Tropsch synthesis of olefin-rich liquid hydrocarbons from biomass-derived syngas over carbon-encapsulated iron carbide/iron nanoparticles catalyst
ترجمه فارسی عنوان
سنتز فیوچر تروپچ از هیدروکربن های مایع غنی از الفین از سیگنز گاز مشتق شده از زیست توده در مقایسه با کربن بسته بندی شده کاربید آهن / آهن نانوذرات کاتالیزور
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• 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 6–30 nm and graphite-shell thickness of 2–5 nm, 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, 1000 psig, 3000 h−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 0.12 g/(gcat h) during the time-on-stream of 100 h 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.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel - Volume 193, 1 April 2017, Pages 369–384