The structure of sulfided Mo-catalysts and their oxidic precursors has been abundantly studied, but the genesis of the active phase has remained much less investigated. The sulfidation (in H2S/H2 atmosphere) of a series of MoO3/SiO2 catalysts has been examined by means of temperature-programmed sulfidation, X-ray absorption fine structure, and transmission electron microscopy.The oxidic, oligomeric clusters in a 5.6 wt 5% MoO3/Si02 catalyst are transformed into partly sulfided particles (MOOS,,) by 0-S exchange at room temperature. A molybdenum sulfide species the structure of which resembles the MoS, structure is formed during sulfidation at 423 K. The MoS2 phase is formed at temperatures between 523 and 573 K, depending on the dispersion of the initial Moo3 phase. The transition of MoS3 into MoS2 can be monitored by the evolution of H2S from the catalyst with a simultaneous consumption of H2. The two-dimensional size of the MoS2 slabs can be derived from the EXAFS Mo-Mo coordination number by means of a theoretical model. TEM is required to elucidate the stacking height of the slabs. The application of supported molybdena-based catalysts in industrial processes, such as partial oxidation’-5 and hydrotreating,+lB has rendered supported molybdenum oxide catalysts a main subject of investigations. Many studies are dedicated to the preparation and the structure of Moo3 catalysts on different supports. The sulfded counterpart of the oxidic precursors of Co(Ni)/Mo(W) catalysts is one of the most thoroughly investigated catalyst systems. Conversion of the oxidic catalyst into the active sulfide occurs under reaction conditions, due to presulfiding or the presence of sulfur-containing feedstocks. It is industrial practice to “spike” the feedstock with agents, such as CS2, dimethyl sulfide (DMS), or dimethyl disulfide (DMDS), to accelerate the sulfidation of the catalyst.I9-20 As an alternative, thecatalyst can besulfided exsitu by impregnation with a sulfurcontaining liquid. In situ heating of the catalyst subsequently leads to sulfidation.2’ In most of the laboratory tests the catalyst is sulfided by a mixture of H2S/H2 at high temperat~re~~v~~ or in a temperature program. A number of models have been proposed to explain the activity of the Co(Ni)/Mo(W) catalysts. Consensus exists on the structure of the molybdenum sulfide phase: under typical hydrotreating conditions (i.e., p = 10-200 bar, T = 573-723 K, excess H2, and a sulfur-rich feedstock”) MoS2 is present, in which molybdenum is trigonal prismatically coordinated by sulfur However, the position and the role of the cobalt atoms in the catalysts are still debated. The earlier proposed models are based on the assumptionof a monolayer,34~ontactsynergy,’~J~ inter~alation,3S33~ and remote control.37 The most popular model is based on publications by Topsoe et al.30 and by Wive1 et a1.38 The latter reported a linear relationship between the activity in thiophene HDS and the concentration of Co present in the “Co-Mo-S” species. This phase had been designated as ‘COMOS”~~ because its Mbssbauer spectrum did not resemble any of the known cobalt sulfide or cobalt molybdenum sulfide spectra. The CoMoS species is envisioned as a MoS2 layer (slab), with cobalt atoms decorating the edges.30J9 Since the introduction of this model, some
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