期刊文献+

混捏法制备的Ni-Mo/γ-Al_2O_3加氢催化剂中活性组分存在状态的研究 被引量:1

STUDY ON THE STATE OF Ni AND Mo IN Ni Mo/γ-Al 2O 3 CATALYST
下载PDF
导出
摘要 利用XRD、TEM、UV-漫反射光谱分析等手段,探讨了混捏法制备的Ni-Mo/γ-Al2O3催化剂中活性组分的存在状态及其随Ni、Mo原子比ρ和焙烧温度T变化而变化的情况。结合样品的加氢活性测定结果,得出样品表面上的新相xNiO·yMoO3·zH2O的相对含量的变化规律以及表面八面体配位状态Ni〔O〕的相对含量的变化规律与样品加氢活性的变化规律相同。研究认为,新相xNiO·yMoO3·zH2O为Ni-Mo/γ-Al2O3催化剂的活性相,xNiO-yMoO3·zH2O中的Ni为八面体配位状态的Ni。 By means of X ray diffraction (XRD),transmission electron microscopy (TEM) and UV visible diffuse reflection spectronscopy (DRS),the state of active components of the kneading prepared catalyst Ni Mo/γ Al 2O 3 was studied.The relation between catalytic acti vity of hydrogenation and the state of active components was also investigated.The experimental results show that nickel(Ni) and molybdenum (Mo) are entirely dispersed on the surface of γ Al 2O 3,and the active components of Ni and Mo existed as the phases of MoO 3,δ NiAl 26 O 40 ,NiAl 2O 4,NiMoO 4 and xNiO·yMoO 3·zH 2O.The relative content of each phase varies with the atomic ratio of Ni and Mo and the calcination temperature.When the atomic ratio of Ni and Mo is 0 4 and the calcination temperature to be 550℃,the relative content of the xNiO·yMoO 3·zH 2O phase reaches its maximum,so does the relative content of the octahedral Ni (Ni O ) with further study of Ni coordinate state.The hydrogenation activity evaluation also show that the variation of relative contents of xNiO·yMoO 3·zH 2O and Ni O phases has the same trend as the hydrogenation activity.As a result,xNiO·yMoO 3·zH 2O phase is supposed to be the active phase in which Ni is in the octahedral coordinated state.
机构地区 天津大学化工系
出处 《石油学报(石油加工)》 CSCD 北大核心 1996年第3期9-15,共7页 Acta Petrolei Sinica(Petroleum Processing Section)
关键词 活性相 加氢催化剂 混捏法 Ni Mo/γ Al 2O 3 catalyst active phase state of Ni and Mo
  • 相关文献

二级参考文献3

  • 1李大东,第三届全国催化会议,1986年
  • 2李大东,催化学报,1981年,2卷,4期,275页
  • 3吴新国,科学通报,8期,590页

共引文献17

同被引文献17

  • 1Marafi A, Hauser A, Stanislaus A. Deactivation patterns of Mo/Al2O3 ,Ni-Mo/Al2O3 and NiMoP/Al2O3 catalysts in atmospheric residue hydrodesulphurization[J]. Catalysis Today,2007,125(3-4) : 192-202.
  • 2Maity S K, Perez V H, Aneheyta J, et al. Catalyst deactivation during hydrotreating of Maya crude in a batch reactor [J]. Energy &Fuels,2007,21(2):636-639.
  • 3Hung C W, Howell R L,Johnson D R. HDM catalysts can be tailored to provide residuum hydroprocessing units flexibility to process heavy crudes[J]. Chem Engng Prog, 1986,85: 57-64.
  • 4Limbach K W, Wei James, Effect of nonuniform activity on Hydrodemetallation catalyst[J]. AIChE J, 1988, 34 (2) : 305-313.
  • 5Sepehr A, Muhammad S, Computer simulations of catalyst deactivation : II. The effect of morphological, transportand kinetic parameters on the performance of the catalyst [J]. Chem Eng Sci,1991,46(7) :1749-1755.
  • 6Chiang Chien Lih, Fang Zhong Ren, Simulation and optimal design for the residual oil hydrodemetallation in a cocurrent moving bed reactor[J]. Chem Eng Sci, 1994,49(8) : 1175-1183.
  • 7Liu Xue,Khinast J G. ,Benjamin J,et al. A parametric investigation of impregnation and drying of supported catalysts [J]. Chem Eng Sci,2008,63(18):4517-4530.
  • 8Komiyama M. Design and preparation of impregnated eatalysts[J]. Catal Rev-Sci Eng,1985,27(12) :341-372.
  • 9Lekhal A, Glasser B, Khinast J G. Impact of drying on the catalyst profile of supported impregnation eatalysts[J]. Chem Eng Sci,2001a,56(15) :4473-4487.
  • 10I.ekhal A,Glasser B,Khinast G, In{luence of pH and ionic strength on the metal profile of impregnation catalysts[J]. Chem Eng Sci,2004,59(5) :1063-1077.

引证文献1

二级引证文献10

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