Safe operation of stirred-tank semibatch reactors subject to risk of thermal hazard

被引:10
|
作者
Mas, E. [1 ]
Bosch, C. M. [1 ]
Recasens, F. [1 ]
Velo, E. [1 ]
机构
[1] Univ Politecn Catalunya, ETS Engn Ind Barcelona, E-08028 Barcelona, Spain
关键词
semibatch chemical reactors; exothermic reaction simulation; reaction engineering; thermal safety; scale-up;
D O I
10.1002/aic.10975
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, the behavior of exothermic chemical reactions conducted in a wall-cooled, semibatch stirred-tank reactor is studied, with particular attention to conditions that lead to a thermal accident. The dimensionless heat and mass conservation equations for a semicontinuous tank were solved using second-order irreversible kinetics and a number of selected dimensionless numbers, for both the feed period and the late batch stage. The criterion implemented is based on the nonaccumulation of the dosed reactant, and the safest operating mode is based on the values of the reactor parameters that lead to an instantaneous consumption of the dosed feed. The criterion is implemented into an algorithm that runs in parallel with the integration of the model equations. Its applicability is shown using a few examples that show that the computer implementation of our methods works well in hazard prediction. (c) 2006 American Institute of Chemical Engineers.
引用
收藏
页码:3570 / 3582
页数:13
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