Effects of composition and morphology of active phase of CoMo/Al2O3 catalysts prepared using Co2Mo10–heteropolyacid and chelating agents on their catalytic properties in HDS and HYD reactions

[Display omitted] •CoMo catalysts were synthesised using heteropolyacid and chelating agents simultaneously.•Type of chelating agent significantly affects the structure of the active phase and catalytic properties.•TOF and HDS/HYD selectivity depend on the number and location of the CoMoS sites and...

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Veröffentlicht in:Journal of catalysis 2014-04, Vol.312, p.152-169
Hauptverfasser: Nikulshin, P.A., Ishutenko, D.I., Mozhaev, A.A., Maslakov, K.I., Pimerzin, A.A.
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Sprache:eng
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Zusammenfassung:[Display omitted] •CoMo catalysts were synthesised using heteropolyacid and chelating agents simultaneously.•Type of chelating agent significantly affects the structure of the active phase and catalytic properties.•TOF and HDS/HYD selectivity depend on the number and location of the CoMoS sites and the shape of the CoMoS2 crystallites.•Highly efficient catalysts in HDS of DBT and 4,6-DMDBT and diesel HDT.•Highly efficient catalysts in selective HDT of a model FCC gasoline. CoMo/Al2O3 catalysts were synthesised from the ammonium and Co salts of [CoMo6O24H6]3− and [Co2Mo10O38H4]6− anions as well as Co–chelate complexes with nitrilotriacetic, ethylenediaminetetraacetic, citric and tartaric acids. The catalysts were characterised using X-ray powder diffraction, Raman spectroscopy, N2 physisorption, high-resolution transmission electron microscopy and X-ray photoelectron spectroscopy. The catalysts were tested in the hydrotreating (HDT) of a mixture containing thiophene and n-hexene-1, the hydrodesulphurisation (HDS) of dibenzothiophene and 4,6-dimethyldibenzothiophene and the HDT of diesel. The type of chelating agent significantly affects the structure of the active phase and catalytic properties. The catalytic activity, selectivity and turnover frequency during the HDS and hydrogenation reactions depend on the number and location of CoMoS sites, as well as the shape of the active phase crystallites. New “structure–activity” relationships were established. These approaches yielded catalysts that demonstrated high efficiency towards the deep diesel HDT and selective HDS of a model fluid catalytic cracking gasoline.
ISSN:0021-9517
1090-2694
DOI:10.1016/j.jcat.2014.01.014