摘要
Selective conversion of syngas to olefins has aroused extensive attention while some challenges still existed such as high CO 2 selectivity. Herein, a series of hydrophobic FeMnO x @SiO 2 -y-(CH 3 ) 3 (y represents SiO 2 weight percent of the catalyst) catalysts with various SiO 2 shell content were synthesized for Fischer-Tropsch to olefins (FTO). During the activation process, high hydrophobic SiO 2 -coating content catalysts suppressed the reduction/carburization of iron species to iron carbide. During FTO reaction, iron carbide of low hydrophobic SiO 2 -coating content catalysts was re-oxidized while it was stabilized for high hydrophobic SiO 2 -coating content catalysts. The trade-off among CO 2 , CH 4 selectivity and SiO 2 -coating content was reflected as an increasing trend relationship, while olefins selectivity exhibited a decreasing trend. Additionally, a desirable hydrophobic SiO 2 -coating (8.2 wt%) catalyst apparently suppressed CO 2 formation (4.7 C%) with high olefins selectivity (54.6 C%) at CO conversion of 50.7%. This study provides an efficient approach to inhibit CO 2 formation of Fe-based FTO catalyst.
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