期刊文献+

超增溶自组装法纳米Ni-Al_2O_3体相催化剂的合成及表征 被引量:4

Synthesize of Bulk Ni-Al_2O_3 Catalysts in the Way of Super-Solubilization Nanometer Self-Assembly and Its characterization
下载PDF
导出
摘要 采用超增溶自组装法进行纳米Ni-Al2O3体相催化剂的制备。对所制备的Ni-Al2O3体相催化剂进行了XRD和压汞法表征。通过实验考察了尿素质量分数、表面活性剂质量分数、NiO质量分数等因素与Ni-Al2O3体相催化剂物化特性之间的关系。结果表明,尿素质量分数为(基准+5)%,表面活性剂质量分数为(基准+2)%,NiO质量分数为(基准+3)%时,Ni-Al2O3催化剂具有较好的孔结构。制备的体相催化剂的比表面积主要集中在186~324m2/g;孔径在3~12nm,属于中、大孔范围,孔径大小均匀、分布集中;孔容较大,在0.45~0.89mL/g,能够满足加氢催化剂的要求,是比较理想的纳米体相催化剂。该合成方法降低了表面活性剂和水的质量分数,操作工艺简单,反应易于控制,制得的纳米粒子比现有的渣油加氢催化剂性能优良,具有工业化生产应用价值。 Bulk Ni-Al2O3 catalysts was synthesized in the way of super-solubilization nanometer self-assembly. The bulk Ni- Al2O3 catalyst was characterized by X-ray diffraction (XRD) and the mercury porosimeter. The influence of affecting factors on physical properties of catalysts was investigated, such as the amount of urea and surfactant, and the amount of nikel oxide. The results show that bulk Ni-Al2O3 catalysts has a better bore structure, which is made from based amount plus 2 of surfactants, based amount plus 5 of urea and plus 3 of NiO. Specific area of the bulk Ni-Al2O3 catalyst is between 186 m2/g to 324 mr/g, bore diameter is 3- 12 nm, and the diameter of bore is even and distribute concentration, witch is belong to medium and big bore scope, the bore permits is 0.45-0.89 mL/g. This bulk catalyst is a more ideal bulk catalyst which can satisfy the request of hydrogenation. This synthesize method has more merits, such as decreasing the dosage of surfactant and aqueous, operation craft simple, reaction can be controlled easily. Nanometer bulk catalyst has a good application value in industrialize production because of its better property than the residue oil hydrogenation catalyst.
出处 《辽宁石油化工大学学报》 CAS 2013年第1期30-34,共5页 Journal of Liaoning Petrochemical University
关键词 超增溶 自组装 纳米 体相 表面活性剂 氧化铝 Super-solubilization Self-assembly Nanometer Bulk Surfactant Alumina
  • 相关文献

参考文献13

二级参考文献74

  • 1肖招金,黄星亮.镍基催化剂上硫醇与异戊二烯硫醚化反应的研究[J].分子催化,2005,19(4):280-284. 被引量:12
  • 2路勇,邓存,丁雪加,沈师孔.Ni/Al_2O_3催化剂上甲烷部分氧化制合成气[J].催化学报,1996,17(1):28-33. 被引量:30
  • 3邓存,谢鸿芳,黄炎琳,童迅.负载型镍催化剂催化性能研究[J].吉林化工学院学报,1996,13(4):18-22. 被引量:4
  • 4安高军,柳云骐,柴永明,刘晨光.柴油加氢精制催化剂制备技术[J].化学进展,2007,19(2):243-249. 被引量:7
  • 5Song C. An overview of new approaches to deep desulfurization for ultra-clean gasoline, diesel fuel and jet fuel. Catal Today, 2003,86:211
  • 6EPA,Control of air pollution from new motor vehicles amendment to the tier 2/gasoline sulfur regulations, US Environmental Protection Agency, April 13,2001, http://www. epa. gov/fedrgstr/EPA AIR/ 2001/April/Day-13/a8927. htm
  • 7Topsφe H, Clausen B S, Massoth F E. In : Anderson J R, Boudart M eds. Hydrotreating Catalysis-Science and Technology, Springer, Berlin, 1996. Vol. 11
  • 8Whitehurst D D,Isoda T,Mochida I. Present state of the art and future challenges in the hydrodesulfurization of polyatomarie sulfur compounds. Adv Catal, 1998,42 : 345
  • 9Startsev A N. The mechanism of HDS catalysis. Catal Rev Sci Eng,1995,37:353
  • 10Alvarez L, Espino J, Ornelas C, et al. Comparative study of MoS2 and Co/MoS2 catalysts prepared by ex sstu/in situ activation of ammonium and tetraalkylammonium thiomolybdates. J Mol Catal A,2004,210(1-2):105-117

共引文献77

同被引文献49

引证文献4

二级引证文献4

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