Preparation and characterization of a novel hydrodesulfurization catalyst

被引:0
|
作者
Zhu Q. [1 ]
机构
[1] Department of Chemistry, Hanshan Normal University
来源
Shiyou Xuebao, Shiyou Jiagong/Acta Petrolei Sinica (Petroleum Processing Section) | 2011年 / 27卷 / 03期
关键词
Deep hydrodesulfurization; Oxycarbide catalyst; Sulfidation;
D O I
10.3969/j.issn.1001-8719.2011.03.023
中图分类号
学科分类号
摘要
The oxidic precursor, NiO-MoO3/γ-Al2O3, was synthesized by the successive impregnation method. The catalysts resulted from the sulfidation, the temperature programmed carburization (TPC), and TPC followed by sulfidation of this precursor, as well as a kind of commercial hydrodesulfurization (HDS) catalyst, were evaluated with dibenzothiophene HDS performance and were characterized by XRD and XPS. It was observed that the sulfidation promoted HDS activity and stability of oxycarbide catalyst, which was attributed to the transformation of some Lewis acid sites to Brönsted acid sties favorable for HDS, while some hydrogenation catalytic performance and a majority of active sites were retained at the same time.
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页码:465 / 470
页数:5
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共 15 条
  • [1] Kelty S.P., Berhault G., Chianelli R.R., The role of carbon in catalytically stabilized transition metal sulfides, Appl Catal A, 322, pp. 9-15, (2007)
  • [2] Mccrea K.R., Logan J.W., Tarbuck T.L., Et al., Thiophene hydrodesulfurization over alumina-supported molybdenum carbide and nitride catalysts: Effect of Mo loading and phase, J Catal, 171, 1, pp. 255-267, (1997)
  • [3] Oshikawa K., Nagai M., Omi S., Characterization of molybdenum carbides for methane reforming by TPR, XRD, and XPS, J Phys Chem B, 105, 38, pp. 9124-9131, (2001)
  • [4] Zhu Q., Zhang Q., Ke D., Et al., Preparation of γ-Al<sub>2</sub>O<sub>3</sub>-supported molybdenum oxycarbide catalyst and its HDS activity, J Fuel Chem & Tech, 36, 3, pp. 316-321, (2008)
  • [5] Eijsbouts S., van den Oetelaar L.C.A., van Puijenbroek R.R., MoS<sub>2</sub> morphology and promoter segregation in commercial type 2 Ni-Mo/Al<sub>2</sub>O<sub>3</sub> and Co-Mo/Al<sub>2</sub>O<sub>3</sub> hydroprocessing catalysts, J Catal, 229, 2, pp. 352-364, (2005)
  • [6] Struis R.P.W.J., Schildhauer T.J., Czekaj I., Et al., Sulfur poisoning of Ni catalysts in the SNG production from biomass: A TPO/XPS/XAS study, Appl Catal A, 362, 1-2, pp. 121-128, (2009)
  • [7] Vogelaara B.M., Kagami N., van der Zijden T.F., Et al., Relation between sulfur coordination of active sites and HDS activity for Mo and NiMo catalysts, J Mol Catal A, 309, 1-2, pp. 79-88, (2009)
  • [8] Ma D., Wang D., Su L., Et al., Carbonaceous deposition on Mo/HMCM-22 catalysts for methane aromatization: A TP technique investigation, J Catal, 208, 2, pp. 260-269, (2002)
  • [9] Aegerter P.A., Quigley W.W.C., Simpson G.J., Et al., Thiophene hydrodesulfurization over alumina-supported molybdenum carbide and nitride catalysts: Adsorption sites, catalytic activities, and nature of the active surface, J Catal, 164, 1, pp. 109-121, (1996)
  • [10] Bej S.K., Bennett C.A., Thompson L.T., Acid and base characteristics of molybdenum carbide catalysts, Appl Catal A, 250, 2, pp. 197-208, (2003)