Hydrodesulfurization of 4,6-dimethyldibenzothiophene over high surface area metal phosphides

High surface area MoP (139 m 2/g), Ni 2P (216 m 2/g) and a series of Ni x MoP (121–16 m 2/g) catalysts were synthesized by adding citric acid (CA) to precursor salt solutions prior to drying, calcination and reduction. Their HDS TOFs decreased in the order Ni 2P > Ni x MoP > MoP and for the Ni x MoP catalysts, the observed TOF increased with Ni content. Unsupported monometallic phosphides (MoP and Ni 2P), as well as a series of bimetallic nickel molybdenum phosphides (Ni x MoP), were synthesized with high surface area by adding citric acid (CA) to precursor metal salt solutions prior to drying, calcination and temperature-programmed reduction (TPR). The resulting MoP and Ni 2P catalysts had surface areas of 139 and 216 m 2/g, respectively. The surface areas of the Ni x MoP catalysts decreased with increased Ni content and ranged from 121 to 16 m 2/g. In all cases, the catalyst surface area was greater than that obtained when a conventional preparation procedure was followed that did not use CA. The activity of the catalysts for the hydrodesulfurization (HDS) of a feed containing 3000 ppm 4,6-dimethyldibenzothiophene (4,6-DMDBT) in toluene was measured at 583 K and 3.0 MPa. The resulting catalysts were highly active and among the studied phosphides, Ni 2P exhibited the highest HDS activity with a conversion of 87.7% at a WHSV of 26 h −1 and a H 2/liquid feed ratio of 625 (v/v). The HDS TOF decreased in the order Ni 2P > Ni x MoP > MoP and for the Ni x MoP catalyst, the observed TOF increased with Ni content.