Synthesis of carbon nanofibers supported cobalt catalysts for Fischer–Tropsch process
•Support crystallinity clearly influenced on the metal particle size.•Co/CNF-1 and Co/CNF-2 showed the highest activity and selectivity to CO2 and CH4.•Co/CNF-3 sample presented the highest selectivity to long-chained hydrocarbons.•Metal sintering was significant in catalysts with small metal partic...
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Veröffentlicht in: | Fuel (Guildford) 2013-09, Vol.111, p.422-429 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | •Support crystallinity clearly influenced on the metal particle size.•Co/CNF-1 and Co/CNF-2 showed the highest activity and selectivity to CO2 and CH4.•Co/CNF-3 sample presented the highest selectivity to long-chained hydrocarbons.•Metal sintering was significant in catalysts with small metal particles.•Catalyst fouling by long-chained hydrocarbons slow down the reaction.
In this paper, CNFs prepared at three different temperatures (1023, 873 and 723K, called CNF-1, CNF-2 and CNF-3, respectively) were used as supports for cobalt-based catalysts in the Fischer–Tropsch Synthesis (FTS). The supports and cobalt catalysts were characterized by nitrogen adsorption–desorption, temperature-programmed reduction (TPR), X-ray diffraction (XRD) and thermogravimetric analysis (TGA) techniques; the metal content of the cobalt-based catalysts was analyzed by atomic absorption. The activity and selectivity of the CNFs supported catalysts were studied at 523K, 20bar and H2/CO=2. Co/CNF-1 and Co/CNF-2 were very active and showed high selectivity to CH4 and CO2, without further deactivation, whereas the less active catalyst Co/CNF-3 led to the highest selectivity to long-chained hydrocarbons (C5+) and under was a remarkable deactivation. Used catalysts were characterized by nitrogen adsorption–desorption, XRD and TGA. Results confirmed that all the catalysts underwent catalyst fouling as a consequence of C5+ hydrocarbons formation whereas catalyst Co/CNF-3 presented a notably metal sintering by coalescence. |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2013.04.003 |