Abstract

The direct production of gasoline-range isoparaffins from synthesis gas (CO + H2, syngas) via the Fischer−Tropsch (FT) route was investigated over a hybrid catalyst composed of Co/SiO2 and Pd/β under the conditions of P = 1.0 MPa, W/F = 7.9 g·h·mol-1 and reaction temperatures of 503−513 K. Results indicate that the contact state between the Co/SiO2 and the Pd/β particles in the hybrid catalyst (powdery mixture and granular mixture) had a clear effect on both the activity toward CO hydrogenation and the product distribution. Interestingly, the granular hybrid catalyst showed much higher performance in the case of isoparaffin selectivity than the powdery hybrid catalyst at the initial stage of the reaction. Furthermore, irrespective of the reaction conditions applied, the powdery hybrid catalyst gave apparently lower CO conversion and obviously higher CH4 selectivity than the granular hybrid catalyst. Irrespective of the catalyst used, the total selectivity of isoparaffins (I/C4+) noticeably decreased with ...

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