Model based control of a liquid swelling constrained batch reactor subject to recipe uncertainties
This work presents the application of nonlinear model predictive control (NMPC) to a simulated industrial batch reactor subject to safety constraint due to reactor level swelling, which can occur with relatively fast dynamics. Uncertainties in the implementation of recipes in batch process operation...
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Published in | Chemical engineering journal (Lausanne, Switzerland : 1996) Vol. 153; no. 1; pp. 151 - 158 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Oxford
Elsevier B.V
01.11.2009
Elsevier |
Subjects | |
Online Access | Get full text |
ISSN | 1385-8947 1873-3212 1873-3212 |
DOI | 10.1016/j.cej.2009.06.003 |
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Abstract | This work presents the application of nonlinear model predictive control (NMPC) to a simulated industrial batch reactor subject to safety constraint due to reactor level swelling, which can occur with relatively fast dynamics. Uncertainties in the implementation of recipes in batch process operation are of significant industrial relevance. The paper describes a novel control-relevant formulation of the excessive liquid rise problem for a two-phase batch reactor subject to recipe uncertainties. The control simulations are carried out using a dedicated NMPC and optimization software toolbox
OptCon which implements efficient numerical algorithms. The open-loop optimal control problem is computed using the multiple-shooting technique and the arising nonlinear programming problem is solved using a sequential quadratic programming (SQP) algorithm tailored for large-scale problems, based on the freeware optimization environment HQP. The fast response of the NMPC controller is guaranteed by the initial value embedding and real-time iteration technologies. It is concluded that the
OptCon implementation allows small sampling times and the controller is able to maintain safe and optimal operation conditions, with good control performance despite significant uncertainties in the implementation of the batch recipe. |
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AbstractList | This work presents the application of nonlinear model predictive control (NMPC) to a simulated industrial batch reactor subject to safety constraint due to reactor level swelling, which can occur with relatively fast dynamics. Uncertainties in the implementation of recipes in batch process operation are of significant industrial relevance. The paper describes a novel control-relevant formulation of the excessive liquid rise problem for a two-phase batch reactor subject to recipe uncertainties. The control simulations are carried out using a dedicated NMPC and optimization software toolbox OptCon which implements efficient numerical algorithms. The open-loop optimal control problem is computed using the multiple- shooting technique and the arising nonlinear programming problem is solved using a sequential quadratic programming (SQP) algorithm tailored for large-scale problems, based on the freeware optimization environment HQP. The fast response of the NMPC controller is guaranteed by the initial value embedding and real-time iteration technologies. It is concluded that the OptCon implementation allows small sampling times and the controller is able to maintain safe and optimal operation conditions, with good control performance despite significant uncertainties in the implementation of the batch recipe. This work presents the application of nonlinear model predictive control (NMPC) to a simulated industrial batch reactor subject to safety constraint due to reactor level swelling, which can occur with relatively fast dynamics. Uncertainties in the implementation of recipes in batch process operation are of significant industrial relevance. The paper describes a novel control-relevant formulation of the excessive liquid rise problem for a two-phase batch reactor subject to recipe uncertainties. The control simulations are carried out using a dedicated NMPC and optimization software toolbox OptCon which implements efficient numerical algorithms. The open-loop optimal control problem is computed using the multiple-shooting technique and the arising nonlinear programming problem is solved using a sequential quadratic programming (SQP) algorithm tailored for large-scale problems, based on the freeware optimization environment HQP. The fast response of the NMPC controller is guaranteed by the initial value embedding and real-time iteration technologies. It is concluded that the OptCon implementation allows small sampling times and the controller is able to maintain safe and optimal operation conditions, with good control performance despite significant uncertainties in the implementation of the batch recipe. |
Author | Simon, Levente L. Nagy, Zoltan K. Hungerbuhler, Konrad |
Author_xml | – sequence: 1 givenname: Levente L. surname: Simon fullname: Simon, Levente L. email: levente.simon@chem.ethz.ch organization: ETH Zurich, Institute of Chemical and Bioengineering, W. Pauli str. 10, Zurich, Switzerland – sequence: 2 givenname: Zoltan K. surname: Nagy fullname: Nagy, Zoltan K. organization: Loughborough University, Chemical Engineering Department, Loughborough LE11 3TU, United Kingdom – sequence: 3 givenname: Konrad surname: Hungerbuhler fullname: Hungerbuhler, Konrad organization: ETH Zurich, Institute of Chemical and Bioengineering, W. Pauli str. 10, Zurich, Switzerland |
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Keywords | Dynamic simulation Multiphase reactors Multiphase flow Batch Process control Optimization Uncertainty Samplings Modeling Batchwise Safety Sampling Dynamic model Reactor Mathematical programming Predictive control Swelling Quadratic programming Real time Algorithm Real time system Optimal control Non linear model Open loop Software |
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SubjectTerms | Applications of mathematics to chemical engineering. Modeling. Simulation. Optimization Applied sciences Batch Chemical engineering Dynamic simulation Exact sciences and technology Hydrodynamics of contact apparatus Multiphase flow Multiphase reactors Optimization Process control Reactors Safety |
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Title | Model based control of a liquid swelling constrained batch reactor subject to recipe uncertainties |
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