This work presents a modeling and control study of a reactive distillation column
used for hydrogenation of benzene. A steady state and a dynamic model have been
developed to investigate control structures for the column. The most important aspects of
this control problem are that the purity of the product streams regarding benzene need to
be met. At the same time as little toluene as possible should be converted. The former is a
constraint imposed by EPA regulations while the latter is tied to process economics due
to the high octane number of toluene. It is required to satisfy both of these objectives
even under the influence of disturbances, as the feed composition changes on a regular
basis. The dynamic model is used for developing transfer function models of two
potential control structures. Pairing of inputs and outputs is performed based upon the
Relative Gain Array (RGA) and PI controllers were designed for each control structure.
The controller performance was then compared in simulation studies. From our results,
control structure 2 performed better than control structure 1. The main advantage of CS2
over CS1 is noticed in the simulation of feed composition disturbance rejection, where
CS2 returns all variables back to steady state within 3 hrs while it take CS1 more than 20
hrs to return the temperature variables back to steady state.
| Identifer | oai:union.ndltd.org:tamu.edu/oai:repository.tamu.edu:1969.1/ETD-TAMU-2008-08-27 |
| Date | 16 January 2010 |
| Creators | Aluko, Obanifemi |
| Contributors | Hahn, Juergen |
| Source Sets | Texas A and M University |
| Language | en_US |
| Detected Language | English |
| Type | Book, Thesis, Electronic Dissertation |
| Format | application/pdf |
Page generated in 0.002 seconds