Mass transfer effects during homogeneous 1-octene hydroformylation in CO2-expanded solvent:: Modeling and experiments

被引:14
|
作者
Guha, Debangshu
Jin, Hong
Dudukovic, M. P.
Ramachandran, P. A.
Subramaniam, Bala [1 ]
机构
[1] Univ Kansas, Dept Chem & Petr Engn, Lawrence, KS 66045 USA
[2] Washington Univ, Chem React Engn Lab, St Louis, MO 63130 USA
基金
美国国家科学基金会;
关键词
CO2-expanded liquids; hydroformylation; batch reactor model;
D O I
10.1016/j.ces.2006.12.029
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CO2-expanded liquids (CXLs) represent a continuum of reaction media that combine the reaction benefits provided by organic solvents and the environmental benefits provided by supercritical CO2 (scCO(2)) in an optimal manner. Homogeneous hydroformylation of I-octene using an unmodified rhodium catalyst (Rh(acac)(CO)2) was successfully demonstrated employing CXLs as reaction media [Jin, H., Subramaniam, B., 2004. Homogeneous catalytic hydroformylation of I-octene in CO2-expanded solvent media. Chemical Engineering Science 59, 4887-4893]. The reported experimental study, however, showed a long induction period of nearly 2h, following which reaction occurs. A detailed reactor model incorporating reaction kinetics, mass transfer rates and phase equilibrium is presented to systematically investigate the effects of mass transfer and catalyst activation on induction period in I-octene hydroformylation in CXL. Complementary experiments performed in stirred autoclave reactors equipped with an in situ ReactIR probe validate the cause of the induction period predicted by the model. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4967 / 4975
页数:9
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