Application of Heteropolyacid H4SiMo3W9O40 for the Preparation of Bimetallic MoWS2/Al2O3 Hydrotreatment Catalysts
- Authors: Nikul’shina M.S.1,2, Mozhaev A.V.1, Minaev P.P.1, Fournier M.2, Lancelot C.2, Blanchard P.2, Payen E.2, Lamonier C.2, Nikul’shin P.A.1
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Affiliations:
- Samara State Technical University
- Unité de Catalyse et de Chimie du Solide
- Issue: Vol 58, No 6 (2017)
- Pages: 825-832
- Section: Article
- URL: https://journals.rcsi.science/0023-1584/article/view/163473
- DOI: https://doi.org/10.1134/S0023158417060088
- ID: 163473
Cite item
Abstract
The bimetallic MoWS2/Al2O3 catalyst was synthesized using the Keggin-type mixed heteropolyacid H4SiMo3W9O40. The monometallic catalysts SiMo12/Al2O3 and SiW12/Al2O3 based on the H4SiMo12O40 and H4SiW12O40 acids are prepared as reference samples. The sulfidized catalysts are analyzed by temperature-programmed reduction with hydrogen, high-resolution transmission electron microscopy, and X-ray photoelectron spectroscopy. Their catalytic properties are studied in the cohydrotreatment of dibenzothiophene (DBT) and naphthalene on a flow-type setup. The introduction of three molybdenum atoms into the structure of an oxide precursor is shown to increase the degree of sulfidation of the tungsten particles by 20% in comparison with SiW12/Al2O3. The DBT turnover frequency in the hydrodesulfurization (HDS) on the sites on the edges of the active phase of the SiMo3W9/Al2O3 catalyst is shown to be 5.5 times higher than in the presence of SiW12/Al2O3. The bimetallic sample demonstrated the highest selectivity in the preliminary DBT hydrogenation route and activity in the prehydrogenation of naphthalene. The high level of activity of the SiMo3W9/Al2O3 catalyst was due to the formation of a mixed MoxW(1–x)S2 active phase with a MoW oxide precursor, whose structure contained both metals bonded at the molecular level.
About the authors
M. S. Nikul’shina
Samara State Technical University; Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
Russian Federation, Samara, 443100; Villeneuve d’Ascq, CEDEX F-59655
A. V. Mozhaev
Samara State Technical University
Email: p.a.nikulshin@gmail.com
Russian Federation, Samara, 443100
P. P. Minaev
Samara State Technical University
Email: p.a.nikulshin@gmail.com
Russian Federation, Samara, 443100
M. Fournier
Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
France, Villeneuve d’Ascq, CEDEX F-59655
C. Lancelot
Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
France, Villeneuve d’Ascq, CEDEX F-59655
P. Blanchard
Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
France, Villeneuve d’Ascq, CEDEX F-59655
E. Payen
Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
France, Villeneuve d’Ascq, CEDEX F-59655
C. Lamonier
Unité de Catalyse et de Chimie du Solide
Email: p.a.nikulshin@gmail.com
France, Villeneuve d’Ascq, CEDEX F-59655
P. A. Nikul’shin
Samara State Technical University
Author for correspondence.
Email: p.a.nikulshin@gmail.com
Russian Federation, Samara, 443100
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