The conversion of quinoline over ReS 2 supported on g-Al 2 O 3 , SiO 2 , ZrO 2 and TiO 2 catalysts in a batch reactor at 300•C and 5 MPa of hydrogen pressure was studied. The catalysts were prepared by wet impregnation with a loading of 1.5 atoms of Re per nm 2 of support. The catalysts were characterized by N 2 adsorption, X-ray photoelectron spectroscopy (XPS) and X-ray powder diffraction (XRD). The Re(x)/supports catalysts displayed high activities for the conversion of quinoline, although negligible formation of N-free compounds (hydrodenitrogenation) were observed. The intrinsic activities of ReS 2 were modified by the support decreased in the order: Re/TiO 2 > Re/ZrO 2 > Re/SiO 2 > Re/g-Al 2 O 3 . The highest activity displayed by the Re/TiO 2 catalyst was correlated with the Re dispersion and formation of ReS 2 species. Meanwhile, the lower conversion of quinoline over the Re/ZrO 2 , Re/SiO 2 and Re/g-Al 2 O 3 catalysts was related to the combined effect of the textural properties of catalysts and the formation of ReS (2-x) species on the supports.