Role of ZrO2 and Porosity Induced by Activated Carbon and Starch Templates in NiMo/Al2O3-ZrO2 Catalysts for Naphthalene Hydrogenation and 4,6-Dimethyldibenzothiophene Hydrodesulfurization

The influence of zirconia incorporation and template type on the physicochemical properties of NiMo/Al2O3-ZrO2 catalysts was investigated for the hydrodesulfurization (HDS) of 4,6-dimethyldibenzothiophene (4,6-DMDBT) and the hydrogenation (HYD) of naphthalene (N). Catalysts were prepared by co-impregnation on supports synthesized via a sol-gel method using starch (A) and activated carbon (C) as structure-directing templates, followed by zirconium incorporation through a grafting procedure. The resulting materials were characterized by SEM–EDX, N2 physisorption, H2-TPR, XPS, HRTEM, and pyridine-FTIR. SEM-EDX confirmed homogeneous metal distributions and compositions close to nominal values (Mo = 20 wt%, Ni = 5 wt%, Zr = 11 wt%) with Ni/(Ni + Mo) = 0.30. N2 adsorption–desorption isotherms correspond to type IV(a) with H3-H4 hysteresis loops, characteristic of mesoporous structures. After metal incorporation, surface areas decreased to 96 m2 g−1 for NiMo/Al2O3 and 81 m2 g−1 for Zr-modified catalysts, while the activated carbon-templated sample preserved a larger mesoporous volume (0.335 cm3 g−1) and higher macroporosity (72%). H2-TPR profiles indicated improved reducibility for Zr-containing catalysts. XPS revealed an increase of MoS2 species from 45% in NiMo/Al2O3 to 75% in NiMo/Al2O3-ZrO2(C), accompanied by a higher degree of sulfidation index (DSI) from 47.1% to 73.9%. HRTEM analysis of Zr-modified catalysts revealed longer MoS2 slabs (11.8–12.1 nm) and higher edge-to-corner ratios (17–17.4) compared with NiMo/Al2O3 (6.2 nm; fe/fc = 8.2). Pyridine-FTIR showed a substantial increase in total acidity from 91 to 421 μmol g−1 upon Zr addition. Catalytically, NiMo/Al2O3-ZrO2(C) exhibited the highest HDS conversion (40%), reaction rate (10.5 × 10−9 mol s−1 g−1), and TOF (4.69 × 10−5 s−1), whereas NiMo/Al2O3-ZrO2(A) reached the highest naphthalene conversion (97.18%), with a reaction rate of 27.4 × 10−7 mol s−1 g−1 and TOF of 12.9 × 10−3 s−1. These results demonstrate that Zr incorporation and the activated carbon template favored hydrodesulfurization, whereas the starch template promoted hydrogenation performance.

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Journal
Inorganics
Published
2026-04-11
DOI
https://doi.org/10.3390/inorganics14040109
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
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article

Role of ZrO2 and Porosity Induced by Activated Carbon and Starch Templates in NiMo/Al2O3-ZrO2 Catalysts for Naphthalene Hydrogenation and 4,6-Dimethyldibenzothiophene Hydrodesulfurization

Carlos A.T. Toloza, Esneyder Polo, Elíseo Díaz Varela
Inorganics
Catalysis and Hydrodesulfurization Studies
article

Role of ZrO2 and Porosity Induced by Activated Carbon and Starch Templates in NiMo/Al2O3-ZrO2 Catalysts for Naphthalene Hydrogenation and 4,6-Dimethyldibenzothiophene Hydrodesulfurization

Carlos A.T. Toloza, Esneyder Polo, Elíseo Díaz Varela
article en

Abstract

The influence of zirconia incorporation and template type on the physicochemical properties of NiMo/Al2O3-ZrO2 catalysts was investigated for the hydrodesulfurization (HDS) of 4,6-dimethyldibenzothiophene (4,6-DMDBT) and the hydrogenation (HYD) of naphthalene (N). Catalysts were prepared by co-impregnation on supports synthesized via a sol-gel method using starch (A) and activated carbon (C) as structure-directing templates, followed by zirconium incorporation through a grafting procedure. The resulting materials were characterized by SEM–EDX, N2 physisorption, H2-TPR, XPS, HRTEM, and pyridine-FTIR. SEM-EDX confirmed homogeneous metal distributions and compositions close to nominal values (Mo = 20 wt%, Ni = 5 wt%, Zr = 11 wt%) with Ni/(Ni + Mo) = 0.30. N2 adsorption–desorption isotherms correspond to type IV(a) with H3-H4 hysteresis loops, characteristic of mesoporous structures. After metal incorporation, surface areas decreased to 96 m2 g−1 for NiMo/Al2O3 and 81 m2 g−1 for Zr-modified catalysts, while the activated carbon-templated sample preserved a larger mesoporous volume (0.335 cm3 g−1) and higher macroporosity (72%). H2-TPR profiles indicated improved reducibility for Zr-containing catalysts. XPS revealed an increase of MoS2 species from 45% in NiMo/Al2O3 to 75% in NiMo/Al2O3-ZrO2(C), accompanied by a higher degree of sulfidation index (DSI) from 47.1% to 73.9%. HRTEM analysis of Zr-modified catalysts revealed longer MoS2 slabs (11.8–12.1 nm) and higher edge-to-corner ratios (17–17.4) compared with NiMo/Al2O3 (6.2 nm; fe/fc = 8.2). Pyridine-FTIR showed a substantial increase in total acidity from 91 to 421 μmol g−1 upon Zr addition. Catalytically, NiMo/Al2O3-ZrO2(C) exhibited the highest HDS conversion (40%), reaction rate (10.5 × 10−9 mol s−1 g−1), and TOF (4.69 × 10−5 s−1), whereas NiMo/Al2O3-ZrO2(A) reached the highest naphthalene conversion (97.18%), with a reaction rate of 27.4 × 10−7 mol s−1 g−1 and TOF of 12.9 × 10−3 s−1. These results demonstrate that Zr incorporation and the activated carbon template favored hydrodesulfurization, whereas the starch template promoted hydrogenation performance.

InorganicsVol. 14(4)
University of Atlántico (CO), University of the Coast (CO)
Universidad del Atlántico
Openalex Percentile: Top 26%
Catalysis and Hydrodesulfurization Studies
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