Influence of feed components on the activity and stability of cobalt molybdenum alumina metathesis catalyst

被引:16
作者
Kwini, MN [1 ]
Botha, JM [1 ]
机构
[1] Sasol Technol Res & Dev, ZA-1947 Sasolburg, South Africa
关键词
metathesis; deactivation; feed components; cobalt molybdenum alumina catalyst;
D O I
10.1016/j.apcata.2004.10.043
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
Alkene metathesis plays a vital role industrially in the upgrading of low value alkenes to higher value alkenes such as linear internal alkenes in the C-10-C-18 range. These in turn find application as feedstock for manufacturing of surfactants and detergents. Industrial alkene cuts contain component(s) that might be detrimental to the catalyst active sites during the metathesis reaction leading to catalyst deactivation. The focus of this study was to investigate the effect of some of the components present in typical low value feed streams on the activity and stability of a CoO/MoO3/Al2O3 catalyst. The results indicated that the feed composition does have a major influence on the metathesis reactivity of the catalyst. Pure 1-octene (98%), which was used as a reference feed was spiked with various components that had a concentration of 100 ppm. Results revealed a trend in terms of the severity of the component that deactivated the catalyst to be water > methylcyclopentadiene dimer > methylcyclopentane > toluene > 2-pentanone > 2-methyl-1,5-hexadiene > 2-methyl-1-hexene > butanol. A study was also undertaken to examine whether the component (methylcyclopentadiene dimer as an example) that deactivates the catalyst is a temporary or permanent poison. Results showed that methylcyclopentadiene dimer is a temporary poison. The carbonaceous deposits (oligomers) formed during the reaction seem to be the primary cause of catalyst deactivation. However, the catalyst deactivation mechanism in the presence of water in I-octene feed is mostly linked to the molecular structural change of the catalyst rather than accumulation of carbonaceous deposits on the surface of the catalyst. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:199 / 208
页数:10
相关论文
共 17 条
[1]   METHATHESIS OF ETHYLENE BUTENE MIXTURES TO PROPYLENE WITH RHENIUM ON ALUMINA CATALYSTS [J].
AMIGUES, P ;
CHAUVIN, Y ;
COMMEREUC, D ;
HONG, CT ;
LAI, CC ;
LIU, YH .
JOURNAL OF MOLECULAR CATALYSIS, 1991, 65 (1-2) :39-50
[2]  
[Anonymous], 1985, ADV ORG CHEM
[3]  
Banks R.L., 1984, APPL IND CATALYSIS, V3, P215
[4]   INDUSTRIAL-ASPECTS OF THE DISPROPORTIONATION REACTION [J].
BANKS, RL .
JOURNAL OF MOLECULAR CATALYSIS, 1980, 8 (1-3) :269-276
[5]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[6]   Reaction and deactivation study of mesoporous silica-alumina (MSA) in propene oligomerisation [J].
Flego, C ;
Peratello, S ;
Perego, C ;
Sabatino, LMF ;
Bellussi, G ;
Romano, U .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2003, 204 :581-589
[7]  
McMurry J., 1988, ORGANIC CHEM
[8]   Olefin metathesis over supported rhenium oxide catalysts [J].
Mol, JC .
CATALYSIS TODAY, 1999, 51 (02) :289-299
[9]   Catalyst deactivation: is it predictable? What to do? [J].
Moulijn, JA ;
van Diepen, AE ;
Kapteijn, F .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :3-16
[10]  
PEARCE R, 1981, CARBON CARBON BOND F, V2, P194