Photocatalytic oxidative desulfurization of model oil catalyzed by TiO2 with different crystal structure in the presence of phase transfer catalyst
- Authors: Song H.1,2, Zhu N.1, Chen B.3, Wang F.1, Bai M.4, Wang X.1
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Affiliations:
- College of Chemistry & Chemical Engineering
- Provincial Key Laboratory of Oil & Gas Chemical Technology
- Personnel Department
- Department of Petroleum Engineering
- Issue: Vol 89, No 12 (2016)
- Pages: 2076-2083
- Section: Various Technological Processes
- URL: https://journal-vniispk.ru/1070-4272/article/view/214598
- DOI: https://doi.org/10.1134/S1070427216120211
- ID: 214598
Cite item
Abstract
The photocatalytic oxidative desulfurization is one of the promising processes to realize the deep desulfurization of the fuel. A series of TiO2 nanoparticles (TiO2 NPs) were prepared to investigate the effect of annealing temperatures on its physical properties and the photocatalytic oxidative desulfurization performance. Their physicochemical properties were investigated by X–ray diffraction (XRD), fourier transform infrared spectroscopy (FTIR), thermal gravimetric and differential thermal analysis (TG–DTA), scanning electron microscopy (SEM), and X–ray energy dispersive spectrometer (EDS). The results show that, the crystallite structure of TiO2 NPs annealed at 250–450°C was mainly composed of anatase phase. The rutile phase appeared when the anneal temperature increased to 550°C and all of the anatase converted into rutile phase when annealed at 750°C. The effect of crystallite structure of TiO2 on its photocatalytic oxidative desulfurization performance was investigated using benzothiophene (BT) as the model sulfur compound. The anatase phase was preferable for the photocatalytic oxidation of BT. Phase transfer catalyst plays an important role for improving the photocatalytic desulfurization rate. The photocatalytic oxidative reaction mechanism was also proposed in the presence of TiO2 as catalyst, H2O2 as oxidant, and the DMDAAC as phase transfer catalyst. In the heterogeneous catalytic system, the entire reaction rate is mainly determined by the oxidation reaction and the extraction process, in which the oxidation process could be the rate determining step.
About the authors
Hua Song
College of Chemistry & Chemical Engineering; Provincial Key Laboratory of Oil & Gas Chemical Technology
Email: wangji624@163.com
China, Heilongjiang, 163318; Daqing, 163318
Ningfang Zhu
College of Chemistry & Chemical Engineering
Email: wangji624@163.com
China, Heilongjiang, 163318
Bo Chen
Personnel Department
Email: wangji624@163.com
China, Heilongjiang, 163318
Fang Wang
College of Chemistry & Chemical Engineering
Email: wangji624@163.com
China, Heilongjiang, 163318
Mingxing Bai
Department of Petroleum Engineering
Email: wangji624@163.com
China, Daqing, 163318
Xueqin Wang
College of Chemistry & Chemical Engineering
Author for correspondence.
Email: wangji624@163.com
China, Heilongjiang, 163318
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