Preparation and characterization of TiO2 support for Pd catalysts: Application in hydrogenation of 4-carboxybenzaldehyde

被引:5
作者
Kan, Yu [1 ]
Li, Kai [1 ]
Wang, Jiyuan [2 ]
Lin, Ling [1 ]
Zeng, Chongyu [1 ]
机构
[1] Nanjing Univ Technol, Coll Chem & Chem Engn, Nanjing 210009, Jiangsu, Peoples R China
[2] Res Inst Yangzi Petrochem Co Ltd, SINOPEC, Nanjing PT-210048, Jiangsu, Peoples R China
来源
NATURAL RESOURCES AND SUSTAINABLE DEVELOPMENT, PTS 1-3 | 2012年 / 361-363卷
关键词
TiO2; support; Compression method; Pd/TiO2; Hydrogenation of 4-CBA; PARTICLES;
D O I
10.4028/www.scientific.net/AMR.361-363.584
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The formed TiO2 supports were prepared by compression method and then used in the Pd/TiO2 catalytic hydrogenation of 4-carboxybenzaldehyde (4-CBA). Supports and catalysts were characterized by the intensity test, BET, XRD, SEM and ICP techniques. Results showed that the pore-forming agent can adjust both the specific surface and average pore diameter. The suitable content is 4 wt.%. Silicon additive inhibits the growth of TiO2 grain and the anatase-rutile phase transformation. Forming pressure brings out a certain crushing strength and pore characteristic. The crushing strength of support significantly increases with increasing support calcination temperature. However, the specific surface and pore volume decrease. The TiO2 support has the side crushing strength of 122 N/cm and the specific surface of 38 m(2)/g at the optimum preparation conditions of silicon additive of 4 wt.%, forming pressure of 150 MPa and calcination temperature of 700 degrees C. A series of Pd/TiO2 catalysts were prepared by incipient wetness of impregnation and liquid-phase chemical reduction method. On Pd/TiO2700 (Pd, 0.5 wt.%) catalyst, the 99.5% conversion of 4-CBA is obtained after reaction for 90 min at reaction temperature of 280 degrees C and hydrogen partial pressure of 0.6 MPa.
引用
收藏
页码:584 / +
页数:3
相关论文
共 30 条
  • [1] FORMING OF HIGH SURFACE-AREA TIO2 TO CATALYST SUPPORTS
    BANKMANN, M
    BRAND, R
    ENGLER, BH
    OHMER, J
    [J]. CATALYSIS TODAY, 1992, 14 (02) : 225 - 242
  • [2] Bartos T.M., 1997, US. Patent, Patent No. [5,616,792, 5616792]
  • [3] Chang Y.Q., 2003, CN. Patent, Patent No. [1,457,922, 1457922]
  • [4] Chen XH., 1992, Petro Indus, V21, P557
  • [5] Reversible deactivation of TiO2 in CS2 conversion associated with Claus reaction
    Clark, P. D.
    Dowling, N. I.
    Huang, M.
    [J]. APPLIED CATALYSIS A-GENERAL, 2008, 343 (1-2) : 104 - 108
  • [6] Dogterom R.J., 2006, WO. Patent, Patent No. [2,006,048,424, 2006048424]
  • [7] Bimetallic Rh-Ge and Pt-Ge catalysts supported on TiO2 for citral hydrogenation II.: Catalytic properties
    Ekou, T.
    Vicente, A.
    Lafaye, G.
    Especel, C.
    Marecot, P.
    [J]. APPLIED CATALYSIS A-GENERAL, 2006, 314 (01) : 73 - 80
  • [8] Fox E., 2000, CN. Patent, Patent No. [1,269,787, 1269787]
  • [9] Titanium dioxide photocatalysis: present situation and future approaches
    Fujishima, A
    Zhang, XT
    [J]. COMPTES RENDUS CHIMIE, 2006, 9 (5-6) : 750 - 760
  • [10] Comparison of different iron-based catalysts for photocatalytic removal of imidacloprid
    Guzsvany, Valeria
    Banic, Nemanja
    Papp, Zsigmond
    Gaal, Ferenc
    Abramovic, Biljana
    [J]. REACTION KINETICS MECHANISMS AND CATALYSIS, 2010, 99 (01) : 225 - 233