Université de Lyon- CNRS-LAGEP, France Paper CCC07-0506 Model Predictive Control of a Powder Coating Curing Process: an Application.

Slides:



Advertisements
Similar presentations
What is UV curing system ?
Advertisements

ECG Signal processing (2)
Hongjie Zhang Purge gas flow impact on tritium permeation Integrated simulation on tritium permeation in the solid breeder unit FNST, August 18-20, 2009.
A.M. Alonso, C. García-Martos, J. Rodríguez, M. J. Sánchez Seasonal dynamic factor model and bootstrap inference: Application to electricity market forecasting.
Optimization of thermal processes2007/2008 Optimization of thermal processes Maciej Marek Czestochowa University of Technology Institute of Thermal Machinery.
U D A Neural Network Approach for Diagnosis in a Continuous Pulp Digester Pascal Dufour, Sharad Bhartiya, Prasad S. Dhurjati, Francis J. Doyle III Department.
Acoustic design by simulated annealing algorithm
1 1 Alternative Risk Measures for Alternative Investments Alternative Risk Measures for Alternative Investments Evry April 2004 A. Chabaane BNP Paribas.
Université de Lyon- CNRS-LAGEP, France Paper C-090 Model Predictive Control of the Primary Drying Stage of the Drying of Solutions.
1 Optimal input design for online identification : a coupled observer-MPC approach by: Saida Flila, Pascal Dufour, Hassan Hammouri 10/07/2008 IFAC’08,
PROCESS INTEGRATED DESIGN WITHIN A MODEL PREDICTIVE CONTROL FRAMEWORK Mario Francisco, Pastora Vega, Omar Pérez University of Salamanca – Spain University.
Module F: Simulation. Introduction What: Simulation Where: To duplicate the features, appearance, and characteristics of a real system Why: To estimate.
Support Vector Machines (SVMs) Chapter 5 (Duda et al.)
280 SYSTEM IDENTIFICATION The System Identification Problem is to estimate a model of a system based on input-output data. Basic Configuration continuous.
INTEGRATED DESIGN OF WASTEWATER TREATMENT PROCESSES USING MODEL PREDICTIVE CONTROL Mario Francisco, Pastora Vega University of Salamanca – Spain European.
A Comparative Study Of Deterministic And Stochastic Optimization Methods For Integrated Design Of Processes Mario Francisco a, Silvana Revollar b, Pastora.
16/12/ Texture alignment in simple shear Hans Mühlhaus,Frederic Dufour and Louis Moresi.
Chess Review May 11, 2005 Berkeley, CA Closing the loop around Sensor Networks Bruno Sinopoli Shankar Sastry Dept of Electrical Engineering, UC Berkeley.
1 Simulation Modeling and Analysis Verification and Validation.
November 21, 2005 Center for Hybrid and Embedded Software Systems Engine Hybrid Model A mean value model of the engine.
Lecture outline Support vector machines. Support Vector Machines Find a linear hyperplane (decision boundary) that will separate the data.
Overall Objectives of Model Predictive Control
1 Jordan University of Science and Technology Chemical Engineering Department “Modeling & Control of Continuous Fluidized Bed Dryers” BY MOHAMMAD AL-HAJ.
Introduction to API Process Simulation
Powder Coating Jason Fox Material Science Meen 3344.
Overview of Model Predictive Control in Buildings
Speaker: Xin Zuo Heterogeneous Computing Laboratory (HCL) School of Computer Science and Informatics University College Dublin Ireland International Parallel.
How do Scientists Think?
Chapter 10 Boosting May 6, Outline Adaboost Ensemble point-view of Boosting Boosting Trees Supervised Learning Methods.
1 Chapter 8 Nonlinear Programming with Constraints.
A Framework for Distributed Model Predictive Control
Outline 1-D regression Least-squares Regression Non-iterative Least-squares Regression Basis Functions Overfitting Validation 2.
Andrew Poje (1), Anne Molcard (2,3), Tamay Ö zg Ö kmen (4) 1 Dept of Mathematics, CSI-CUNY,USA 2 LSEET - Universite de Toulon et du Var, France 3 ISAC-CNR.
Machine Learning Using Support Vector Machines (Paper Review) Presented to: Prof. Dr. Mohamed Batouche Prepared By: Asma B. Al-Saleh Amani A. Al-Ajlan.
Technology The practical use of human knowledge to extend human abilities and to satisfy human needs and wan ts.
Huixian Liu and Shihua Li, Senior Member, IEEE
Multiple Model approach to Multi-Parametric Model Predictive Control of a Nonlinear Process a simulation case study Boštjan Pregelj, Samo Gerkšič Jožef.
Estimation of the derivatives of a digital function with a convergent bounded error Laurent Provot, Yan Gerard * 1 DGCI, April, 6 th 2011 * speaker.
Mathematical Models & Optimization?
Local Probabilistic Sensitivity Measure By M.J.Kallen March 16 th, 2001.
CONTROL ENGINEERING IN DRYING TECHNOLOGY FROM 1979 TO 2005: REVIEW AND TRENDS by: Pascal DUFOUR IDS’06, Budapest, 21-23/08/2006.
Interval Type-2 Fuzzy T-S Modeling For A Heat Exchange Process On CE117 Process Trainer Proceedings of 2011 International Conference on Modelling, Identification.
Kanpur Genetic Algorithms Laboratory IIT Kanpur 25, July 2006 (11:00 AM) Multi-Objective Dynamic Optimization using Evolutionary Algorithms by Udaya Bhaskara.
Structured H ∞ control of a continuous crystallizer L. Ravanbod, D. Noll, P. Apkarian Institut de Mathématiques de Toulouse IFAC Workshop on Control Distributed.
Chapter 20 1 Overall Objectives of Model Predictive Control 1.Prevent violations of input and output constraints. 2.Drive some output variables to their.
Intelligent controller design based on gain and phase margin specifications Daniel Czarkowski  and Tom O’Mahony* Advanced Control Group, Department of.
Distributed Models for Decision Support Jose Cuena & Sascha Ossowski Pesented by: Gal Moshitch & Rica Gonen.
Operations Research The OR Process. What is OR? It is a Process It assists Decision Makers It has a set of Tools It is applicable in many Situations.
1 Chapter 20 Model Predictive Control Model Predictive Control (MPC) – regulatory controls that use an explicit dynamic model of the response of process.
دانشگاه صنعتي اميركبير دانشكده مهندسي پزشكي استاد درس دكتر فرزاد توحيدخواه بهمن 1389 کنترل پيش بين-دکتر توحيدخواه MPC Stability-2.
IEEE Vehicle Power and propulsion conference, p.p. 1-4, Sept Control strategies for fuel cell based hybrid electric vehicles: From offline to online.
Dynamic Neural Network Control (DNNC): A Non-Conventional Neural Network Model Masoud Nikravesh EECS Department, CS Division BISC Program University of.
Nonlinear balanced model residualization via neural networks Juergen Hahn.
DoING Science: Science Process Skills Science is a process through which we learn about the world. We not only learn about science, we actually DO Science!
Introduction to Spin Coating and Derivation of a Simple Model
Chapter 20 Model Predictive Control (MPC) from Seborg, Edgar, Mellichamp, Process Dynamics and Control, 2nd Ed 1 rev. 2.1 of May 4, 2016.
SOFTWARE: A SOLUTION FOR MODEL PREDICTIVE CONTROL SOFTWARE: A SOLUTION FOR MODEL PREDICTIVE CONTROL Laboratoire.
Bounded Nonlinear Optimization to Fit a Model of Acoustic Foams
ENME 392 Regression Theory
Recent Advances in Iterative Parameter Estimation
Decomposed optimization-control problem
Thermoformable Conductive Ink:
On calibration of micro-crack model of thermally induced cracks through inverse analysis Dr Vladimir Buljak University of Belgrade, Faculty of Mechanical.
Overall Objectives of Model Predictive Control
Two-level strategy Vertical decomposition Optimal process operation
Laser Hardening of Grey Cast Iron using a High Power Diode Laser
Identification of Wiener models using support vector regression
Whitening-Rotation Based MIMO Channel Estimation
Masoud Nikravesh EECS Department, CS Division BISC Program
Presentation transcript:

Université de Lyon- CNRS-LAGEP, France Paper CCC Model Predictive Control of a Powder Coating Curing Process: an Application of the Software © Software by: Kamel Abid, Pascal Dufour, Isabelle Bombard, Pierre Laurent CCC’07, Zhangjiajie, July,

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Painting applications in: building (outdoor and indoor), furniture, cars accessories … Need to decrease pollution due to the painting: organic solvent based coating are replaced by powder coatings Quite recently, UV-curable powder coatings and low- temperature coatings designed for heat sensitive substrates have appeared on the coatings market. But few studies on curing kinetics, thermal modelling and control of such powder coating curing process: trajectory tracking or minimization of curing time or … Control problem statement

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC First principle PDE model Schematic drawing of the “substrat+powder” sample Powder coatings = fine particles of: resin + cross-linker in thermosetting or thermoplastic powder coatings + pigments + extenders + flow additives and fillers to achieve specific properties (color, ….)

Université de Lyon- CNRS-LAGEP, France Paper CCC Thermal model based on the Fourier law of heat conduction uses: 1. 1.the temperature variable varying in the thickness of the powder coated metal sample 2. 2.the degree of cure conversion variable (ranging from 0+ to 1 at the end) 2. 2.A non linear PDE Boundary control problem has to be tackled First principle PDE model

Université de Lyon- CNRS-LAGEP, France Paper CCC First principle PDE model [Bombard et al, 2006] Tp(z,t) = temperature across the powder film thickness ep = film thickness (~0.1 mm) x(z,t) = degree of cure Ts(z,t) = temperature across the substrate es = film thickness (~1 mm)  0t,e0,z x)(1xek C ΔHe z t)(z,T Cρ λ t t)(z,T p nm ) t)(z,RT E ( 0 pp 0p 2 p 2 p pc,p p a          0t,ee,ez z t)(z,T Cρ λ t t)(z,T spp 2 s 2 pss sc, s      

Université de Lyon- CNRS-LAGEP, France Paper CCC First principle PDE model [Bombard et al, 2006] 3 boundary conditions for the temperature: Manipulated variable 0t 0,z at )Tt)(z,(Th)Tt)(z,(Tσε(t)φα z t)(z,T λ extpp 4 4 ppir p p      0t,ez at z t)(z,T λ z t)(z,T λ p p sc, p p        0t,eez at )Tt)(z,(Th)Tt)(z,(Tσε z t)(z,T λ sp extss 4 4 ss s s     

Université de Lyon- CNRS-LAGEP, France Paper CCC First principle PDE model [Bombard et al, 2006] The degree of cure x(z,t) of the powder: Initial conditions:  0t,e0,z x)(1xek t t)x(z, p nm ) t)(z,RT E ( 0 p a     0t],ee[0,zTt)(z,Tt)(z,T spextsp  0t],e[0,z0t)x(z, p  

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Advantages: - constraints (such as manipulated variables physical limitations, constraints due to operating procedures or safety reasons…) may be specified - a model aims to predict the future behavior of the process and the best one is chosen by a correct optimal control of the manipulated variables. Drawbacks: - computational time needed may limit online use - suboptimal solutions - how to handle unfeasibilities Model predictive control strategy

Université de Lyon- CNRS-LAGEP, France Paper CCC Model predictive control strategy The function f means: trajectory tracking, processing time minimization, productivity function …

Université de Lyon- CNRS-LAGEP, France Paper CCC Originaly developed for nonlinear PDE model control Main idea: decrease the online time needed to compute the PDE model based control Approach: Input constraints: hyperbolic transformation Output constraints: exterior penalty method Linearization + sensitivites computed off line On line use of a time varying linear model On line resolution of a penalized (and so unconstrained) optimization control problem : a modified Levenberg Marquardt Algorithm Model predictive control strategy [Dufour et al, IEEE TCST 11(5) 2003]

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Developed under Matlab, solves any user defined :   trajectory tracking problem   operating time minimization problem   any cost function   input/output constraint handled Any user defined continuous model (SISO, MISO, SIMO, MIMO model), including large scale PDE model Easy to introduce a user defined observer Easy to apply the software for simulation or real time application ©: flexibility/ease for a quick use in control ! software main features

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Minimization of the curing time, with magnitude+velocity constraints on u(t) + output contraint yp(t) : horizon=6, sampling time = 1s Simulation results

Université de Lyon- CNRS-LAGEP, France Paper CCC Minimization of the curing time, with magnitude+velocity constraints on u(t) + output contraint yp(t) : horizon=6, sampling time = 1s Simulation results

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=6, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=6, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=6, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=14, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=14, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=14, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking: influence of the horizon over the results Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Control problem statement 2. 2.First principle PDE model 3. Model predictive control strategy 4. software main features 5. Simulation results 6. Experimental results 7. Conclusions & perspectives Outline

Université de Lyon- CNRS-LAGEP, France Paper CCC The real time control of powder curing is possible : temperature trajectory tracking Experimental control of PDE system by a general software has been shown Conclusions Perspectives Minimization of the powder curing time under constraints: an observer is under development may be used for any process: since its development, it is currently used for control of polymer production, vial lyophilisation, pasta drying. To use

Université de Lyon- CNRS-LAGEP, France Paper CCC Thank you Any questions ?

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=6, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC Temperature trajectory tracking, with magnitude+velocity constraints on u(t) : horizon=14, sampling time = 1s Experimental results

Université de Lyon- CNRS-LAGEP, France Paper CCC