CATALYTIC AND STRUCTURAL-PROPERTIES OF RUTHENIUM BIMETALLIC CATALYSTS - KINETICS OF 2,2,3,3-TETRAMETHYLBUTANE HYDROGENOLYSIS

被引:21
作者
COQ, B
CRABB, E
FIGUERAS, F
机构
[1] Laboratoire de Chimie Organique Physique et Cinétique Chimique Appliquées, 34053 Montpellier, 8, rue de l'Ecole Normale
关键词
BIMETALLIC CATALYSTS; HYDROGENOLYSIS; KINETICS; RUTHENIUM; SUPPORTED CATALYSTS; TETRAMETHYLBUTANE;
D O I
10.1016/1381-1169(94)00028-X
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
The kinetics of 2,2,3,3-tetramethylbutane (TeMB) hydrogenolysis has been investigated over alumina-supported mono- and bimetallic ruthenium catalysts. The bimetallic catalysts were prepared from the monometallic ones by controlled surface modification with Sn, Pb and Ge organometallics. As reported earlier, large Ru particles (> 3 nm) favour the cleavage between the two quaternary carbon atoms leading to isobutane (alpha delta process); moreover, deep hydrogenolysis of the adsorbed alkyl fragments occurs before desorption. At the opposite, on small Ru particles (approximate to 1 nm) demethylation to 2,2,3-trimethylbutane is the main reaction (alpha gamma process) and deep hydrogenolysis is suppressed. The addition of Sn or Pb onto small Ru particles has only a small effect on the reaction rate but shifts the selectivity pattern towards that of large Ru particles, while the selectivity remains unchanged upon Ge addition, The addition of either Sn or Ge to large Ru particles decreases the rate by two orders of magnitude. With respect to the rate, hydrogen has a stronger inhibiting effect on the sample of lower dispersion. Both rates for alpha gamma and alpha delta processes go through a maximum as a function of hydrogen pressure, the maximun for the alpha delta process being shifted to higher H-2 pressures. Assuming (i) Langmuir adsorption isotherms, (ii) multisite competitive adsorption between hydrogen and TeMB, (iii) hydrogenation of the dehydrogenated adsorbed alkane (most abundant surface intermediate, MASI) by a surface hydrogen atom as the rate determining step, a rate law was proposed for both alpha gamma and alpha delta processes. The kinetic analysis suggests that highly dehydrogenated intermediates (alpha delta process, -5H) are formed on large Ru particles. These species need a large ensemble of Ru atoms to be formed. At variance, on small Ru particles hydrogenolysis could proceed through less dehydrogenated adsorbed species: metallacyclobutane for the alpha gamma process (-2H) and metallacyclopentane for the alpha delta process (-3H), the formation of the latter being inhibited at high H-2 pressure. These metallacycles can be formed on small ensembles of Ru atoms. The addition of Sn or Ge to small Ru particles does not change very much the positions of the rate maxima for alpha gamma and alpha delta processes, or the hydrogen dependence of the rate. It emerges that the main effect of Sn and Ge addition is to decrease the number of sites active for alpha gamma and alpha delta processes respectively, the former being the sites of low coordination, the latter the sites of high coordination.
引用
收藏
页码:35 / 48
页数:14
相关论文
共 25 条
[1]   STUDIES ON RUTHENIUM CATALYSTS .4. HYDROGENOLYSIS OF N-BUTANE ON RU/AL2O3 CATALYST-DEPENDENCE OF REACTION-KINETICS ON PARTICLE-SIZE AND ON PRETREATMENT [J].
BOND, GC ;
SLAA, JC .
JOURNAL OF MOLECULAR CATALYSIS, 1994, 89 (1-2) :221-228
[2]   SOURCE OF THE ACTIVATION-ENERGY IN HETEROGENEOUSLY CATALYZED-REACTIONS [J].
BOND, GC .
CATALYSIS TODAY, 1993, 17 (03) :399-410
[3]  
BOND GC, UNPUB J MOL CATAL
[4]   REACTIONS OF HYDROCARBONS OVER RU/SIO2 - EXCHANGE WITH DEUTERIUM AND THE ONSET OF HYDROGENOLYSIS [J].
BROWN, R ;
KEMBALL, C .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1993, 89 (03) :585-594
[5]  
BROWN R, 1988, 9TH P INT C CAT, V3, P1013
[6]  
BURTON JJ, 1975, J CATAL, V37, P106, DOI 10.1016/0021-9517(75)90138-4
[7]   SURFACE-REACTIONS OF HYDROCARBONS AS A PROBE FOR THE CHARACTERIZATION OF RHCU/SIO2 CATALYSTS [J].
COQ, B ;
DUTARTRE, R ;
FIGUERAS, F ;
ROUCO, A .
JOURNAL OF PHYSICAL CHEMISTRY, 1989, 93 (12) :4904-4908
[8]   CATALYTIC PROPERTIES OF WELL DISPERSED SUPPORTED RUTHENIUM ALLOYS [J].
COQ, B ;
BITTAR, A ;
DUTARTRE, R ;
FIGUERAS, F .
JOURNAL OF CATALYSIS, 1991, 128 (01) :275-286
[9]   ALKANE CONVERSION AND TOPOLOGICAL SEGREGATION IN PTM/AL2O3 CATALYSTS [J].
COQ, B ;
CHAQROUNE, A ;
FIGUERAS, F ;
NCIRI, B .
APPLIED CATALYSIS A-GENERAL, 1992, 82 (02) :231-245
[10]   CATALYTIC AND STRUCTURAL-PROPERTIES OF RUTHENIUM BIMETALLIC CATALYSTS - PREPARATION AND CHARACTERIZATION [J].
COQ, B ;
CRABB, E ;
WARAWDEKAR, M ;
BOND, GC ;
SLAA, JC ;
GALVAGNO, S ;
MERCADANTE, L ;
RUIZ, JG ;
SIERRA, MCS .
JOURNAL OF MOLECULAR CATALYSIS, 1994, 92 (01) :107-121