期刊文献+

CoMo/TiO_2和CoMo/γ-Al_2O_3催化剂硫化行为的研究 被引量:1

STUDIES ON SULFIDATION OF CoMo/TiO_2 AND CoMo/Al_2O_3 CATALYSTS
下载PDF
导出
摘要 运用程序升温硫化和原位激光拉曼光谱方法研究了CoMo/Al_2O_3和CoMo/TiO_2催化剂的硫化行为。结果表明,两种载体上Co和Mo氧化态物种的硫化均通过O-S交换,Mo—S或Co—S键断裂,元素S被H_2还原和高温下进一步深度硫化等多步骤完成。由于TiO_2载体上Mo物种主要以八面体配位Mo—O—Mo形式存在以及TiO_2载体参与硫化过程,CoMo/TiO_2比CoMo/Al_2O_3容易硫化。 The sulfidation of CoMo/TiO_2 and CoMo/Al_2O_3 catalysts was studied by means of temperature programmed sulfiding (TPS) and in situ laser raman spectroscopy (LRS). The results showed that CoMo supported on TiO_2 and Al_2O_3 are sulfided to MoS_2 and Co_9S_8 by a multistep process. First, oxidie Co and CoMo species are partially sulfided by O-S exchange at low temperature forming Mo and CoMo oxysulfide. Then, the Mo—S or Co—S bond reptures in the presence of H_2 to produce H_2S. Finally, the deep sulfiding of Mo or CoMo oxysulfide occurs forming crystalline sulfides of Mo and Co. It has been found that the sulfidation of CoMo/TiO_2 catalysts takes place at much lower temperature as compared with CoMo/Al_2O_3 catalyst. The reasons are that the main Mo species on TiO_2 support exist in octahedral Mo—O—Mo bridge structure, which are easilly to be sulfided, while the presence of tetrahedral Mo species on Al_2O_3 support needs higher temperature for sulfiding. Another difference between CoMo/TiO_2 and CoMo/Al_2O_3 is that the oxygen in TiO_2 support can be exchanged with S in H_2S, thus promoting the sulfiding of Co and Mo species, while Al_2O_3 does not.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 1994年第4期18-24,共7页 Acta Petrolei Sinica(Petroleum Processing Section)
  • 相关文献

参考文献1

二级参考文献3

  • 1魏昭彬,1990年
  • 2魏昭彬,Appl Catal,1990年,63卷,306页
  • 3Cheng C P,J Catal,1979年,60卷,276页

共引文献16

同被引文献40

  • 1葛晖,李学宽,秦张峰,王建国.油品深度加氢脱硫催化研究进展[J].化工进展,2008,27(10):1490-1497. 被引量:28
  • 2曾崇余,汤升亮,周立进.一种纳米二氧化钛成型物及其制备方法:中国,1778466[P].2006-05-31.
  • 3Roukoss C, Laurenti D, Devers E, et al. Hydrodesulfurization catalysts: Promoters, promoting methods and support effect on catalytic activities[J]. Comptes. Rendus. Chimie., 2009, 12: 683-691.
  • 4Segawa K, Takahashi K, Satoh S. Development of new catalysts for deep hydrodesulfurization of gas oil [J]. Catalysis Today, 2000, 63: 123-131.
  • 5Aridi T N, Al-Daous M A. HDS of 4, 6-dimethyldibenzothiophene over MoS2 catalysts supported on macroporous carbon coated with aluminosilicate nanoparticles[J]. Applied Catalysis A: General, 2009, 359: 180-187.
  • 6Shaft R, Hutchings G J. Hydrodesulfurization of hindered dibenzothiophenes: an overview[J]. Catalysis Today, 2000, 59: 423-442.
  • 7Ramirez J, Sanchez-Minero F. Support effects in the hydrotreatment of model molecules[J]. Catalysis Today, 2008, 130: 267-271.
  • 8Mochida I, Isoda T, Ma X, et al. Deep hydrodesulfurization of diesel fuel: design of reaction process and catalysts[J]. Catalysis Today, 1996, 29: 185-189.
  • 9Babich I V, Moulijn J A. Science and technology of novel processes for deep desulfurization of oil refinery streams: a review [J]. Fuel, 2003, 82 (6): 607-631.
  • 10Ramirez J, Macfas G, Castillo P, et al. The role of titania in supported Mo, CoMo, NiMo, and NiW hydrodesulfurization catalysts: analysis of past and new evidences[J]. Catalysis Today, 2004, 98: 19-30.

引证文献1

二级引证文献14

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部