Supported aqueous phase catalysis:: a new kinetic model of hydroformylation of octene in a gas-liquid-liquid-solid system

被引:15
作者
Jáuregui-Haza, UJ
Pardillo-Fontdevila, E
Kalck, P
Wilhelm, AM
Delmas, H
机构
[1] Ctr Quim Farmaceut, Havana, Cuba
[2] Ecole Natl Super Ingn Arts Chim & Technol, F-31077 Toulouse, France
关键词
hydroformylation; gas-liquid-liquid-solid system; supported aqueous phase catalysis;
D O I
10.1016/S0920-5861(03)00072-5
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The kinetics of the [Rh-2(mu-(SBu)-Bu-t)(2)(CO)(2)(TPPTS)(2)] catalyzed hydroformylation of I-octene by supported aqueous phase catalysis has been investigated under mild conditions (0.5-1 MPa, 353-373 K). The effect of 1-octene and catalyst concentration and partial pressure of hydrogen and carbon monoxide on the rate of reaction has been studied. The rate was found to be first-order with respect to catalyst concentration and partial order with respect to partial pressure of hydrogen. However, when partial pressure of carbon monoxide and 1-octene concentration increased, the rate showed a typical case of substrate-inhibited kinetics. A rate equation has been proposed, considering that each particle of supported aqueous phase catalyst is a microreactor, where the reaction takes place at the aqueous/organic interface. The kinetic model showed the good agreement with the experimental data, being the average relative error of estimation less than 7%. The kinetic parameters have been evaluated for different temperatures. The activation energy was found to be 71 kJ/mol. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:409 / 417
页数:9
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