Volume 46 Issue 5
May  2018
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Article Contents
ZHANG Jin-ling, SONG Chun-min, WANG Yan-zhen, DUAN Hong-ling. Preparation of Co-Mo/SiO2-Al2O3 catalyst for hydrotreating lubricating oil[J]. Journal of Fuel Chemistry and Technology, 2018, 46(5): 543-550.
Citation: ZHANG Jin-ling, SONG Chun-min, WANG Yan-zhen, DUAN Hong-ling. Preparation of Co-Mo/SiO2-Al2O3 catalyst for hydrotreating lubricating oil[J]. Journal of Fuel Chemistry and Technology, 2018, 46(5): 543-550.

Preparation of Co-Mo/SiO2-Al2O3 catalyst for hydrotreating lubricating oil

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  • Corresponding author: WANG Yan-zhen, E-mail: yanzhenw@upc.edu.cn
  • Received Date: 2017-12-15
  • Rev Recd Date: 2018-03-12
  • Available Online: 2021-01-23
  • Publish Date: 2018-05-10
  • SiO2-Al2O3, with a mass content of 5%, 10% and 15%, was synthesized by using a Al(NO3)3-NaAlO2 double hydrolysis method, with surfactant Pluronic P123 as template and Si(OC2H5)4 as Si source. The Co-Mo/SiO2-Al2O3 hydrotreating catalysts for lubricating oil were then prepared by co-impregnation method and characterized by a series of techniques such as XRD, N2 sorption, Py-FTIR, NH3-TPD, H2-TPR, TEM and XRF. The results show that the SiO2-Al2O3 support containing 10% Si is provided with abundant moderate-strong acid sites and partially ordered mesoporous structure; MoS2 particles are uniformly dispersed on the SiO2-Al2O3 surface. Moreover, the Co-Mo/10%SiO2-Al2O3 catalyst exhibits high amount of Bronsted acid sites and type Ⅱ CoMoS active phase. The catalytic performance was evaluated in a high-pressure fixed-bed reactor, with second vacuum side distillate oil as the raw material oil. The results show that the Co-Mo/10%SiO2-Al2O3 catalyst exhibits high activity in hydrotreating and paraffins and cycloalkanes are the main components in product oil. Under 380℃, 15 MPa, a space velocity of 0.6 h-1, and a hydrogen to oil ratio of 1000, the HDS and HDN values over Co-Mo/10%SiO2-Al2O3 exceed 99%. Meanwhile, the contents of S and N in the product are less than 10 and 2 μg/g, respectively, which can meet the requirements on the raw materials for the subsequent isomerization dewaxing process.
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