A gas-expanded-liquid technique (GXL) was applied to the preparation of supported iron catalysts for Fischer− Tropsch synthesis (FTS). A mixture of presynthesized iron oxide nanoparticles with an average size of 12 nm was deposited onto a SiO 2 support in a manner such that nanoparticles smaller than 5 nm were excluded from the final catalyst product. A series of SiO 2 -supported iron oxide nanoparticle catalysts were prepared with iron loadings of 11.4, 18.0, 24.0, and 28.8 wt %. Catalysts were characterized by nitrogen adsorption, inductively coupled plasma optical emission spectrometry, H 2 temperatureprogrammed reduction (H 2 -TPR), X-ray diffraction (XRD), trasmission electron microsopy (TEM), X-ray photoelectron spectroscopy, and carbon monoxide temperature-programmed desorption. TEM analysis showed that iron oxide nanoparticles were well-distributed over the surface of the SiO 2 support with an increase in the iron loading resulting in the formation of multilayers and three-dimensional islands of iron oxide nanoparticles. H 2 -TPR indicated that the reducibility of the iron oxide nanoparticles increased monotonically with iron loading. According to XRD results, the increase in the iron loading resulted in an increase in the iron oxide crystallite size, and iron carbides were present in the used catalysts after solvent treatment. FTS was carried out in a fixed-bed reactor at reaction conditions of 230 °C, 2 MPa, H 2 /CO = 1.70, and GHSV = 3000 L/kg cat /h. For the catalysts studied, the highest syngas conversion and iron time yield were observed at intermediate (18, 24 wt %) iron loadings. The C 5+ selectivity and carbon chain growth probability factor were approximately 68% and 0.76, respectively, for each catalyst. A 16 wt % iron on SiO 2 catalyst prepared by the same GXL technique was promoted with 0.7 wt % potassium using the incipient wetness method. As expected, K promotion resulted in a slight decrease in FTS activity and increased selectivity toward CO 2 and C 5+ selectivity.