Title of article
Modeling of a Three-Phase Industrial Batch Reactor Using a Hybrid First-Principles Neural-Network Model
Author/Authors
Fischer، Ulrich نويسنده , , Hungerbuhler، Konrad نويسنده , , Simon، Levente L. نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2006
Pages
-7335
From page
7336
To page
0
Abstract
We present an industrial case study of a three-phase reaction system in a batch reactor. For the successful modeling and prediction of the plant-scale performance, a hybrid model is used. Data from different scales were available for developing and testing the model. Laboratory data from a 1 kg vessel were used for the determination of the parameters related to reaction kinetics. Here, a first-principle approach is applied for modeling reactions and dissolution of one reactant that is introduced into the reactor in solid form. To model the large-scale production process, this model was extended with neural-network models to identify the missing parameters. In addition, a refitting of the kinetic parameters on the plant scale was required. With this hybrid model, a good prediction of the concentration courses in the industrial reactor was obtained and improved operating conditions were identified. This paper discusses the potentials and limitations of applying hybrid models in complex processes in the chemical industry.
Keywords
Secular term , Non-linearity , Perturbation method , Tidal water table fluctuation
Journal title
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Serial Year
2006
Journal title
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Record number
109995
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