New insights into parameters controlling the selectivity in hydrocracking reactions

被引:62
作者
Benazzi, E
Leite, L
Marchal-George, N
Toulhoat, H
Raybaud, P
机构
[1] IFP Energies Nouvelles, Div Chim & Physicochim Appl, F-92852 Rueil Malmaison, France
[2] IFP Energies Nouvelles, Direct Sci, F-92852 Rueil Malmaison, France
[3] IFP Energies Nouvelles, Div Dev, F-92852 Rueil Malmaison, France
[4] IFP Energies Nouvelles, Div Cinet & Catalyse, F-92852 Rueil Malmaison, France
关键词
hydrocracking; bifunctional catalyst; zeolite; silica-alumina; phenanthrene; selectivity; force-field simulation; adsorption energy;
D O I
10.1016/S0021-9517(03)00041-1
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Improving the selectivity of the transformation of heavy oils into valuable middle distillates represents one of the current challenges for hydrocracking (HCK) catalysts. For that purpose, new insights are required for a better design of HCK catalysts. We choose the hydrocracking of phenanthrene as a model reaction in order to compare several mesoporous and microporous acid solids. Characterization of the acidity of the solids reveals that there is no direct correlation between the HCK selectivity and the solids acidity. Moreover, combining the results of catalytic tests and force-field simulations, we are able to show that diffusional limitations can be ruled out and that the key phenomenon adversely affecting the selectivity is a too strong adsorption of isomerized products which favors overcracking. Below a steric exclusion threshold, pore size controls energies by virtue of confinement effects. Optimal solid acid HCK catalysts should therefore be designed by taking those effects into account. (C) 2003 Elsevier Science (USA). All rights reserved.
引用
收藏
页码:376 / 387
页数:12
相关论文
共 36 条
[1]  
Allen M. P., 1989, COMPUTER SIMULATION
[2]   CONFORMATIONAL ANALYSIS .70. PERHYDROPHENANTHRENES [J].
ALLINGER, NL ;
GORDEN, BJ ;
TYMINSKI, IJ ;
WUESTHOF.MT .
JOURNAL OF ORGANIC CHEMISTRY, 1971, 36 (06) :739-&
[3]   Hydroisomerization and hydrocracking of alkanes - Influence of the balance between acid and hydrogenating functions on the transformation of n-decane on PtHY catalysts [J].
Alvarez, F ;
Ribeiro, FR ;
Perot, G ;
Thomazeau, C ;
Guisnet, M .
JOURNAL OF CATALYSIS, 1996, 162 (02) :179-189
[5]   A NEW FAMILY OF MESOPOROUS MOLECULAR-SIEVES PREPARED WITH LIQUID-CRYSTAL TEMPLATES [J].
BECK, JS ;
VARTULI, JC ;
ROTH, WJ ;
LEONOWICZ, ME ;
KRESGE, CT ;
SCHMITT, KD ;
CHU, CTW ;
OLSON, DH ;
SHEPPARD, EW ;
MCCULLEN, SB ;
HIGGINS, JB ;
SCHLENKER, JL .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1992, 114 (27) :10834-10843
[6]   Mild hydrocracking of vacuum gasoil over NiMo-Beta zeolite catalysts: The role of the location of the NiMo phases and the crystallite size of the zeolite [J].
Camblor, MA ;
Corma, A ;
Martinez, A ;
Martinez-Soria, V ;
Valencia, S .
JOURNAL OF CATALYSIS, 1998, 179 (02) :537-547
[7]   CHARACTERIZATION OF ACID SURFACES BY ADSORPTION OF 2,6-DIMETHYLPYRIDINE [J].
CORMA, A ;
RODELLAS, C ;
FORNES, V .
JOURNAL OF CATALYSIS, 1984, 88 (02) :374-381
[8]   Catalytic performance of the new delaminated ITQ-2 zeolite for mild hydrocracking and aromatic hydrogenation processes [J].
Corma, A ;
Martínez, A ;
Martínez-Soria, V .
JOURNAL OF CATALYSIS, 2001, 200 (02) :259-269
[9]   Cracking behavior of zeolites with connected 12- and 10-member ring channels: The influence of pore structure on product distribution [J].
Corma, A ;
Davis, M ;
Fornes, V ;
GonzalezAlfaro, V ;
Lobo, R ;
Orchilles, AV .
JOURNAL OF CATALYSIS, 1997, 167 (02) :438-446
[10]   Zeolites as solid solvents [J].
Derouane, EG .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 1998, 134 (1-3) :29-45