Dynamics of a three-phase upflow fixed-bed catalytic reactor

被引：12

作者：

Julcour, C ^{[1
]}

Stüber, F ^{[1
]}

Le Lann, JM ^{[1
]}

Wilhelm, AM ^{[1
]}

Delmas, H ^{[1
]}

机构：

[1] INPT, ENSIGC, CNRS, Lab Genie Chim, F-31078 Toulouse, France

来源：

CHEMICAL ENGINEERING SCIENCE | 1999年 / 54卷 / 13-14期

关键词：

fixed-bed reactor; cocurrent upflow; dynamic modeling;

D O I：

10.1016/S0009-2509(98)00304-2

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A dynamic model of an upflow fixed-bed catalytic reactor :is developed to examine numerically transient axial temperature and concentration profiles obtained for the consecutive hydrogenation of 1,5,9-cyclododecatriene on a Pd/Al2O3 catalyst, This non-isothermal heterogeneous model includes the resistances to heat and mass transfer at the gas-liquid and liquid-solid interfaces, as well as the heat exchange through the jacket of the reactor. The predictions of the model are compared to experimental data for various gas and liquid flow rates to describe dynamic events, such as the start-up of the reactor and the effects of sudden changes in the operating conditions on the reactor behaviour and its thermal stability. The predicted transient profiles are in good agreement with the experimental measurements. Still, the dynamic model is not able to correctly predict hot spots and runways experimentally observed at very high hydrogen flow rates. (C) 1999 Elsevier Science Ltd. All rights reserved.

引用

页码：2391 / 2400

页数：10