ADCHEM Final Program

 

Program at a Glance

                                           

                                                  (or you may download the PDF file here)

 

 

Date

 

Time

SUNDAY

MONDAY

TUESDAY

WENDESDAY

11 January

12 January

13 January

14 January

8:00

 

Registration

(Academic Concourse)

 

 

 

 

 

 

 

9:00

Opening Ceremony

(LTB)

Semi-Plenary Lectures

SP #2

Semi-Plenary Lectures

SP #3

 

Session

SP 2.1

(LTF)

 

Session

SP 2.2

(LTG)

 

Session

SP 3.1

(LTF)

 

Session

SP 3.2

(LTG)

 

 

 

 

Plenary Lecture #1

(LTB)

 

 

 

10:00

 

Coffee Break

Coffee Break

 

 

Coffee Break

 

Oral Lectures #3

Oral Lectures #5

 

Session

3.1

(LTD)

 

Session

3.2

(LTF)

 

Session

3.3

(LTG)

 

Session 5.1

(LTD)

 

Session 5.2

 (LTF)

 

Session 5.3

(LTG)

 

11:00

Oral Lectures #1

 

Session 1.1

(LTD)

 

Session 1.2

(LTF)

 

Session 1.3

(LTG)

 

 

 

 

 

12:00

 

 

 

 

Lunch

Lunch

 

13:00

Lunch

 

 

 

 

 

Oral Lectures #4

Oral Lectures #6

14:00

Registration

(Academic Concourse)

Semi-Plenary Lectures

SP #1

Session

4.1

(LTD)

 

Session

4.2

(LTF)

 

Session

4.3

(LTG)

 

Session 6.1

(LTD)

 

Session 6.2

(LTF)

 

Session 6.3

(LTG)

 

 

Session

SP 1.1

(LTF)

 

Session

SP 1.2

(LTG)

 

 

 

 

 

15:00

 

Coffee Break

 

 

Coffee Break

 

Plenary Lecture #3

(LTB)

 

 

Oral Lectures #2

 

Session 2.1

(LTD)

 

Session 2.2

(LTF)

 

Session 2.3

(LTG)

 

16:00

Plenary Lecture #2

(LTB)

 

 

 

 

Closing Ceremony

(LTB)

 

Departure to  Harbour Cruise Reception at 17:00 sharp

 

17:00

Poster Session

(Academic Concourse)

Closing Reception Refreshment

(Academic Concourse)

 

 

 

 

 

 

18:00

Departure to Conference Banquet

                           

                                

 Detailed Program

 

 12 January 2004 (Monday)

 

Plenary Lecture #1           09:30 – 10:30

LTB

Chair: F. Allgower                                                                                                                                

 

Frontiers in Industrial Process Automation – A Personal Perspective

Peter Terwiesch, ABB Process Industries GmbH, GERMANY

 

 

Oral Session #1         11:00 – 13:00

LTD

LTF

LTG

Session 1.1

Session 1.2

Session 1.3

Control Applications 1

System Identification

Control Monitoring and Fault Detection

 

 

 

Co-chairs:

S. Skogestad, F. Doyle

 

Co-chairs:

Y. Arkun, W. Marquardt

Co-chairs:

A. Cinar, C. Scali

11:00 – 11:20

Modeling and Optimization on Energy Costs in Internal Thermally Coupled Distillation Columns of Non-Ideal Mixtures

X. -G. Liu, J. -X. Qian,

Zhejiang University

 

11:00 – 11:20

Stochastic Grey-Box Modeling as a Tool for Improving the Quality of First Engineering Principles Models

N. R. Kristensen, H. Madsen, S. B. Jørgensen, Technical University of Denmark

 

11:00 – 11:20

Development of a Technique for Performance Evaluation of Industrial Controllers

C. Scali, M. Rossi,

University of Pisa

M. Amadei, Polimeri Europa

 

11:20 – 11:40

Multi-objective Robust Control of an Evaporation Process

W. -J. Yan, Zhejiang University

Y. Cao, Cranfield Univeristy

11:20 – 11:40

Identification of Multirate Sampled-Data Systems

J. -D. Wang, T. -W. Chen,

 B. Huang, University of Alberta

11:20 – 11:40

Performance Assessment of Constrained Controllers

C. Georgakis,

Polytechnic University

L.-L. Huang, Lehigh University

 

11:40 – 12:00

Nonlinear Control of a Fluid Catalytic Cracking Unit

Q. Yang, S. -R. Li,

X. -M. Tian, University of Petroleum (East China)

 

11:40 – 12:00

System Identification from Multi-rate Data

R. B. Gopaluni,

H. Raghavan, S. L. Shah, University of Alberta

11:40 – 12:00

Performance Envelopes of Process Intensified Systems

S. R. Abd Shukor, M. T. Tham, University of Newcastle upon Tyne

 

12:00 – 12:20

Estimator Design with PLS Model for Consistent Control of Refinery Main Fractionators

D. Pastore, A.Brambilla,

G. Pannocchia, University of Pisa

12:00 – 12:20

Robust PID Tuning using Closed-Loop Identification

Y. -C. Zhu,

Eindhoven University of Technology

12:00 – 12:20

Fault Diagnosis Based on Limit Measurements of Process Variables

H. A. Preisig,

Norwegian University of Science and Technology (NTNU)

Y. X. Xi, K. W. Lim, National University Singapore

 

12:20 – 12:40

Actuator Selection based upon Model Insights for an Energy Integrated Distillation Column

H. W. Li, R. Gani,

 S. B. Jørgensen,

Technical University of Denmark

 

12: 20 – 12:40

Estimation of Reaction Rates by Nonlinear System Inversion

W. Marquardt, A. Mhamdi, RWTH Aachen

12:20 –12:40

Optimal Experimental Design for Training of a

Fault Detection Algorithm

T. Duever, S. J. Lou,

H. Budman, University of Waterloo

 

12:40 – 13:00

Study on the Soft-Sensor and Control Scheme for an Industrial Azeotropic Distillation Column

S. Zhang, C. -M. Bo, J. Li,

C. -Y. Sun, Y. -R. Wang,

Nanjing University of Technology

 

12:40 – 13:00

An Incremental Approach for the Identification of Reaction Kinetics

W. Marquardt, M. Brendel,

A. Mhamdi, RWTH Aachen

D. Bonvin, EPFL

12:40 – 13:00

Fault Diagnosis and Fault Identification for Fault-Tolerant Control of Chemical Processes

K. -K. Noh, E. S. Yoon,

Seoul National University

 

Semi-Plenary Lectures SP#1         14:00 – 15:10

LTF

LTG

Session SP 1.1

Session SP 1.2

Modelling and Identification

Process and Control Monitoring

 

 

Chair: J. Qin

Chair: B. Huang

 

14:00 – 14:35

New Developments in Industrial MPC Identification

Y. -C. Zhu, Eindhoven University of Technology

14:00 – 14:35

Digital Imaging for Process Monitoring and Control with Industrial Applications

H. -L. Yu, J. F. MacGregor, McMaster University

 

14:35 – 15:10

Modelling and Control of Reactive Distillation Systems

M. O. Tadé, B. H. Bisowarno, Y. -C. Tian,

Curtin University of Technology

 

14:35 – 15:10

Monitoring Performance in Flexible Process Manufacturing

E.B. Martin, A.J. Morris, University of Newcastle

 

Oral Session #2          15:40 – 17:40

LTD

LTF

LTG

Session 2.1

Session 2.2

Session 2.3

Model Predictive Control

Modelling and Identification

Statistical Process Monitoring and Application

 

 

 

Co-chairs:

M. Kothare, A. Vande Wouwer

 

Co-chairs:

K. M. Ng, S. L. Shah

Co-chairs:

E. S.Yoon, M. Kano

 

15:40 – 16:00

Constraint Handling in Reduced Order MPC: Application to Paper Machines

Y. Arkun, Koc University

A. Rigopoulos,

Weyerhaeuser Corp.

 

15:40 – 16:00

A Complete Dynamic Model for Twin Screw Extruders

Y. Le Gorrec, S. Choulak,

F. Couenne, C. Jallut, LAGEP

P. Cassagnau, A. Michel, LMPB

 

15:40 – 16:00

PCA with Efficient Statistical Testing Method for Process Monitoring

F. -P. Mu,

V. Venkatasubramanian,

Purdue University

 

16:00 – 16:20

Simulation-Based Dual Mode Controller for Nonlinear Processes

J. M. Lee, J. H. Lee,

Georgia Institute of Technology

 

16:00 – 16:20

A Data-Driven Model for Valve Stiction

S. L. Shah,

M. A. A. S. Choudhury, University of Alberta

N. F. Thornhill,

University College London

 

16:00 – 16:20

Computation of the Performance of Shewhart Control Charts

E. B. Martin, P. Mulder,

J. Morris,

University of Newcastle

 

16:20 – 16:40

Nonlinear Model Predictive Control of Multicomponent Distillation Columns using Wave Models

S. Schwarzkopf, S. Grüner,

I. Uslu, Universität Stuttgart

A.Kienle, E. D. Gilles,

Max-Planck-Institut für Dynamik Komplexer technischer Systeme Magdeburg

 

16:20 – 16:40

A Software Sensor for a Wastewater Treatment Plant

T. Lopez,

Instituto Mexicano del Petróleo

A. Pulis, M. Mulas, R. Baratti, Universita’ di Cagliari

 

16:20 – 16:40

Combined Multivariate Statistical Process Control

M. Kano, S. Tanaka,

S. Hasebe, I. Hashimoto, Kyoto University

H. Ohno, Kobe University

 

16:40 – 17:00

Nonlinear Model Predictive Control of Cement Grinding Circuits

R.Lepore, A. Vande Wouwer,

M. Remy, Faculté Polytechnique de Mons

 

16:40 – 17:00

Experimental Verification of Gap Metric as a Tool for Model Selection in Multi-Linear Model-Based Control

A. Palazoğlu, University of California, Davis O. Galán,

ABB Australia Limited Paper

J. A. Romagnoli,

University of Sydney

Y. Arkun, Koç University

 

16:40 – 17:00

Batch Monitoring through Common Subspace Models

J. Morris, S. Lane,

E. B. Martin, University of Newcastle

17:00 – 17:20

Optimal Operation and Control of a Reactive Simulated Moving Bed Process

A.Toumi, S. Engell,

University of Dortmund

17:00 – 17:20

Bayesian Estimation of Unconstrained Nonlinear Dynamic Systems

W. -S. Chen, B. R. Bakshi,

P. K. Goel, Ohio State University

S. Ungarala,

Cleveland State University

 

17:00 – 17:20

Application of PLS Based Regression for Monitoring Bitumen Recovery in a Separation Cell

H. Raghavan, S. L. Shah, University of Alberta

R. Kadali, B. Doucette,

Suncor Extraction

 

17:20 – 17:40

Combinations of Measurements as Controlled Variables: Application to a Petlyuk Distillation Column

V.Alstad, S. Skogestad, Norwegian University of Science and Technology (NTNU)

 

17:20 – 17:40

Multivariate Analysis of Process Data using Robust Statistical Analysis and Variable Selection

L. H. Chiang, R. J. Pell,

 M. B. Seasholtz,

Dow Chemical Company

 

17:20 – 17:40

Online Performance Monitoring and Quality Prediction for Batch Processes

A.Cinar, C. Ündey,

Illinois Institute of Technology

 

 

 

13 January 2004 (Tuesday)

 

Semi-Plenary Lectures SP #2       09:00 – 10:10

LTF

LTG

Session SP 2.1

Session SP 2.2

Scheduling and Optimization

Model Based Control

 

 

Chair: S. Hasebe

Chair: J. Lee

 

09:00 – 09:35

Combined On-Line and Run-To-Run Optimization of Batch Processes with Terminal Constrains

C. Welz, B. Srinivasan, D. Bonvin, École Polytechnique Fédérale de Lausanne

 

09:00 – 09:35

A Framework for Design of Scheduled Output Feedback Model Predictive Control

Z. -Y. Wan, M. V. Kothare, Lehigh University

09:35 – 10:10

Constrained Self-Optimizing Control via Differentiation

Y. Cao, Cranfield University

 

09:35 – 10:10

Adaptive Backstepping Nonlinear Control of Bioprocesses

D. Dochain, Université Catholique de Louvain

M. Perrier, Ecole Polytechnique de Montréal

 

 

Oral Session #3         10:40 – 12:40

LTD

LTF

LTG

Session 3.1

Session 3.2

Session 3.3

Nonlinear and Robust Control

Modelling and Control of Biochemical and Biomedical Systems

Process Monitoring

 

 

 

Co-chairs:

A. Palazoglu, J. Hahn

 

Co-Chairs:

M. Henson, R. Parker

Co-Chairs:

J. Alvarez, P. Terwiesch

 

10:40 – 11:00

Design of Sub-Optimal Robust Gain-Scheduled PI Controllers

H. M. Budman, J. -Y. Gao, University of Waterloo

 

10:40 – 11:00

Combined Metabolic and Cell Population Modelling for Yeast Bioreactor Control

M. A. Henson, University of Massachusetts

D. Müller, M. Reuss,

Universität Stuttgart

 

10:40 – 11:00

Process Monitoring Based on Nonlinear Wavelet Packet PCA

Y. Qian, X. -X. Li, J. -F. Wang, Y. -B. Jiang,

South China University of Technology

 

11:00 – 11:20

Adaptive Extremum Seeking Control of Continuous Stirred Tank Bioreactors

M. Guay, Queen's University

D. Dochain, Université Catholique de Louvain

M. Perrier, Ecole Polytechnique de Montréal

 

11:00 – 11:20

Optimization of a Fed-Batch Bioreactor using Simulation-Based Approach

J. H. Lee, N. S. Kaisare,

Georgia Institute of Technology

C.V. Peroni,

Universitat Rovira I Virgili

 

11:00 –11:20

Application of Statistical Process Monitoring with External Analysis to an Industrial Monomer Plant

M. Kano, I. Hashimoto,

Kyoto University

T. Yamamoto,

A. Shimameguri, M. Ogawa,

Mitsubishi Chemical Corporation

 

11:20 – 11:40

Set Stabilization of a Class of Positive Systems

B. A. Foss, L. Imsland, Norwegian University of Science and Technology

 

11:20 – 11:40

Glucose Control in Type I Diabetic Patients: A Volterra Model-Based Approach

R. S. Parker, J. D. Rubb, University of Pittsburgh

11:20 –11:40

On-Line Monitoring of a Copolymer Reactor: A Cascade Estimation Design

T. Lopez, Instituto Mexicano del Petróleo

J. Alvarez, Universidad Autonoma Metropolitana – Iztapalapa

R. Baratti, Universita’ di Cagliari

 

11:40 – 12:00

Stabilization of Gas Lifted Wells based on State Estimation

B. A. Foss, G. O. Eikrem,

L. Imsland,

Norwegian University of Science and Technology

 

11:40 – 12:00

Biomass Reconstruction in a Wastewater Treatment Biofilter

A. Vande Wouwer, C. Renotte, Faculté Polytechnique de Mons

N. Deconinck, P. Bogaerts, Université Libre de Bruxelles

 

11:40 – 12:00

A Robust PCA Modeling Method for Process Monitoring

D.Wang, J. A. Romagnoli, University of Sydney

 

 

12:00 –12:20

H-Infinity Control of Descriptor Systems: An Application from Binary Distillation Control

A. Rehm, F. Allgöwer, Universität Stuttgart

12:00 – 12:20

An Optical Operating Strategy for Fed-Batch Fermentations by Feeding the Overflow Metabolite

S. Valentinotti, C. Cannizzaro,

B. Srinivasan, D. Bonvin,

Ecole Polytechnique Fédérale de Lausanne

 

12:00 – 12:20

A Framework for On-Line Trend Extraction and Fault Diagnosis

V. Venkatasubramanian,

M. R. Maurya,

Purdue University

R Rengaswamy,

Clarkson University

12:20 – 12:40

Cascade Control of Unstable Systems with Application to Stabilization of Slug Flow

S. Skogestad, E. Storkaas, Norwegian University of Science and Technology

12:20 – 12:40

Target-set Control

R. K. Pearson,

Thomas Jefferson University

B. A. Ogunnaike,

University of Delaware

 

12:20 – 12:40

Application of Software Sensors for Monitoring and Prediction in Fermentation Processes

M. Thaysen, S. B. Jørgensen, Technical University of Denmark

 

 

Oral Session #4       13:50  - 15:30

LTD

LTF

LTG

Session 4.1

Session 4.2

Session 4.3

New Formulations and Issues in MPC

Monitoring and Batch Processes

Real Time Optimization and Scheduling

 

 

 

Co-chairs:

S. Engell, S. L. Shah

 

Co-chairs:

H. Preisig, E. B. Martin

 

Co-chairs:

C. C. Yu, T. E. Marlin

 

13:50 –14:10

Developments in Multi-Rate Predictive Control

J. A. Rossiter,

Sheffield University

T. -W. Chen, S.L. Shah, University of Alberta

 

13:50 – 14:10

Investigation of Calibration-Free Resolution Techniques and Independent Component Analysis

E.B. Martin, S. Triadaphillou,

I. Wells, J.A. Morris,

University of Newcastle

 

13:50 – 14:10

Combined Real-Time and Iterative Learning Control Technique with Decoupled Disturbance Rejection for Batch Processes

S. J. Qin, I. S. Chin,

University of Texas at Austin

K. S. Lee, M. Cho,

Sogang University

 

14:10 – 14:30

Nonlinear Predictive Control in the LHC Accelerator

C. de Prada, S. Cristea, University of Valladolid

E. Blanco, J. Casas, CERN

 

14:10 – 14:30

Stage-Based Multivariate Statistical Analysis for Injection Molding

F. -R. Gao, N. -Y. Lu, Y. Yang, the Hong Kong University of Science & Technology

F. -L. Wang,

Northeastern University

 

14:10 – 14:30

Results Analysis in a Constrained Real-Time Optimization (RTO) System

T. E. Marlin, W. S. Yip, McMaster University

 

14:30 – 14:50

Disturbance Attenuation with Actuator Constraints by Moving Horizon H-Infinity Control

H.Chen, Jilin University

C. W. Scherer,

 Delft University of Technology

14:30 – 14:50

Nonlinear Control of a Batch Reactor in the Presence of Uncertainties

Y. Samyudia, H. Sibarani, McMaster University

P. L. Lee,

Curtin University of Technology

 

14:30 – 14:50

Predictive Scheduling of a Penicillin Bioprocess Plant

S. Lau, M. J. Willis, G. A. Montague, J. Glassey,

University of Newcastle

 

14:50 – 15:10

An LMI-based Constrained MPC Scheme with Time-Varying Terminal Cost

B. Pluymers, L. Roobrouck,

J. Buijs, J. A. K. Suykens,

B. De Moor, ESAT-SCD-SISTA

 

14:50 – 15:10

Modeling and Model Based Feeding Control for Pichia pastoris fed-batch cultivation

J. -Q. Yuan, H. -T. Ren,

Shanghai Jiao Tong University

J. -H. Deng, B. -K. He,

L.-M. Ren, North China Pharmaceutical Company

 

14:50 – 15:10

Modeling and Optimization for High-Throughput-Screening Systems

E. Mayer, J. Raisch,

Max-Planck-Institut Magdeburg

15:10 – 15:30

Computational Delay in Nonlinear Model Predictive Control

R. Findeisen, F. Allgöwer, University of Stuttgart

 

15:10 – 15:30

Feedforward Control of Batch Crystallisers - an Approach based on Orbital Flatness

U. Vollmer, J. Raisch,

Max-Planck-Institut Magdeburg

 

15:10 – 15:30

Variance-Constrained Filtering for Uncertain Stochastic Systems with Missing Measurements

Z. D. Wang, Brunel University

W. C. Ho,

City University of Hong Kong

 

 

 

Plenary Lecture #2     16:00 – 17:00
LTB

Chair: W. Marquardt

 

 

 

 

 

A Learning Theory Approach to System Identification

M. Vidyasagar, Tata Consultancy Services

R. L. Karandikar, Indian Statistical Institute

 

 

 

14 January 2004 (Wednesday)

 

Semi-Plenary Lectures SP #3     09:00 – 10:10

LTF

LTG

Session SP 3.1

Session SP 3.2

Batch and Semi – Batch Control

Process Control Applications

 

 

Chair: D. Bonvin

Chair: B. Foss

 

 

09:00 – 09:35

Advances in the Modeling and Control of Batch Crystallizers

Z. K. Nagy, J. W. Chew, M. Fujiwara,

R. D. Braatz, University of Illinois at Urbana-Champaign

 

09:00 – 09:35

MPC in Statoil – Advantages with In-House Technology

S. Strand, J. R. Sagli, Statiol R&D, Process Control

09:35 – 10:10

Joint Process and Control Designs of a Semibatch Emulsion Polymerization Reactor

F. Zaldo, M. Hernández,

Centro de Investigación en Polímeros

J. Álvarez,

Universidad Nacional Autónoma de México

 

09:35 – 10:10

Modeling and Control of Thermal Microsystems

Y. J. Lee, S. Park, Korea Advanced Institute of Science and Technology

S. W. Sung, LG Chem. Ltd. Research Park

D. S. Yoon, G. Lim,

Samsung Advanced Institute of Technology

 

Oral Session #5        10:40 – 12:40

LTD

LTF

LTG

Session 5.1

Session 5.2

Session 5.3

Robustness and Nonlinearity Analysis

Subspace Approaches to Control and Monitoring

Microelectronic Manufacturing Process Control Simulation and Control

 

 

 

Co-Chair:

J. Hahn, N. Hernjak

Co-Chairs:

J. Qin, B. Huang

Co–Chairs:

R. Adomaitis, R. Braatz

 

 

 

10:40 – 11:00

Robust Tuning of Feedback Linearizing Controllers via Bifurcation Analysis

J. Hahn, M. Mönnigmann,

W. Marquardt, RWTH Aachen

10:40 – 11:00

Modified Subspace-Identification Method for Building A Long-Range Prediction Model for Inferential Control

J.H. Lee, Y. -D. Pan,

Georgia Institute of Technology

10:40 – 11:00

Nonlinear Feedback Control of a Coupled Kinetic Monte Carlo-Finite Difference Code

R. D. Braatz, E. Rusli,

T. O. Drews, D. L. Ma,

R. C. Alkire, University of Illinois at Urbana-Champaign

 

11:00 – 11:20

Closed Loop Properties and Block Relative Gain

J. F. Forbes, V. Kariwala,

E. S. Meadows,

University of Alberta

 

11:00 – 11:20

Model Identification and Error Covariance Matrix Estimation from Noisy Data using PCA

S. L. Shah, University of Alberta

S. Narasimhan, Indian Institute of Technology

 

11:00 – 11:20

Optimal Control of Transient Enhanced Diffusion

R. D. Braatz, R. Gunawan,

M. Y. L. Jung, E. G. Seebauer, University of Illinois at Urbana-Champaign

 

11:20 – 11:40

A Tool to Analyze Robust Stability for Constrained MPC

L. O. Santos, J. A. A. M. Castro, Universidale de Coimbra

L. T. Biegler, Carnegie Mellon University

11:20 – 11:40

Nonlinear Subspace Model Identification

A. Cinar, J. DeCicco,

Illinois Institute of Technology

11:20 – 11:40

Application of Reduced-Rank Multivariate Methods to the Analysis of Spatial Uniformity of Silicon Wafer Etching

P. Misra, M. Nikolaou,

University of Houston

A. D. Bailey III, Lam Research Corporation

 

11:40 – 12:00

Relationship between Control-Relevant Nonlinearity and Performance Objective

N. Hernjak, University of Delaware

F. J. Doyle III, University of California, Santa Barbara

F. Allgöwer,

T. Schweickhardt, Universität Stuttgart

 

11:40 – 12:00

Semi-Batch Trajectory Control in Reduced Dimensional Spaces

J. Flores-Cerrillo,

J. F. MacGregor,

McMaster University

 

11:40 – 12:00

Real-Time Feedback Control of Carbon Content of Zirconium Dioxide Thin Films Using Optical Emission Spectroscopy

P. D. Christofides, N. Dong,

Y. Lou, S. Lao, J. P. Chang, University of California, Los Angeles

 

12:00 – 12:20

Effect of Process Nonlinearity on Linear Quadratic Regulator Performance

M. Guay, R. Dier,

P. J. McLellan, Queen's University

12:00 – 12:20

A Subspace Approach to MIMO Control Performance Monitoring and Diagnosis

S. J. Qin,

University of Texas at Austin

C.A. McNabb,

Boise Paper Solutions

 

12:00 –12:20

Design, Simulation, and Experimental Testing of a Spatially Controllable CVD Reactor

R. A. Adomaitis, J. -O. Choo,

G. W. Rubloff,

L. Henn-Lecordier, Y. -J. Liu, University of Maryland

 

12:20 – 12:40

Lower Limit on Controller Gain for Acceptable Disturbance Rejection

S. Skogestad, Norwegian University of Science and Technology (NTNU)

12:20 – 12:40

Multivariate Controller Performance Assessment without Interactor Matrix

– a Subspace Approach

B. Huang, R. Kadali,

University of Alberta

 

 

 

Oral Session #6         13:50 –15:30

LTD

LTF

LTG

Session 6.1

Session 6.2

Session 6.3

Control Application 2

Batch Process and Control

Advances in Process Control

 

 

 

Co-chairs:

D. Dochain, J. Rieber

Co-chairs:

C. Georgakis, S. B. Jørgensen

Co-chairs: 

S. Pistikopoulos, B. Srinivasan

 

 

 

13:50 –14:10

Model-Based Trajectory Control of Pressure Swing Adsorption Plants

M. Bitzer, K. Graichen,

M. Zeitz, Universität Stuttgart

13:50 – 14:10

Feedback Control of Industrial Solution Polymerization of Acrylic Acid using NIR Measurements

G. Févotte, N. Othman, Université Lyon 1

J. B. Egraz, J. M. Sau, COATEX

 

13:50 –14:10

Robust Iterative Learning Control Design based on Gradient Method

S. Liu, T. -J. Wu,

Zhejiang University

14:10 – 14:30

Control of Gasholder Level by Trend Prediction based on Time-Series Analysis and Process Heuristics

C. Han, Y. -H. Chu, J. H. Kim, Pohang University of Science and Technology

S. J. Moon, I. S. Kang, Pohang Iron and Steel Company

S. J. Qin, University of Texas at Austin

 

14:10 – 14:30

Data-Driven Modeling of Batch Processes

D. Bonné, S. B. Jørgensen, Technical University of Denmark

14:10 – 14:30

Compensator for Internet-based Advanced Control

S. -H. Yang, X. Chen, Loughborough University

14:30 – 14:50

Setting of Injection Velocity Profile via an Iterative Learning Control Approach

F. -R. Gao, Y. Yang,

The Hong Kong University of Science and Technology

 

14:30 – 14:50

Two-dimensional Population Balance Modeling of Semi-Batch Organic Solution Crystallization

G.Févotte, F. Puel,

Université Lyon 1

 

14:30 – 14:50

Model-Based Auto-Tuning System Using Relay Feedback

H. -P. Huang, K. -Y. Luo, National Taiwan University

14:50 – 15:10

Dynamics of Process Networks with Recycle and Purge: Time Scale Separation and Model Decomposition

P. Daoutidis, M. Baldea, University of Minnesota

A. Kumar, GE Corporate Research and Development

 

14:50 – 15:10

Calorimetric Estimation of Viscosity and Acid Number in Alkyd Reactors

I. S. de Buruaga, Centro de Investigación en Polímeros

T. Lopez, S. Pérez, J. Alvarez, Universidad Autónoma Metropolitana-Iztapalapa

 

14:50 – 15:10

The Explicit Model-Based Tracking Control Law via Parametric Programming

E. N. Pistikopoulos, V. Sakizlis, J. D. Perkins,

Imperial College London

15:10 – 15:30

Youla-Kučera Parametrisation in Self-Tuning LQ Control of a Chemical Reactor

J. Mikleš, L. Čirka, M. Fikar, Slovak University of Technology in Bratislava

15:10 – 15:30

State Estimation in Batch Crystallization using Reduced Population Models

S. Motz, S. Mannal,

E. D. Gilles, Universität Stuttgart

 

15:10 – 15:30

Discrete Control of Nearly Integrable Two-Dimensional Continuous Systems

S. Blouin, M. Guay, K. Rudie, Queen’s University

 

Plenary Lecture #3          15:30 – 16:30

LTB

Chair: F. -R. Gao

 

 

 

 

 

A Systems Approach to Modelling and Analyzing Biological Regulation

F. J. Doyle III, University of California, Santa Barbara

 

 

 

13 January 2004 (Tuesday)

 

Poster Session          17:00 –18:00

Chair: F. -R. Gao

 

Area 1      Process and Control Monitoring

 

P1-1      Variance Estimation in Multisensor Fusion Algorithm

C. -Q. Zhong, X. -L. Dong, L.-Y. Zhang, Y. Cao, Dalian University of Technology

 

P1-2      Respirometry Estimations Based Monitoring of Biological Wastewater

Treatment Processes

D. -C. Yuan, L.-P. Fan, H. -B. Yu, Shenyang Institute of Automation

 

P1-3      Wavelet Packet Images Matching Applied to Noise Faults Diagnosis

C. Lu, G. -Z. Wang, Tsinghua University

Q. -G. Qiu, Dalian University of Technology

 

P1-4      Performance Monitoring based on Characteristic Subspace

M. Guo, S. -Q. Wang, Zhejiang University

 

P1-5      Sensing of the Dry Point of Benzene using PCA and DRBFN

Y. -Q. Chang, F. -L. Wang, Northeastern University

F. -R. Gao, The Hong Kong University of Science and Technology

 

P1-6      A Fault Diagnosis Method for Fermentation Process

L.-L. Ma, F. -L. Wang, Y. -B. Jiang, Northeastern University

F. -R. GAO, The Hong Kong University of Science and Technology

 

P1-7      Multi-PCA Models for Process Monitoring and Fault Diagnosis

L.-L. Ma, Y. -B. Jiang, F. -L. Wang, Northeastern University

F. -R. Gao, Hong Kong University of Science and Technology

 

P1-8      A Fault Accommodation Control For Nonlinear Processes

Y. -W. Zhang, F. -L. Wang, G. Yu, Northeastern University

F. -R. Gao, The Hong Kong University of Science & Technology

 

P1-9      A Novel Detection of Vessel Liquid Level based on Echo Identification

Z. -H. Zhang, J. -M. Yuan, University of Science and Technology Beijing

W. -Y. Huang, Southeast University

 

P1-10    Multi-Site Performance Monitoring in Batch Pharmaceutical Production

C. W. L. Wong, A. J. Morris and E. B. Martin, University of Newcastle

R. E. A. Escott, GlaxoSmithKline Chemical Development

 

P1-11    Process Monitoring of an Electro-Pneumatic Valve Actuator Using Kernel

Principal Component Analysis

S. -O. Song, G. Lee, E. S. Yoon, Seoul National University

 

P1-12    Real-Time Application of Scheduling Quasi-Minmax Model Predictive Control to a Bench-Scale Neutralization

Y. -H. Lu, Georgia Institute of Technology

Y. Arkun, KOC University

A. Palazoglu, University of California at Davis

 

P1-13    Fault-Tolerant Control of Process Systems: Integrating Supervisory and Feedback Control over Networks

N. H. El-Farra, A. Gani, P. D. Christofides, University of California, Los Angeles

 

Area 2     Real-Time Optimization and Scheduling

 

P2-1      Real-Time Optimization of Distillation Column via Sliding Modes

A. Y. Torgashov, K. -C. Park, H. -C. Choi, Y. -K. Choe, Samsung Fine Chemicals

Co., Ltd.

 

P2-2      A Receding Optimization Control Policy for Production Systemswith Quadratic Inventory Costs

C. -Y. Song, H. Wang, P. Li, Zhejiang University

 

P2-3      Hard Real-Time CORBA (HRTC) for Process Control Systems

S. Galán, M. Rodríguez, R. Sanz, Universidad Politécnica de Madrid

 

P2-4      A Disaggregation Technique for the Optimal Planning of Offshore Platforms

M. C. A. Carvalho, University of Sao Paulo

J. M. Pinto, Polytechnic University

 

Area 3     Process and Control Applications

 

P3-1      Analysis and Modeling of Industrial Purified Terephthalic Acid Oxidation

Process

S. -J. Mu, H. -Y. Su, R. -L. Liu, Y. Gu, J. Chu, Zhejiang University

 

P3-2      Analyzing the Start-Up of Reactive Distillation Columns

F. Reepmeyer, J. -U. Repke, G. Wozny, Technical University Berlin

 

P3-3      Plantwide Economical Dynamic Optimization: Application on a Borealis Borstar Process Model

W. Van Brempt, P. Van Overschee, T. Backx, IPCOS

Ø. Moen, Borealis

C. Kiparissides, C. Chatzidoukas, Aristotle University of Thessaloniki

 

P3-4      Fuzzy Neural Network for Predicting 4-CBA Concentration of PTA Process

R. -L. Liu, Y. -X. Wang, H. -Y. Su, S. -J. Mu, Y. -Y. Hu, W. -Q. Chen, J. Chu, Zhejiang University

 

P3-5      Designing Neurofuzzy System based on Improved CART Algorithm

L. Jia, E. -G. Li, J. -S. Yu, East China University of Science and Technology

 

P3-6      Hybrid Control of a Four Tanks System

C. de Prada, S. Cristea, University of Valladolid

D. Megías, J. Serrano, Universitat Autónoma de Barcelona

 

P3-7      Temperature Control of Butyl Propionate Reactive Distillation

S. -G. Huang, National Taiwan University of Science and Technology

C. -C. Yu, National Taiwan University

 

P3-8      Design and Control for Recycle Process with Tubular Reactor

Y. -H. Chen, National Taiwan University of Science and Technology

C. -C. Yu, National Taiwan University

 

P3-9      Optimal Control of Fluid Catalytic Cracking Unit

Q. -Y. Jiang, Z. -K. Cao, J. Cai, H. Zhou, Xiamen University

Z. -L. Chen, C. -L. Wang, X. -L. Chen, M. -B. Deng, China Petroleum & Chemical Corporation Guangzhou Branch

 

P3-10    Modeling and Advanced Process Control (APC) for Distillation Columns of Linear Alkylbenzene Plant

X. -M. Jin, G. Rong, S. -Q. Wang, Zhejiang University

 

Area 4     Model-Based Control

 

P4-1      A Robust Iterative Learning Control with Neural Networks for Robot

C. Shao, J. Nie, Dalian University of Technology

F. -R. Gao, The Hong Kong University of Science and Technology

 

P4-2      Robust Stable Adaptive Control of Uncertain Bilinear Plants and It’s Application for Distillation Column

C. Shao, G. Luo, Dalian University of Technology

F. -R. Gao, The Hong Kong University of Science and Technology

 

P4-3      Combined Gain-Scheduling and Multimodel Control of a Reactive Distillation

Column

B. H. Bisowarno, Y. -C. Tian, M. O. Tadé, Curtin University of Technology

 

P4-4      Constructing Takagi-Sugeno Fuzzy Model based on Modified Fuzzy Clustering

Algorithm

Z. -Y. Xing, L.-M. Jia, T. -Y. Shi, Y. Qin, Q. -H. Jiang, China Academy of Railway

Science

 

P4-5      Nonlinear Predictive Functional Control based on Artificial Neural Network

Q. -L. Zhang, L. Xie, S. -Q. Wang, Zhejiang University

 

P4-6      Computational Intelligence (CI) Self-Adaptive PID (CISAPID)

M. -Z. Yi, Y. Qin, L.-M. Jia, China Academy of Railway Sciences

 

P4-7      Robust Stability Analysis for Descriptor Systems with State Delay and Parameter Uncertainty

S. -Y. Xu, J. Lam, University of Hong Kong

C. -W. Yang, Nanjing University of Science and Technology

 

P4-8      Zone Model Predictive Control Algorithm Using Soft Constraint Method

Z. -H. Xu, J. Zhao, J. -X. Qian, Zhejiang University

 

P4-9      Evaluation Method and Workbench for APC Strategies

G. Reinig, B. Mahn, M. Boll, Ruhr University of Bochum

 

P4-10    Non-Fragile PID Stabilizing Controller on Second-Order Systems with Time Delay

J. -M. Xu, L. Yu, Zhejiang University of Technology

 

P4-11    A Method of Controlling Unstable, Non-Minimum-Phase, Nonlinear Processes

C. Panjapornpon, M. Soroush, Drexel University

W. D. Seider, University of Pennsylvania

 

P4-12    Design of a Sliding Mode Control System based on an Identified SOPDT Model

C. -T. Chen, S. -T. Peng, Feng Chia University

 

P4-13    Nonlinear MIMO Adaptive Predictive Control based on Wavelet Network Model

D. -X. Huang, Y. -H. Wang, Y. -H. Jin, Tsinghua University

 

P4-14    Input-Output Pairing of Multivariable Predictive Control

L.-C. Chen, GAIN Tech Co.

P. Yuan, G. -L. Zhang, University of Petroleum

 

P4-15    Generalized Predictive Control for a Class of Bilinear Systems

G. -Z. Liu, P. Li, Liaoning University of Petroleum & Chemical Technology

 

P4-16    Nonlinear Model Predictive Control using a Neural Network

R. -D. Zhang, P. Li, Liaoning University of Petroleum & Chemical Technology

 

P4-17    Process Optimization and Control under Chance Constraints

P. Li, M. Wendt, H. Arellano-Garcia, G. Wozny, Technische Universität Berlin

 

P4-18    Adaptive Extremum Seeking Control of Nonisothermal Continuous Stirred Tank

Reactors

M. Guay, Queen’s University

D. Dochain, Université Catholique de Louvain

M. Perrier, Ecole Polytechnique de Montréal

 

P4-19    On the Use of Controller Parameterization in the Optimal Design of Dynamically Operable Plants

K. G. Dunn, C. L. E. Swartz, McMaster University

 

P4-20    Improved Performance of Robust MPC with Feedback Model Uncertainty

A. L. Warren and T. E. Marlin, McMaster University

 

P4-21    Adaptive Extremum Seeking Output Feedback Control for a Continuous Stirred Tank Bioreactor

N. I. Marcos, M. Guay, Queen’s University

D. Dochain, Université Catholique de Louvain

 

P4-22    A BMI-Based Design of Switched PID Controllers

J. Aoyama, K. Konishi, T. Yamamoto, T. Hinamoto, Hiroshima University

 

P4-23    Hybrid Control: Implementing Output Feedback MPC with Guaranteed Stability

Region

P. Mhaskar, N. H. El-Farra, P. D. Christofides, University of California, Los Anglos

 

P4-24    An Internal Model Control for Max-Plus Linear Systems with Linear Parameter Varying Structure

S. Masuda, T. Amemiya, Tokyo Metropolitan Institute of Technology

H. Goto, K. Takeyasu, Japan Research Institute

 

Area 5      Modeling and Identification

 

P5-1      Hybrid strategy for parameter estimation and PID tuning

L. Wang, D. -Z. Zheng, D. -X. Huang, Tsinghua University

 

P5-2      Integration of Product Quality Estimation and Operating Condition Monitoring for Efficient Operation of Industrial Ethylene Fractionator

H. Kamohara, A. Takinami, M. Takeda, Showa Denko K.K.

M. Kano, S. Hasebe, I. Hashimoto, Kyoto University

 

P5-3      On-Line Lower-Order Modeling Using Fuzzy Systems

A. B. Rad, H. F. Ho, Y. K. Wong, W. L. Lo, the Hong Kong Polytechnic University

 

P5-4      A Novel Soft Sensor Modeling for Gasoline Endpoint of the Crude Unit

X. -M. Tian, G. -C. Chen, University of Petroleum

 

P5-5      State and Parameter Estimation through Dynamic Bayesian Forecasting

Z. Lu, E. Martin, J. Morris, University of Newcastle

 

P5-6      Heat Transfer in a Cable Penetration Fire Stop System

S. -P. Kwon, J. Cho, S. -O. Song, W. Kim, E. S. Yoon, Seoul National University

 

P5-7      Modeling of Metabolic Systems using Global Optimization Methods

E. P. Gatzke, University of South Carolina

E. O. Voit, Medical University of South Carolina

 

P5-8      A State-Shared Modeling Approach to Transition Control

Z. -H. Tian, K. A. Hoo, Texas Tech University

 

Area 6     Batch Process Modeling and Control

 

P6-1      Temperature Control of the Batch Polypropylene Reactor by ADRC

Y. -Q. Wang, X. -F. Zhu, South China University of Technology

 

P6-2      Fermentation Batch Process Monitoring by Step-By-Step Adaptive MPCA

N. He, L. Xie, S. -Q. Wang, J. -M. Zhang, Zhejiang University

 

P6-3      Improved Operation of a Batch Polymerization Reactor through Batch-To-Batch Iterative Optimization

Z. -H. Xiong, J. Zhang, University of Newcastle

 

P6-4      Kappa Number Prediction by Hybrid Model for Batch Pulp Cooking Process

Y. Li, J. Zhang, X. -F. Zhu, D. -P. Huang, South China University of Technology

 

P6-5      A Modular Batch Laboratory Process

R. Olsson, K. -E. Årźen, Lund Institute of Technology