HYDROGENATION OF BENZENE ON A PT/AL2O3 BLOCK CATALYST WITH A HONEYCOMB STRUCTURE

被引:0
|
作者
OSTROVSKII, NM
PARMALIANA, A
FRUSTERI, F
MASLOVA, LP
GIORDANO, N
机构
[1] UNIV MESSINA,INST CHIM IND,I-98100 MESSINA,ITALY
[2] IST TAE CNR,MESSINA,ITALY
关键词
D O I
暂无
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 reaction kinetics in a gradient-free flow-type circulating reactor and in an integral reactor with a single block were investigated. The kinetic model was substantiated and the condition for the existence of a reaction rate maximum as a function of the temperature was obtained. The possibility of conducting the process in a multilayer adiabatic reactor was evaluated.
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页码:67 / 73
页数:7
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