4.2 Article

Oxidative desulfurization of model oil and oil cuts with MoO3/SBA-15: experimental design and optimization by Box-Behnken method

Journal

REACTION KINETICS MECHANISMS AND CATALYSIS
Volume 131, Issue 2, Pages 935-951

Publisher

SPRINGER
DOI: 10.1007/s11144-020-01852-2

Keywords

Oxidative desulfurization (ODS); Catalyst; MoO3/SBA-15; Dibenzothiophene (DBT); Box-Behnken (BBD); H2O2

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Using wet impregnation method, MoO(3)particles were loaded on hierarchical silica support, SBA-15, and applied for oxidative desulfurization (ODS) process from a model oil containing dibenzothiophene (DBT). The experiments were carried out by the use of H(2)O(2)and acetonitrile as oxidant and extractant. The MoO3/SBA-15 catalyst was characterized by powder X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), energy dispersive X-ray spectroscopy (EDX), field emission scanning electron microscope (FE-SEM) and Brunauer-Emmett-Teller (BET) analyses. At first, the effect of molybdenum loading was examined. Then, the effect of operating parameters on ODS including temperature, catalyst dosage, the molar ratio of H2O2/DBT and reaction time were investigated using Box-Behnken experimental design. The complete efficiency, similar to 100% S removal, was achieved by 0.004 g mL(-1)catalyst at 55 degrees C within 49 min reaction time and H2O2/DBT = 9. At the optimized operating conditions, real oil cuts of gasoline and gas oil were tested and the S removal efficiency of 69.73% and 49% was achieved. The desulfurization activity of the catalyst from DBT model oil after 5 times regeneration was above 93%.

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