Effect of phosphorus on the hydrodesulfurization and hydrodenitrogenation performance of presulfided NiMo/Al2O3 catalyst

被引:5
作者
Xiang C.-E. [1 ,2 ]
Chai Y.-M. [3 ]
Fan J. [3 ]
Liu C.-G. [1 ,3 ]
机构
[1] State Key Laboratory of Heavy Oil Processing, China University of Petroleum (East China)
[2] China Petroleum Engineering and Construction Corporation East-China Design Branch
[3] Key Laboratory of Catalysis, China National Petroleum Corporation
来源
Ranliao Huaxue Xuebao/Journal of Fuel Chemistry and Technology | 2011年 / 39卷 / 05期
关键词
Hydrodenitrogenation; Hydrodesulfurization; Phosphorus;
D O I
10.1016/s1872-5813(11)60026-1
中图分类号
学科分类号
摘要
Phosphorus promoted presulfided NiMo/Al2O3 catalysts were prepared by successive incipient wetness impregnation and characterized by XRD, N2-physisorption, TPR and HRTEM. The effect of phosphorus on the hydrodesulfurization (HDS) hydrodenitrogenation (HDN) performance of the presulfided NiMo/Al2O3 catalyst was investigated. The results indicate that the main active phase is type II MoS2 or Ni-Mo-S phase because of their weak interaction with the support. The incorporation of phosphorus in the catalyst enhances the dispersion of MoS2 particles by increasing the stacking number and reducing the slab length. Phosphorus has no influence on the metal-sulfur bonding energies in the Ni-Mo-S phases and bulk MoS2, but it increases the proportion of Ni-Mo-S phases in the metal sulfides. NiMoP-1.2 catalyst (containing 1.2% phosphorus) exhibits high hydrogenation (HYD) selectivity in the HDS of dibenzothiophene (DBT) and high HDN ratio of quinoline, which can be attributed to its high dispersion of the active phase. The HYD activity in HDS and HDN ratio on NiMoP-1.8 catalyst with excess phosphorus (1.8%) is declined due to the aggregation of MoS2 particles and the decrease of the catalyst surface area.
引用
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页码:355 / 360
页数:5
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