N. Bhatt, M. Amrhein and D. Bonvin
Completed project (2005-2011)
This project investigated and developed appropriate tools that facilitate the analysis of homogeneous and gas-liquid reaction systems. The main contribution was a novel procedure for computing the extents of reaction and the extents of mass transfer for reaction systems with inlet and outlet streams.
Extents of Reaction, Mass Transfer and Flow
For open homogeneous reaction systems, this project proposed a linear transformation of the number of moles vector into four distinct parts, namely, the extents of reaction, the extents of inlet, the extent of outlet and the invariants, using only the stoichiometry, the inlet composition and the initial conditions.
For open gas-liquid reaction systems and using only the stoichiometry, the inlet composition, the initial conditions, and the knowledge of the species transferring between phases, a linear transformation of the numbers of moles in the liquid into ﬁve distinct parts was proposed, namely, the extents of reaction, the extents of mass transfer, the extents of liquid inlet, the extent of liquid outlet and the invariants. Similarly, a transformation of the numbers of moles in the gas phase into four distinct parts was proposed to generate the extents of mass transfer, the extents of gas inlet, the extent of gas outlet and the invariants.
Minimal State Representation and State Reconstruction
The conditions under which the transformed models are minimal state representations have been derived for homogeneous and gas-liquid reaction systems. Furthermore, using the measured ﬂow rates and the proposed transformations, it was shown how to reconstruct unmeasured concentrations without knowledge of the reaction and mass-transfer rate expressions. It was also shown that the minimal number of measured concentrations equals the number of independent reactions for homogeneous reactors or the number of reactions plus the number of transferring species for gas-liquid reactors.
The incremental identiﬁcation proceeds in two steps: (i) computation of the extents of reaction and mass transfer from measured data, and (ii) estimation of the parameters of the individual reaction and mass-transfer rates from the computed extents. In the ﬁrst step, the linear transformation is applied to compute the extents of reaction, mass transfer and ﬂow directly from measured data without knowledge of the reaction and mass-transfer rate expressions. An approach was also developed for the case where concentrations are only available for a subset of the reacting species. In the second step, the unknown rates are identiﬁed individually for each reaction or each mass transfer from the corresponding individual extent using the integral method.
Incremental identification; Transport phenomena; Extents of reaction; Extents of mass transfer; Extents of inlet/outlet flow; Linear transformations; Model reduction; Minimal state representation; Homogeneous reactors; Gas-liquid reactors.
Minimal State Representation for Open Fluid-Fluid Reaction Systems
2012. 2012 American Control Conference (ACC) , Montreal, Canada , June 27 - 29, 2012. p. 3496-3502.
Incremental Identification of Reaction Systems - A Comparison between Rate-based and Extent-based Approaches
Chemical Engineering Science. 2012.
DOI : 10.1016/j.ces.2012.05.040.
Extents of Reaction and Mass Transfer in the Analysis of Chemical Reaction Systems
Lausanne, EPFL, 2011.
DOI : 10.5075/epfl-thesis-5028.
Incremental Identification of Reaction and Mass-Transfer Kinetics Using the Concept of Extents
Industrial & Engineering Chemistry Research. 2011.
DOI : 10.1021/ie2007196.
Incremental Identification of Reaction and Mass-Transfer Rates In Gas-Liquid Reaction Systems Using Tendency Modeling
2011 AIChE Annual Meeting, Minneapolis, MN, USA, October 16-21, 2011.
Incremental model identification for homogeneous systems – A comparison
7th In.t Workshop on Mathematics in Chemical Kinetics and Engineering 2011, University of Heidelberg, Wednesday May 18th - Friday May 20th 2011.
Extents of Reaction, Mass Transfer and Flow for Gas-Liquid Reaction Systems
Industrial Engineering & Chemistry Research. 2010.
DOI : 10.1021/ie902015t.
Extents of reaction and flow for homogeneous reaction systems with inlet and outlet streams
AIChE Journal. 2010.
DOI : 10.1002/aic.12125.
Identification of reaction and mass-transfer rates in gas-liquid reaction systems
2010. International Symposium on "Thermodynamics and Transport processes", Recent and Emergent Advances in Chemical Engineering , IIT-Madras, Chennai, India , December 2-4, 2010. p. 70-75.
Minimal state representation of homogeneous reaction systems
2010. ESCAPE-20: European Symposium on Computer Aided Process Engineering , Ischia, Naples, Italy , 6-9 June 2010.