Catalytic oxidative desulfurization(ODS) of model oil and commercial oil samples was investigated using an air-assisted performic acid oxidation system with a phase transfer or emulsion catalyst comprising a quaternar...Catalytic oxidative desulfurization(ODS) of model oil and commercial oil samples was investigated using an air-assisted performic acid oxidation system with a phase transfer or emulsion catalyst comprising a quaternary ammonium salt-based heteropolyoxometalate.Different emulsion catalysts with a Keggin type heteroployoxometalate anion(containing W,Mo,and V) and cetyltrimethylammonium bromide cation were prepared and characterized by X-ray fluorescence,Fourier transform infrared spectroscopy,and scanning electron microscopy.[C16H33N(CH3)3]3[PW9Mo3O40] was the most effective catalyst in the current oxidation system,which reduced the sulfur content of the model oil from 1275 μg/g to 57 μg/g.The reactivity order of different model sulfur compounds was thiophene < dibenzothiophene < 4,6-dimethyldibenzothiophene. The ODS of model sulfur compounds followed first order kinetics with apparent activation energy from 29 to 27 kJ/mol.The catalysts also performed efficiently in the ODS of the industrial oil samples,including untreated naphtha,light gas oil,heavy gas oil,and Athabasca oil sands derived bitumen,for which sulfur removal rates were 83%,85%,68% and 64%,respectively.展开更多
Ti Ce complex oxide catalysts for catalytic wet air oxidation of acetic acid as model reactant were prepared by coprecipitation and impregnation methods. The catalysts are very stable during the reaction. The presence...Ti Ce complex oxide catalysts for catalytic wet air oxidation of acetic acid as model reactant were prepared by coprecipitation and impregnation methods. The catalysts are very stable during the reaction. The presence of Bi as base center has promotion effect on the catalyst activity. The optimal Bi content is about 4% (molar fraction). With the increase of calcination temperature, the BET surface area of the catalysts is decreased and so is the activity of the catalysts. The activity of the catalysts and the Bi effect are discussed based on the reference results.展开更多
基金Financial support from the Higher Education Commission(HEC) Pakistan,under the International Research Support Initiative Program(IRSIP)
文摘Catalytic oxidative desulfurization(ODS) of model oil and commercial oil samples was investigated using an air-assisted performic acid oxidation system with a phase transfer or emulsion catalyst comprising a quaternary ammonium salt-based heteropolyoxometalate.Different emulsion catalysts with a Keggin type heteroployoxometalate anion(containing W,Mo,and V) and cetyltrimethylammonium bromide cation were prepared and characterized by X-ray fluorescence,Fourier transform infrared spectroscopy,and scanning electron microscopy.[C16H33N(CH3)3]3[PW9Mo3O40] was the most effective catalyst in the current oxidation system,which reduced the sulfur content of the model oil from 1275 μg/g to 57 μg/g.The reactivity order of different model sulfur compounds was thiophene < dibenzothiophene < 4,6-dimethyldibenzothiophene. The ODS of model sulfur compounds followed first order kinetics with apparent activation energy from 29 to 27 kJ/mol.The catalysts also performed efficiently in the ODS of the industrial oil samples,including untreated naphtha,light gas oil,heavy gas oil,and Athabasca oil sands derived bitumen,for which sulfur removal rates were 83%,85%,68% and 64%,respectively.
文摘Ti Ce complex oxide catalysts for catalytic wet air oxidation of acetic acid as model reactant were prepared by coprecipitation and impregnation methods. The catalysts are very stable during the reaction. The presence of Bi as base center has promotion effect on the catalyst activity. The optimal Bi content is about 4% (molar fraction). With the increase of calcination temperature, the BET surface area of the catalysts is decreased and so is the activity of the catalysts. The activity of the catalysts and the Bi effect are discussed based on the reference results.
