Process Systems Engineering
Exponential observers for distributed tubular (bio)reactors
Article first published online: 7 OCT 2008
DOI: 10.1002/aic.11571
Copyright © 2008 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
García, M. R., Vilas, C., Banga, J. R. and Alonso, A. A. (2008), Exponential observers for distributed tubular (bio)reactors. AIChE Journal, 54: 2943–2956. doi: 10.1002/aic.11571
Publication History
- Issue published online: 17 OCT 2008
- Article first published online: 7 OCT 2008
- Manuscript Revised: 16 MAY 2008
- Manuscript Received: 2 JUL 2007
Funded by
- Bulgarian Academy of Sciences and Process Engineering Group IIM-CSIC
- Spanish Government. Grant Numbers: PPQ2001-3643, DPI2004-07444-C04-03
- Xunta de Galicia. Grant Number: PGIDIT02-PXIC40209PN
- Abstract
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Keywords:
- observer;
- distributed process systems;
- tubular (bio)reactors;
- optimal sensor location
Abstract
The dissipative nature of spatially distributed process systems is exploited to develop efficient exponential state observers based on a low-dimensional dynamic representation of the original set of partial differential equations. The suggested approach combines standard observer design techniques for reactors, where the reaction rates are unknown with efficient model reduction methodologies based on projection of the original concentration and temperature fields on low-dimensional subspaces capturing the slow dynamics of the process. The global exponential stability of the resulting observer is derived combining classical Lyapunov analysis with a transformation that allows us to obtain a diffusion system from a diffusion-convection system. In addition, aspects related to the location of sensors and their influence on the ability to reconstruct the necessary fields to feed the observer will also be considered. © 2008 American Institute of Chemical Engineers AIChE J, 2008

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