Syngas-conversion to methane and C
2∼C
4 hydrocarbons on composite catalysts has heen investigated by continuous flow method under 10∼21atm. Ni-La
2O
3-Ru catalyst (1) exhibited higher activity in methane formation and lower activity in C
2∼C
4 hydrocarbons under 10 atm than those under 1 atm. Fe-La
2O
3-Ru catalyst (2) has high activity in C
2∼C
4 hydrocarbons under medium pressure (10.5atm), however, under high pressure (20.6atm) formation of C
5+ hydrocarbons added, On the other hand, Co-La
2O
3-Ru catalyst (3) exerted best performance among the three catalysts for C
1∼C
4 hydrocarbon synthesis, for instance, space-time yield (
STY
) for methane of 75.7mol/1l·h and
STY
for C
2∼C
4 hydrocarbons of 6.9mol/1·h at 45.7% CO conversion were obtained at the reaction conditions of H
2/CO molar ratio of 2, SV of 11400 h
-1, 10 atm, and 356°C. It is shown that the catalyst prepared by impregnation method using the silica support having meso (5nm)-macro (600nm) bimodal pore structure has a better performance compared with catalysts prepared by another methods.
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