Monday, October 17, 2011: 1:25 PM
Marquette IV (Hilton Minneapolis)
Oliver Litzmann1, Thomas Grützner
2, Günter Wozny
1 and Jens-Uwe Repke
3, (1)Chair of Process Dynamics and Operation, Berlin Institute of Technology, Berlin, Germany, (2)Lcdrn, Lonza AG, Visp, Switzerland, (3)Institut für Thermische Verfahrenstechnik, Umwelt- und Naturstoffverfahrenstechnik, TU Bergakademie Freiberg, Freiberg, Germany
Design of reactive distillation column for
non-parameterized components - which experiments are essential
Litzmann, O., TU Berlin, Berlin; Lorenz, H.-M., TU Berlin, Berlin; Wozny, G., TU Berlin, Berlin; Grützner,
T., Lonza AG, Visp/CH; Repke, J.-U., TU Freiberg, Freiberg
Designing reactive distillation processes
requires a great number of fitted parameters depending on the model used. These
parameters are known for test-systems like MTBE or TAME but not for systems
which have never before used in reactive distillation. As fitting of parameters
require a lot of time and money for trials it is crucial to know the impact of
an improved model to the prediction accuracy. If this is known it is possible
to carry out fewer experiments with and fit a set of sufficient parameters in
order to describe the RD process as good as needed to strive
the goal.
Application to a new industrial substance
system
The system analysed consists of an organic acid, an
alcohol, the corresponding ester and water whereupon some components cannot be
described by standard UNIFAC methods. The esterfication
takes place in a reactive distillation column designed for this system. The reaction
is catalysed by the heterogeneous catalyst Amberlyst 36. In order to describe the results of the
column, models are used which take different phenomena into account and use
different sets of parameters which have been measured independently.
Fig. SEQ Fig. \* ARABIC 1: Comparison of the composition forecast by pseudo homogeneous and adsorption based model |
For instance the reaction can be described either by
equilibrium or by kinetics – which can be corrected by adsorption effects in addition.
This kinetic have been measured in a batch reactor and is described with significant
higher accuracy by an adsorption based kinetic model (see Fig.1) The
portability of these model improvement and similar effects to the reactive
column simulation will be presented and discussed by means of comparison with
the experimental results from the lab scale plant.
Extended Abstract: File Not Uploaded