2 Zhejiang Engineering Design Co., Ltd., Juhua Group Corporation,Hangzhou,China,310002
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纸质出版:2013
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黎俊波, 刘习文, 曹灿灿, 等. Silica-gel Supported V Complexes:Preparation, Characterization and Catalytic Oxidative Desulfurization[J]. 中国化学工程学报(英文版), 2013,21(8):860-8661004-954160558-3.
LI Junbo, LIU Xiwen, CAO Cancan, GUO Jia, PAN Zhiquan. Silica-gel Supported V Complexes:Preparation, Characterization and Catalytic Oxidative Desulfurization[J]. Chin.J.Chem.Eng., 2013, 21(8): 860-866.
黎俊波, 刘习文, 曹灿灿, 等. Silica-gel Supported V Complexes:Preparation, Characterization and Catalytic Oxidative Desulfurization[J]. 中国化学工程学报(英文版), 2013,21(8):860-8661004-954160558-3.DOI:
LI Junbo, LIU Xiwen, CAO Cancan, GUO Jia, PAN Zhiquan. Silica-gel Supported V Complexes:Preparation, Characterization and Catalytic Oxidative Desulfurization[J]. Chin.J.Chem.Eng., 2013, 21(8): 860-866.DOI:
Silica-gel Supported V Complexes:Preparation, Characterization and Catalytic Oxidative Desulfurization
3) was prepared and their structures were fully characterized by Fourier transform-infrared spectroscopy (FT-IR)
thermogravimetric analysis (TGA)
X-ray photoelectron spectroscopy (XPS) and inductive coupled plasma emission spectrometer (ICP) etc. XPS revealed that the metal V and SG
n
-PAMAM-MSA combined more closely after the formation of Schiff base derivatives. Their catalytic activities for oxidation of dibenzothiophene were evaluated using tert-butyl hydroperoxide as oxidant. The results showed that the catalyst SG
2.0
-[V
V
O
2
-PAMAM-MSA
]
presented good catalytic activity and recycling time. Meanwhile
the optimal condition for the catalytic oxidation of SG
2.0
-[V
V
O
2
-PAMAM-MSA
]
was also investigated
which showed that when the oxidation temperature was 90℃
time was 60 min
the O/S was 3:1
and the mass content of catalyst was 1%
the rate of desulfurization could reach 85.2%. Moreover
the catalyst can be recycled several times without significant decline in catalytic activity.
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A novel method for the management of sulfone-rich waste produced in the oxidative desulfurization (ODS) process
Oxidative desulfurization of model and real oil samples using Mo supported on hierarchical alumina-silica: Process optimization by Box-Behnken experimental design
Deep oxidative desulfurization of gas oil based on sandwich-type polysilicotungstate supported β-cyclodextrin composite as an efficient heterogeneous catalyst
Oxidative desulfurization of dibenzothiophene over Fe promoted Co-Mo/Al2O3 and Ni-Mo/Al2O3 catalysts using hydrogen peroxide and formic acid as oxidants
Oxidative Desulfurization of Non-hydrotreated Kerosene Using Hydrogen Peroxide and Acetic Acid
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