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Deep oxidative desulfurization of model fuels catalysed by immobilized ionic liquid on MIL-100(Fe)

Deep desulfurization of fossil fuels has become urgently required because of the serious pollution by the large-scale use of fossil fuels. In this study, [PrSO(3)HMIm]HSO(4)@MIL-100(Fe) was synthesized by wet-impregnation of the ionic liquid (IL) of [PrSO(3)HMIm]HSO(4) on MIL-100(Fe). The constructi...

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Detalles Bibliográficos
Autores principales: Yang, WanXin, Guo, Guoqing, Mei, Zhihong, Yu, Yinghao
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9066548/
https://www.ncbi.nlm.nih.gov/pubmed/35518850
http://dx.doi.org/10.1039/c9ra03035b
Descripción
Sumario:Deep desulfurization of fossil fuels has become urgently required because of the serious pollution by the large-scale use of fossil fuels. In this study, [PrSO(3)HMIm]HSO(4)@MIL-100(Fe) was synthesized by wet-impregnation of the ionic liquid (IL) of [PrSO(3)HMIm]HSO(4) on MIL-100(Fe). The construction of [PrSO(3)HMIm]HSO(4)@MIL-100(Fe) was then confirmed by X-ray powder diffraction, N(2) adsorption–desorption experiments, infrared spectroscopy and elemental analysis, and then applied in the oxidative desulfurization of model fuels. In comparison with the corresponding IL, [PrSO(3)HMIm]HSO(4)@MIL-100(Fe) showed an enhanced performance in the desulfurization rate of model fuels due to the increase of the mass transfer rate. Under the optimized conditions (oxidant to sulphur ratio = 25, oil to acetonitrile ratio = 1, and temperature = 60 °C), a sulphur removal rate of 99.3% was observed (initial sulphur concentration = 50 ppm). The sulphur removal of three sulphur compounds by catalytic oxidation and extraction followed the order of dibenzothiophene (DBT) > thiophene (T) > benzothiophene (BT).