CFD modeling on external mass transfer and intra-particle diffusional effects on the supercritical hydrogenation of sunflower oil

被引:10
|
作者
Guardo, A. [1 ]
Casanovas, M. [1 ]
Ramirez, E. [1 ]
Recasens, F. [1 ]
Magana, I. [1 ]
Martinez, D. [1 ]
Larrayoz, M. A. [1 ]
机构
[1] Univ Politecn Catalunya, Dept Chem Engn, ETS Engn Ind Barcelona, E-08028 Barcelona, Spain
关键词
chemical reactors; computational fluid dynamics; hydrogenation; mass transfer; reaction engineering; supercritical fluids;
D O I
10.1016/j.ces.2007.01.080
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Computational fluid dynamics (CFD) is applied to the study of the catalytic hydrogenation of sunflower oil in the presence of a supercritical solvent. A 2D CFD model of a single Pd-based catalyst pellet is presented. Intra-particle concentration profiles for all species present in the mixture (oil fatty acids and hydrogen) are obtained and compared against experimental results. Different particle sizes are studied and external mass transfer and intra-particle diffusional effects are analyzed. External mass transfer coefficients are obtained and presented. Fitting of the intra-particle concentration profiles allowed to verify the kinetic reaction model. The verified kinetic reaction model and intra-particle diffusion coefficients were utilized in a 3D packed bed reactor model, and conversion profiles are obtained. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5054 / 5061
页数:8
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