期刊文献+

氟硅酸铵处理对γ-Al_2O_3负载NiW催化剂性质的影响 被引量:3

EFFECT OF FLUORINATION WITH (NH 4) 2SiF 6 ON SURFACE PROPERTIES AND ACTIVITY OF NiW/Al 2O 3 CATALYST
下载PDF
导出
摘要 应用IR,XPS,TPR,NO和CO2吸附及脉冲微反等技术研究了氟硅酸铵处理前后γ-Al2O3及负载NiW催化剂的表面性质,探讨了其改性机理和它对催化剂活性相的影响.结果表明,经氟硅酸铵处理后,γ-Al2O3表面的不饱和四面体空位及其四配位Al3+上的强碱性羟基均明显减少,改变了γ-Al2O3表面的酸碱性和Ni2+在γ-Al2O3表面的分布,使NiO倾向分布于γ-Al2O3的八面体空位.过量的氟硅酸铵处理将明显破坏γ-Al2O3表面的碱性羟基,导致WO3和NiO的分散度下降,使改性后催化剂的噻吩加氢脱硫性能降低. The surface properties of γ Al 2O 3 and NiW/Al 2O 3 samples before and after fluorination with (NH 4) 2SiF 6 have been studied by using IR, XRD, XPS and adsorption of NO and CO 2. Their activity for HDS of thiophene has been measured with pulse micro reaction system. The mechanism of fluorination and its influence on the active phase of the catalyst have also been discussed. The results show that the tetrahedral vacancies of γ Al 2O 3, which contain more net positive charge as well as its strongest basic OH groups cordinated to tetrahedral Al 3+ , decrease when γ Al 2O 3 is fluorinated with (NH 4) 2SiF 6. It causes the Ni species on NiW F/Al 2O 3 to prefer to occupy the octahedral vacancies of γ Al 2O 3. However, when γ Al 2O 3 is fluorinated excessively with (NH 4) 2SiF 6, its basic OH groups are replaced largely by F -, which reduces the dispersity of WO 3 and NiO. This disadvantage would cover up the advantage of fluorination for the distribution of Ni species and cut down HDS activity of fluorinated catalyst.
机构地区 复旦大学化学系
出处 《催化学报》 SCIE CAS CSCD 北大核心 1997年第4期279-283,共5页
基金 抚顺石油化工研究院资助
关键词 氟化 氟硅酸铵 负载型 催化剂 加氢 炼油 Alumina, Fluorination, Ammonium fluorosilicate, Nickel, Tungsten, Supported catalyst, Hydrodesulfurization
  • 相关文献

参考文献3

  • 1牛国兴,催化学报,1993年,增刊,57页
  • 2建谋,分子催化,1990年,4卷,104页
  • 3建谋,分子催化,1990年,4卷,181页

同被引文献17

  • 1建谋,杨先春,石亚华,李大东.氟在γ-Al_2O_3及NiW/γ-Al_2O_3催化剂中的作用——Ⅱ.镍、钨的存在状态[J].分子催化,1990,4(3):181-187. 被引量:10
  • 2Han Y S,Li J B,Ning X S,et al.[J].Materials Science and Engineering,2004,A369:241-244.
  • 3Kadinov G,Praliaud H,Primet M,et al.[J].Appl.Catal,1984,10:63-73.
  • 4Eijsbouts S,Van Gestel J N M,Van Veen J A R.et al.[J].J.Catal,1991,131(2):412-432.
  • 5Ahuja S P,Derrien M L,Le Page J F,et al. Activity and selectivity of hydrotreating catalysts. Ind Eng Chem Prod Res Dev,1970,9(3):272-281
  • 6Vradam L, Landau M V, Herskowitz M. Deep desulfurization of diesel fuels:kinetic modeling of model compounds in tricklebed. Catal Today,1999,48(1-4) :41-48
  • 7Bhatia S,Beltramini J,Do D D. Temperature programmed analysis and its applications in catalytic systems. Catal Today,1990,7(3) :309-438
  • 8Scheffer B, Molhoek P, Moulijn J A. Temperature-programmed reduction of NiO-WO3/Al2O2 hydrodesulphurization catalysts. Appl Catal,1989,46(1) :11-30
  • 9Louwers S P A,Prins R. An EXAFS study on the Ni and W environment in carbon-supported, sulfided W and NiW catalysts. J Catal, 1993,139 : 525- 539
  • 10Mangnus P J, Bos A, Mouliin J A. Temperature-programmed reduction of oxidic and sulfidic alumina-supported NiO,WO3,and NiO-WO3 catalysts. J Catal, 1994,146: 437 -448

引证文献3

二级引证文献68

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