Skogestad, Sigurd - Department of Chemical Engineering, Norwegian University of Science and Technology

• An Industrial and Academic Perspective on Plantwide Control James J. Downs*. Sigurd Skogestad**
• IMPLEMENTATION OF MPC ON A DEETHANIZER AT KARST GAS PLANT
• Computerschem. Engng,Vol.2l, Suppl..pp.$379-$384,1997 Peroamon 1997ElsevierScienceLtd
• Buffer Tank Design for Acceptable Control Performance
• Automatica,Vol.28.No.5. pp.989-996.1992 PrintedinGreatBritain. 0005-1098/92$5.00+0.00
• 1. INTRODUCTION The thermally integrated ``Petlyuk'' arrangement imple
• Achievable H1 performance of multivariable systems with unstable zeros and poles
• NCO tracking and Self-optimizing Control in the Context of Real-Time Optimization
• Selection of controlled variables: Maximum gain rule and combination of measurements
• Computerschem.EngngVol.20, Suppl.,pp. SI005-SI010,1996 Copyright 1996ElsevierScienceLtd
• Model Predictive Control of a Kaibel Distillation Column
• "Distillation, Absorption and Extraction" April 5-6, 2001 in Bamberg,, Halvorsen NTNU Department of Chemical Engineering
• Pergamon 0005-1098(93)E0063-A Automatica, Vol. 30, No. 10, pp. 1601-1607, 1994
• Complex Distillation Arrangements : Extending the Petlyuk Ideas
• Degrees of freedom and optimal operation of simple heat pump cycles
• Forpeerreview Dynamic considerations in the synthesis of self-optimizing control
• Symposium on Recent and Emerging Advances in Chemical Engineering (REACH), Indian Institute of Technology Madras, Chennai, India. December 2-4, 2010.
• CONTROL STRUCTURE DESIGN AND PLANTWIDE CONTROL The search for the self-optimizing control structure
• 0 20 40 60 80 Proposed method with F=1 (overshoot=0.10)
• An aggregation model reduction method for one-dimensional distributed parameter systems
• Use of Shortcut Methods to Analyse Optimal Operation of Petlyuk Distillation Columns
• On the Dynamics of Batch Distillation : A Study of Parametric Sensitivity in Ideal
• DYNAMICS AND CONTROL OF DISTILLATION COLUMNS A CRITICAL SURVEY
• Energy Savings in Complex Distillation Arrangements: Importance of Using the Preferred Separation
• Automaaca, Vol. 25, No. 1, pp. 119-125, 1989 Printed in Great Britain.
• Limit Cycles with Imperfect Valves: Implications for Controllability of Processes with Large Gains
• The dos and don'ts of distillation column control Sigurd Skogestad*
• On-Line PI Controller Tuning Using Closed-Loop Setpoint Response Mohammad Shamsuzzohaa
• THE DYNAMIC BEHAVIOR OF CASCADE PROCESSES WITH APPLICATION TO DISTILLATION COLUMNS
• A Plantwide Control Procedure with Application to Control Structure Design for a Gas Power Plant
• STUDIES ON PLANTWIDE CONTROL Truls Larsson
• MULTIVESSEL BATCH DISTILLATION 1 SIGURD SKOGESTAD 2 , BERND WITTGENS,
• SVD Controllers for H 2 , H1 , and Optimal Morten Hovd a , Richard D. Braatz b and Sigurd Skogestad a;1
• Selfoptimizing control: From key performance indicators to control of biological systems 1
• DISCUSSION AND CONCLUSIONS In this concluding chapter, the first section provides a short discussion focusing on the
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• Explicit Real-Time Optimization Johannes Jschke, Sridhar Narasimhan, Sigurd Skogestad
• European Symposium on Computer Aided Process Engineering ESCAPE20 S. Pierucci and G. Buzzi Ferraris (Editors)
• CASCADE CONTROL OF UNSTABLE SYSTEMS WITH APPLICATION TO
• PROCESS DESIGN AND CONTROL Steady-State Operational Degrees of Freedom with Application to Refrigeration
• COMBINATIONS OF MEASUREMENTS AS CONTROLLED VARIABLES: APPLICATION
• Self-optimizing control of a large-scale plant: The Tennessee Eastman process
• SIMULATION OF HENs This chapter describes how dynamic simulations of HENs can be carried out. The type and
• CONTROL STRUCTURE DESIGN Sigurd Skogestad
• M. S. Govatsmark, T. Larsson and S. Skogestad Controllability Analysis and Matlab Software Controllability Analysis and Matlab
• MODELING, IDENTIFICATION AND CONTROL, 2003, VOL. 24, NO. 4, 231244 State Space Realization of Model Predictive Controllers Without
• On the Topology of Ternary VLE Diagrams: Elementary Cells
• European Symp. on Computer Application in the Chemical Industry, Erlangen, 23-26 April, 1989
• Self-optimizing control: Basis issues and Taylor series analysis
• CONTROLLABILITY ANALYSIS PLANTWIDE CONTROL
• Explicit MPC with output feedback using self-optimizing control
• CONTROL CONFIGURATION SELECTION FOR DISTILLATION COLUMNS UNDER TEMPERATURE CONTROL
• CONTROLLABILITY Eureach/Cache
• ACKNOWLEDGMENTS I would like to thank my supervisor at NTNU prof. Sigurd Skogestad for
• THE DYNAMICS OF CHEMICAL REACTORS WITH HEAT INTEGRATION
• ANALYSIS AND CONTROL OF DISTILLATION COLUMNS Sigurd Skogestad, Chem. Eng., Norwegian Inst. of Tech. (NTH), N7034 Trondheim, Norway
• PLANTWIDE CONTROL: THE SEARCH FOR THE SELFOPTIMIZING CONTROL STRUCTURE
• Modelling and Dynamic Simulation for Process Control
• DIRECTIONS AND FACTORIZATIONS OF ZEROS AND POLES IN MULTIVARIABLE SYSTEMS
• Selfoptimizing control of a largescale plant: The Tennessee Eastman process
• MINIMIZATION OF STATE DEVIATIONS USING PERFECT INDIRECT CONTROL
• On-Line PI Controller Tuning Using Closed-Loop Setpoint Response Mohammad Shamsuzzohaa
• Dynamic Modelling for Control of Fuel Cells Federico Zenith
• Federico Zenith Control of fuel cells
• PLANTWIDE CONTROL: THE SEARCH FOR THE SELF-OPTIMIZING CONTROL STRUCTURE
• A review of plantwide control Sigurd Skogestadand Truls Larsson
• Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column
• Chapter 8: Conclusions and Further Work 162 88.. CCOONNCCLLUUSSIIOONNSS
• MULTIVESSEL BATCH DISTILLATION 1 SIGURD SKOGESTAD 2 , BERND WITTGENS,
• MULTIVESSEL BATCH DISTILLATION SIGURD SKOGESTAD 1 , BERND WITTGENS, EVA SRENSEN 2
• Selfoptimizing control: From key performance indicators to control of biological systems 1
• OPTIMAL OPERATION OF INTEGRATED PROCESSES
• LIMITATIONS IMPOSED BY RHP ZEROS/POLES IN MULTIVARIABLE SYSTEMS
• Computers and Chemical Engineering 23 (1999) 509522 Optimal operation of heat exchanger networks
• PROCESS DESIGN AND CONTROL Optimal Selection of Controlled Variables
• 8th International IFAC Symposium on Dynamics and Control of Process Systems
• FLOWSHEET CONTROLLABILITY ASSESSMENT TOOLS Sigurd Skogestad
• Chemical Engineering Science 60 (2005) 28952909 www.elsevier.com/locate/ces
• Proceedings of the 1st Annual Gas Processing Symposium
• Heteroazeotropic Batch Distillation Feasibility and Operation
• Modeling, Identification and Control, Vol. 30, No. 3, 2009, pp. 149155, ISSN 18901328 Feedback: Still the Simplest and Best Solution
• A Simple Strategy for Optimal Operation of Heat Exchanger V. LERSBAMRUNGSUK1
• Self-optimizing control: From key performance indicators to control of biological systems 1
• NTNU Dr. ing. Thesis 2001:43 Ivar J. Halvorsen Minimum Energy Requirements
• pHNEUTRALIZATION: INTEGRATED PROCESS AND CONTROL DESIGN
• LIMITATIONS IMPOSED BY RHP ZEROS/POLES IN MULTIVARIABLE SYSTEMS
• MODELING AND CONTROL OF A CONTINUOUS BIOREACTOR WITH CROSSFLOW FILTRATION
• Separation of Azeotropic Mixtures: Tools for Analysis and Studies
• This article was originally published in a journal published by Elsevier, and the attached copy is provided by Elsevier for the
• Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Grak (Editors)
• Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Grak (Editors)
• Economically Efficient Operation of CO2 Capturing Process Part I: Self-optimizing Procedure for Selecting the Best Controlled Variables
• Multi-product dividing wall columns: A simple and effective assessment and conceptual design
• ADCHEM 2006 International Symposium on Advanced Control of Chemical Processes
• CONTROLLABILITY MEASURES FOR DISTURBANCE Sigurd Skogestad
• A Comparative Analysis of Numerical Methods for Solving Systems of Nonlinear Algebraic Equations
• Evaluation of Dynamic Models of Distillation Columns with Emphasis on the Initial Response
• NTNU Dr. ing. Thesis 2001:43 Ivar J. Halvorsen Notation and Nomenclature 19
• Elsevier Editorial System(tm) for Computers & Chemical Engineering Manuscript Draft
• Chapter 1: Introduction 1 11.. IINNTTRROODDUUCCTTIIOONN
• T. Larsson, S. Skogestad Control of a industrial heat integrated distillation column Control of a industrial
• Control of a Fuel-Cell Powered DC Electric Vehicle Motor
• INTEGRATED OPTIMIZATION AND Marius Stre Govatsmark
• Data reconciliation and optimal operation of a catalytic naphtha reformer
• MIQP formulation for Controlled Variable Selection in Self Optimizing Control Ramprasad Yelchuru*, Sigurd Skogestad*, Henrik Manum*
• CONTROLLABILITY ANALYSIS FOR PROCESS AND CONTROL SYSTEM
• International Journal of Control Vol. 78, No. 16, 10 November 2005, 13271341
• OPTIMAL STARTUP PROCEDURES FOR BATCH DISTILLATION E. S RENSEN2 AND S. SKOGESTAD1
• Consistent inventory control Elvira Marie B. Aske,, and Sigurd Skogestad,
• Reduced distillation models via stage aggregation Andreas Linhart, Sigurd Skogestad
• Relative Gain Array for Norm-Bounded Uncertain Systems Vinay Kariwala and Sigurd Skogestad*
• Graphical Visualisation of Minimum Energy Requirements for Multi-Effect Distillation Arrangements
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE VECTORS
• Three important parts of an integrated plant are reactors, separators and a heat exchanger network (HEN) for heat recovery. Within the process engineering community, much
• Analysis of instability in an industrial ammonia John C. Morud Sigurd Skogestad \Lambda
• THE USE OF RGA AND CONDITION NUMBER AS ROBUSTNESS MEASURES
• Integrated Design, Operation and Control of Batch Extractive Distillation with a Middle Vessel
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE VECTORS
• Performance limitations for unstable SISO plants Kjetil Havre \Lambda and Sigurd Skogestad y
• An Industrial and Academic Perspective on Plantwide Control James J. Downs*. Sigurd Skogestad**
• Improved Analysis and Understanding of the Petlyuk Distillation Column
• BASIC IDEAS AND CONCEPTS This chapter includes the common basis required for the subsequent chapters, particularly for
• ROBUST CONTROL OF DISTILLATION COLUMNS Sigurd Skogestad
• Please cite this article in press as: Lid, T., Skogestad, S., Scaled steady state models for effective on-line applications, Computers and Chemical Engineering (2007), doi:10.1016/j.compchemeng.2007.04.003
• Elvira Marie B. Aske Design of plantwide control
• Reply to "Further Theoretical Results on `Relative Gain Array for Norm-Bonded Uncertain Vinay Kariwala*
• Computers and Chemical Engineering 31 (2007) 15901601 Optimal operation of simple refrigeration cycles
• Optimal Operation of Transient Processes Using Feedback Control
• International Conference CYBERNETICS AND INFORMATICS
• Proceedings of ECOS 2005 Trondheim, Norway
• Optimal Output Selection for Control of Batch Processes Hkon Dahl-Olsen, Sridharakumar Narasimhan and Sigurd Skogestad
• This article was published in an Elsevier journal. The attached copy is furnished to the author for non-commercial research and
• Control of a Industrial Heat Integrated Distillation Column T. Larsson and S. Skogestad
• Single-cycle mixed-fluid LNG process Part II: Optimal operation
• Application of Plantwide Control to the HDA Process. II -Regulatory Control
• Control Structure Selection for an Evaporation Process Marius S. Govatsmark a , Sigurd Skogestad a
• Azeotropic Phase Equilibrium Diagrams: V. N. Kiva , E. K. Hilmen y and S. Skogestad z
• SELFOPTIMIZING CONTROL: A DISTILLATION CASE Sigurd Skogestad
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE DIRECTIONS.
• University of Alberta Library Release Form
• Input performance limitations of feedback control Vinay Kariwala, Sigurd Skogestad, J. Fraser Forbes and Edward S. Meadows
• Improved Analysis and Understanding of the Petlyuk Distillation Column
• Self-optimizing control: Local Taylor series analysis
• Plantwide control: The search for the selfoptimizing control structure
• Techniques in the Control of Interconnected Plants Morten Hovd \Lambda
• STUDIES ON CONTROL OF INTEGRATED Erik Alten Wolff
• Control of Reactor and Separator, with Recycle T. Larsson, S. Skogestad and ChengChing Yu y
• INPUT/OUTPUT SELECTION AND PARTIAL CONTROL Kjetil Havre 1 and Sigurd Skogestad 2
• Chemical Engineering Science. Vol. 43, No. 1. pp. 3348, 1988. Printed in Great Britain.
• COMPLEXITY MEASURE FOR BLOCK DIAGRAMS E. S. Hori1
• Evaluation of Dynamic Models of Distillation Columns with Emphasis on the Initial Response
• MULTIVESSEL BATCH DISTILLATION 1 SIGURD SKOGESTAD 2 , BERND WITTGENS,
• A low-dimensional dynamic model of severe slugging for control design and analysis
• Selfoptimizing control: The basic idea and Taylor series analysis
• OPTIMAL OPERATION USING STRUCTURAL INFORMATION
• On the Dynamics of Batch Distillation : A Study of Parametric Sensitivity in Ideal
• Journal of Process Control 21 (2011) 986 Contents lists available at ScienceDirect
• Self-optimizing control: Optimal measurement selection Department of Chemical Engineering
• STUDIES ON PLANTWIDE CONTROL Truls Larsson
• LIMITATIONS IMPOSED BY RHP ZEROS/POLES IN MULTIVARIABLE SYSTEMS
• On the Topology of Ternary VLE Diagrams: Elementary Cells
• Limitations imposed by lower layer control configurations. Truls Larsson and Sigurd Skogestad \Lambda
• DYCOPS5 Symposium: Corfu, Greece, June 810, 1998 1. INTRODUCTION
• The SIMC method for smooth PID controller Sigurd Skogestad and Chriss Grimholt
• Balancing Energy Consumption and Food Quality Loss in Supermarket Refrigeration System
• Report on the setpoint overshoot method (supplementary material)
• 1848 Ind. Eng. Chem. Res. 1988,27, 1848-1862 Wiede, W., Jr.; Reklaitis,G. V. "Determinationof Completion Times
• Control strategies for reactive batch distillation Eva Swensen and Sigurd Skogestad"
• DYNAMICSAND CONTROLOF DISTILLATIONCOLUMNS A tutorial introduction
• EFFECT OF RHP ZEROS AND POLES ON PERFORMANCE IN MULTIVARIABLE SYSTEMS and S. Skogestad 2
• BK1064-ch56_R2_250706 SELF-OPTIMIZING CONTROL CONFIGURATIONS FOR
• Distillation Absorption 2010 J. Strandberg, S. Skogestad and I.J. Halvorsen
• Time (Energy) Requirements in Closed Batch Distillation Arrangements
• Please cite this article in press as: M. Panahi, S. Skogestad, Economically efficient operation of CO2 capturing process part I: Self-optimizing procedure for selecting the best controlled variables, Chem. Eng. Process. (2011), doi:10.1016/j.cep.2011.02.0
• Article no : 5813 Author Query Form
• Application Engineering,
• ONLINE OPTIMIZATION AND SELECTION OF MEASUREMENTS
• INTEGRATED OPTIMIZATION AND Marius Stre Govatsmark
• A PARAMETRIC APPROACH TO OPTIMAL OPERATION OF HENs
• PROCESS CONTROLLABILITY ANALYSIS USING LINEAR AND NONLINEAR
• T. Larsson, S. Skogestad, C.C. Yu Control of reactor, separator with recycle. Control of reactor, separator with recycle.
• ADCHEM 2006 International Symposium on Advanced Control of Chemical Processes
• Data reconciliation and optimal operation of a catalytic naphtha reformer
• Chemical Engineering and Processing 43 (2004) 291304 Separation of ternary heteroazeotropic mixtures in a closed
• 8th International IFAC Symposium on Dynamics and Control of Process Systems
• Presented at CHEMDATA 88, Goteborg, Sweden, 1315 June, 1988. DISTURBANCE REJECTION IN DISTILLATION COLUMNS
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• Reduced distillation models via stage aggregation Andreas Linhart
• The setpoint overshoot method: A simple and fast closed-loop approach for PID tuning*
• DistillationTheory.fm 2 September 1999 Distillation Theory.
• STUDIES ON OPTIMAL DESIGN AND OPERATION OF INTEGRATED
• Stabilization of Desired Flow Regimes in E.Storkaas, S. Skogestad # and V. Alstad
• Fundamental limitations for control of unstable SISO K. Havre \Lambda and S. Skogestad y
• A Plantwide Control Procedure with Application to Control Structure Design for a Gas Power Plant
• A PROCEDURE FOR CONTROLLABILITY ANALYSIS Erik A. Wolff, Sigurd Skogestad \Lambda , Morten Hovd and Knut W. Mathisen
• Implementation issues for real-time optimization of a crude unit heat exchanger network
• OPTIMAL OPERATION OF INTEGRATED PROCESSES
• Computerschem. EngngVol.20. No. 4. pp. 373-386,1996 Copyright 1996ElsevierScienceLtd
• DESIGN MODIFICATIONS FOR IMPROVED CONTROLLABILITY
• Coordinator MPC with focus on maximizing Elvira Marie B. Aske a,b
• Convex initialization of the H2-optimal static output feedback problem Henrik Manum, Sigurd Skogestad, and Johannes Jaschke
• Federico Zenith Control of fuel cells
• Available online at www.sciencedirect.com Computers and Chemical Engineering 32 (2008) 195204
• FEEDFORWARD CONTROL UNDER THE PRESENCE OF UNCERTAINTY
• Optimalty of SVD controllers Morten Hovd Richard D. Braatz Sigurd Skogestady
• CONTROLLABILITY OF PROCESSES WITH LARGE Antonio Araujo ,1
• SELECTION OF CONTROL STRUCTURE AND TEMPERATURE LOCATION
• 8th International IFAC Symposium on Dynamics and Control of Process Systems
• Self-optimizing Control and NCO tracking in the Context of Real-Time Optimization
• closed-loop disturbance
• ACHIEVABLE H1PERFORMANCE OF MULTIVARIABLE SYSTEMS WITH UNSTABLE ZEROS AND POLES
• STUDIES ON CONTROLLABILITY ANALYSIS AND CONTROL STRUCTURE DESIGN
• A review of plantwide control Sigurd Skogestad \Lambda and Truls Larsson
• Control of a Industrial Heat Integrated Distillation Column T. Larsson and S. Skogestad
• INTRODUCTION 1.1 Motivation
• PROCESS DESIGN AND CONTROL Temperature Cascade Control of Distillation Columns
• Combination of measurements as controlled variables for self-optimizing control
• Control Structure Selection for Reactor, Separator, and Recycle T. Larsson, M. S. Govatsmark, S. Skogestad,* and C. C. Yu
• CONTROLLABILITY ANALYSIS OF AN UNSTABLE, NON-MINIMUM PHASE
• Selection of Controlled Variables and Robust Setpoints Marius S. Govatsmark and Sigurd Skogestad*
• BK1064-ch03_R2_250706 THE DOS AND DON'TS OF DISTILLATION COLUMN CONTROL
• ADCHEM 2006 International Symposium on Advanced Control of Chemical Processes
• This article was published in an Elsevier journal. The attached copy is furnished to the author for non-commercial research and
• Process Integration Applied to the Design and Operation
• CONTROLLABILITY ANALYSIS PLANTWIDE CONTROL
• An aggregation model reduction method for one-dimensional distributed systems
• M. S. Govatsmark, T. Larsson and S. Skogestad Controllability Analysis and Matlab Software Controllability Analysis and Matlab
• 978-1-4244-2800-7/09/$25.00 2009 IEEE ICIEA 2009 Feedback: Still the simplest and best solution
• Use of Short-cut Methods to Analyse Optimal Operation of Petlyuk Distillation Columns
• Optimal operation of Petlyuk distillation: steady-state behavior Ivar J. Halvorsen1
• MODELING, IDENTIFICATION AND CONTROL, 2000, VOL. 21, NO. 4, 209240 Plantwide control--A review and a new design procedure
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE VECTORS
• Performance limitations for unstable SISO plants Kjetil Havre
• Two Degree of Freedom Controller Design for an Ill-conditioned Distillation Process Using -synthesis
• Self-optimizing control: The basic idea and Taylor series analysis
• SELF-OPTIMIZING CONTROL Sigurd Skogestad Ivar J. Halvorsen John C. Morud
• Multivessel Batch Distillation -Potential Energy Savings
• PARTITIONED PETLYUK ARRANGEMENTS FOR QUATERNARY SEPARATIONS
• Energy Savings in Complex Distillation Arrangements: Importance of Using the Preferred Separation
• LIMITATIONS IMPOSED BY RHP ZEROS/POLES IN MULTIVARIABLE SYSTEMS
• PERFORMANCE LIMITATIONS FOR UNSTABLE SISO Kjetil Havre1 Sigurd Skogestad 2
• Fundamental limitations for control of unstable SISO and S. Skogestady
• Techniques in the Control of Interconnected Plants Morten Hovd
• MULTIVESSEL BATCH DISTILLATION -EXPERIMENTAL VERIFICATION Bernd Wittgens and Sigurd Skogestad1
• POTENTIAL ENERGY SAVINGS OF MULTIVESSEL BATCH DISTILLATION
• SELECTION OF FEEDBACK VARIABLES FOR IMPLEMENTING OPTIMIZING CONTROL SCHEMES K. Havre1, J. Morud and S. Skogestad 2
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE DIRECTIONS.
• CONTROL STRUCTURE DESIGN Sigurd Skogestad
• Computers chem. EngngVol.20, Suppl.,pp. S1041-S1046,1996 Copyright 1996ElsevierScience Ltd
• MULTIVESSEL BATCH DISTILLATION SIGURD SKOGESTAD 1 , BERND WITTGENS, EVA S RENSEN 2
• Presented at CHEMDATA 88, Goteborg, Sweden, 13-15 June, 1988. DISTURBANCE REJECTION IN DISTILLATION COLUMNS
• SHORTCUT MODELS FOR DISTILLATION COLUMNS -I. STEADY-STATE BEHAVIOR
• STUDIES ON CONTROLLABILITY ANALYSIS AND CONTROL STRUCTURE DESIGN
• STUDIES ON CONTROLLABILITY ANALYSIS AND CONTROL STRUCTURE DESIGN
• EXPERIMENTAL VERIFICATION OF DYNAMIC OPERATION OF
• Separation of Azeotropic Mixtures: Tools for Analysis and Studies
• STUDIES ON PLANTWIDE CONTROL Truls Larsson
• process improvements ("optimization")
• inequality path inequality path
• Studies on selection of controlled variables
• Antonio Carlos Brandao de Araujo Studies on Plantwide Control
• CONTROL OF FUEL CELLS Federico Zenith
• Jrgen Bauck Jensen Optimal Operation of Refrigera-
• Journal of Process Control 21 (2011) 976985 Contents lists available at ScienceDirect
• Author's personal copy An industrial and academic perspective on plantwide control
• Control Structure Design for Optimal Operation of 4-Product Thermally Coupled Columns
• 21st European Symposium on Computer Aided Process Engineering ESCAPE 21 E.N. Pistikopoulos, M.C. Georgiadis and A.C. Kokossis (Editors)
• ForReview.Confidential-ACS Plantwide Control to Economic Optimum of a Recycle
• 21st European Symposium on Computer Aided Process Engineering ESCAPE 21 E.N. Pistikopoulos, M.C. Georgiadis and A.C. Kokossis (Editors)
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• Optimal Use of Measurements for Control, Optimization and Estimation
• OPTIMAL CONTROLLED VARIABLE SELECTION FOR INDIVIDUAL PROCESS UNITS IN SELF OPTIMIZING CONTROL
• Optimal Controlled Variable Selection with Structural Constraints Using MIQP
• Self-optimizing Control and NCO tracking in the Context of Real-Time Optimization
• Journal of Cybernetics and Informatics
• European Symposium on Computer Aided Process Engineering ESCAPE20 S. Pierucci and G. Buzzi Ferraris (Editors)
• International Conference February 10 -13, 2010 CYBERNETICS AND INFORMATICS VYSN BOCA, Slovak Republic
• PROCESS DESIGN AND CONTROL Consistent Inventory Control
• Experimental and Theoretical Studies on the Start-Up Operation of a Multivessel Batch Distillation Column
• Optimally Invariant Variable Combinations for Nonlinear Systems
• Optimal Operation of a Waste Incineration Plant for District Heating Johannes Jaschke, Helge Smedsrud, Sigurd Skogestad*, Henrik Manum
• Single-cycle mixed-fluid LNG process Part I: Optimal design
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• Control of the mass and energy dynamics of polybenzimidazole-membrane fuel cells Federico Zenith *, Sigurd Skogestad
• Dynamic Considerations in the Synthesis of Self-Optimizing Control Structures
• 409g Implementation of Coordinator Mpc on a Large-Scale Gas Plant Elvira M. B Aske, Dept. of Chemical Engineering, Norwegian Univ of Sci & Tech (NTNU),
• Hkon Dahl-Olsen, Sridharakumar Narasimhan and Sigurd Skogestad
• Selection of Controlled Variables: Maximum Gain Rule and Combination of Measurements
• 471a Explicit Real-Time Optimization Johannes E. P. Jschke1
• PROCESS SYSTEMS ENGINEERING Control Structure Design for Optimal
• A new approach to explicit MPC using self-optimizing control Henrik Manum, Sridharakumar Narasimhan and Sigurd Skogestad
• A new approach to explicit MPC using self-optimizing control Henrik Manum, Sridharakumar Narasimhan and Sigurd Skogestad
• Explicit MPC with output feedback using self-optimizing control
• This article was published in an Elsevier journal. The attached copy is furnished to the author for non-commercial research and
• Hkon Dahl-Olsen, Sridharakumar Narasimhan and Sigurd Skogestad
• This article was originally published in a journal published by Elsevier, and the attached copy is provided by Elsevier for the
• L1=Q Approach for efficient computation of disturbance rejection measures for feedback control q
• 8th International IFAC Symposium on Dynamics and Control of Process Systems
• A new approach to explicit MPC using self-optimizing control Henrik Manum, Sridharakumar Narasimhan, Sigurd Skogestad
• and 9th International Symposium on Process Systems Engineering W. Marquardt, C. Pantelides (Editors)
• Self-optimizing control configurations for two-product distillation columns Eduardo Shigueo Hori, Sigurd Skogestad*
• Branch and Bound Methods for Control Structure Design Vinay Kariwala
• Tuning for Smooth PID Control with Acceptable Disturbance Rejection Sigurd Skogestad*
• BK1064-ch61_R2_250706 STABILIZING OPERATION OF A 4-PRODUCT INTEGRATED
• PROCESS DESIGN AND CONTROL Offset-Free Tracking of Model Predictive Control with Model
• Controller design for serial processes Audun Faanes 1
• Use of Perfect Indirect Control to Minimize the State Eduardo S. Horia
• Optimal operation of simple vapour compression cycles
• Analysis and Control of Heteroazeotropic Batch Distillation
• Control of a Fuel-Cell Powered DC Electric Vehicle Motor Federico Zenith
• Optimal Operation of a Petlyuk Distillation Column: Energy Savings by Over-fractionating
• Control structure design for complete chemical plants Sigurd Skogestad +
• Computers and Chemical Engineering 28 (2004) 14751487 pH-neutralization: integrated process and control design
• Shortcut Analysis of Optimal Operation of Petlyuk Distillation Ivar J. Halvorsen and Sigurd Skogestad*
• Input performance limitations of feedback control Vinay Kariwala, Sigurd Skogestad, J. Fraser Forbes and Edward S. Meadows
• 02638762/03/$23.50+0.00 # Institution of Chemical Engineers
• Application of a Plantwide Control Design Procedure to a Distillation Column with Heat Pump
• Secondary condenser Cooling water
• IEEE TRANSACTIONS ON AUTOMATIC CONTROL, VOL. 48, NO. 8, AUGUST 2003 1393 Fig. 2. Scalar example. Bound on relative undershoot versus settling time for
• Separation of Azeotropic Mixtures in Closed Batch Distillation Arrangements
• Separation of Azeotropic Mixtures in Closed Batch Distillation Arrangements
• Reactor/separator processes with recycles-2. Design for composition Kwo-Liang Wu a
• z=0 z=0 z=0 Steam-turbin Condenser LP-pump
• Prepared for presentation at ESCAPE 12 symposium. Plantwide control: Towards a systematic procedure
• Stabilization of Desired Flow Regimes in E.Storkaas, S. Skogestad
• Evaluation of self-optimising control structures for an integrated
• PROCESS SYSTEMS ENGINEERING Closed Operation of Multivessel Batch
• MODELING, IDENTIFICATION AND CONTROL, 2000, VOL. 21, NO. 2, 83103 Evaluation of Dynamic Models of Distillation Columns with Emphasis
• ELSEVIER Computers and ChemicalEngineering24 (2000) 1395-1401 Engineering
• ABB Review 4/2000 55 ultiphase pipelines connecting
• Plantwide control: The search for the self-optimizing control structure
• Self-optimizing control of a large-scale plant: The Tennessee Eastman process
• pH-NEUTRALIZATION: INTEGRATED PROCESS AND CONTROL DESIGN
• Plantwide control: the search for the self-optimizing control Sigurd Skogestad *
• SELF-OPTIMIZING CONTROL: A DISTILLATION CASE Sigurd Skogestad
• Computers and Chemical Engineering 24 (2000)569-575 Engineering
• Analysis of Closed Multivessel Batch Distillation of Ternary Azeotropic Mixtures
• 12 IEEE TRANSACTIONS ON CONTROL SYSTEMS TECHNOLOGY, VOL. 7, NO. 1, JANUARY 1999 Two-Degree-of-Freedom Controller Design for an Ill-
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• ACHIEVABLE H1-PERFORMANCE OF MULTIVARIABLE SYSTEMS WITH UNSTABLE ZEROS AND POLES
• Computers and Chemical Engineering 23 (1999) 451455 Supplementary editorial material
• Plantwide control: The search for the self-optimizing control structure
• PLANTWIDE CONTROL Sigurd Skogestad
• PLANTWIDE CONTROL Sigurd Skogestad
• Plantwide control A review and a new design procedure Truls Larsson
• Analysis of instability in an industrial ammonia John C. Morud Sigurd Skogestad
• Indirect on-line optimization through setpoint control Ivar J. Halvorsen1 and Sigurd Skogestad
• Two Degree of Freedom Controller Design for an Ill-conditioned Distillation Process Using -synthesis
• THE USE OF RGA AND CONDITION NUMBER AS ROBUSTNESS MEASURES
• TOTAL REFLUX OPERATION OF MULTIVESSEL BATCH DISTILLATION
• Ind. Eng. Chem. Res. 1996,34, 4395-4405 4396 Multiple Steady States and Instability in Distillation. Implications
• 2094 Ind. Eng. Chem. Res. 1995,34,2094-2103 Operation of Integrated Three-Product(Petlyuk)Distillation
• 2134 Ind. Eng. Chem. Res. 1994,33, 2134-2139 Pairing Criteria for Decentralized Control of Unstable Plants
• Improved independent design of robust decentralized controllers
• TOWARDS INTEGRATING DESIGN AND CONTROL: USE OF FREQUENCY-DEPENDENT TOOLS FOR
• Computers them. Engng, Vol. 14, No. 415, pp. 401413, 1990 Printed in Great Britain.AU rightsreserved
• Ind. Eng. Chem.Res. 1990, 29, 2339-2346 2339 Lewis, W. K.; Gilliland, E. R. Glass Werner, Solid-catalyzedreaction
• Comput. them. Engng,Vol. 11, No. 6, pp. 607-617, 1987 Printed in Great Britain. All rights rescrwd
• 898 Ind. Eng. Chem. Res., Vol. 27, No. 5, 1988 the compounds having a wide range dissociation energies.
• Ind. Eng. Chem. Res. 1987,26, 2323-2330 2323 Greek Symbols
• ROBUST CONTROL OF DISTILLATION COLUMNS Sigurd Skogestad
• Heteroazeotropic Batch Distillation Feasibility and Operation
• Dr.Ing. defense, June 8, 2005 Studies on Selection of Controlled Variables
• EXPERIMENTS OF RISER SLUG FLOW USING TOPSIDE MEASUREMENTS: PART I
• EXPERIMENTS OF RISER SLUG FLOW USING TOPSIDE MEASUREMENTS: PART II
• Elvira Marie B. Aske Design of plantwide control
• Appendix A: ACSL Simulation Model Program 182 AA.. AACCSSLL SSIIMMUULLAATTIIOONN MMOODDEELL
• Appendix B: Formal Measures Analysis -MATLAB Program 198 BB.. FFOORRMMAALL MMEEAASSUURREESS AANNAALLYYSSIISS
• Appendix D: Coal Gasifier Control: A Process Engineering Approach 208 DD.. CCOOAALL GGAASSIIFFIIEERR CCOONNTTRROOLL
• Chapter 2: Literature Review 7 22.. LLIITTEERRAATTUURREE RREEVVIIEEWW
• Chapter 3: Refrigeration Process Control: Case Study Model 42 33.. RREEFFRRIIGGEERRAATTIIOONN PPRROOCCEESSSS
• Chapter 4: Refrigeration Process Control: Simulation Model 64 44.. RREEFFRRIIGGEERRAATTIIOONN PPRROOCCEESSSS
• Chapter 5: Refrigeration Process Control: A Pragmatic Design Approach 75 55.. RREEFFRRIIGGEERRAATTIIOONN PPRROOCCEESSSS
• Chapter 7: Further Insights from Graph Theory 137 77.. FFUURRTTHHEERR IINNSSIIGGHHTTSS FFRROOMM
• Contents iv CCOONNTTEENNTTSS
• Nomenclature 164 NNOOMMEENNCCLLAATTUURREE
• References 170 RREEFFEERREENNCCEESS
• DEVELOPMENT OF CONTROL STRUCTURE DESIGN AND STRUCTURAL CONTROLLABILITY
• Control of Refrigeration Systems for Trade-off between Energy
• Optimal Operation of Kaibel Distillation Columns Maryam Ghadrdan1
• 2010 IFAC International Symposium on Dynamics and Control of Process Systems July 5-7, 2010, Leuven, Belgium
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• Our reference: CES 9052 P-authorquery-v7 AUTHOR QUERY FORM
• Reduced distillation models via stage aggregation Andreas Linhart
• On-Line PI Controller Tuning Using Closed-Loop Setpoint Responses for Stable and Integrating Processes*
• European Symposium on Computer Aided Process Engineering ESCAPE20 S. Pierucci and G. Buzzi Ferraris (Editors)
• Elsevier Editorial System(tm) for Chemical Engineering Research and Design Manuscript Draft
• MEDIUM SCALE EXPERIMENTS ON STABILIZING RISER SLUG FLOW
• UNCORRECTED 2 Optimal measurement combinations as controlled variables
• Elsevier Editorial System(tm) for Journal of Process Control Manuscript Draft
• Local Self-Optimizing Control with Average Loss Minimization Vinay Kariwala
• 10th International Symposium on Process Systems Engineering -PSE2009 Rita Maria de Brito Alves, Claudio Augusto Oller do Nascimento and Evaristo
• Self-consistent inventory control Elvira Marie B. Aske,, and Sigurd Skogestad,
• Steady-state operational degrees of freedom with application to refrigeration cycles
• Single-cycle mixed-fluid LNG process Part I: Optimal design
• A convex formulation of fixed-order linear quadratic control with and without noise
• Control of the mass and energy dynamics of polybenzimidazole-membrane fuel cells
• AIChE Journal Copy of e-mail Notification
• Modeling, Identification and Control, Vol. 29, No. 3, 2008, pp. 103115 Coordinator MPC for maximizing
• Problems with specifying Tmin in design of processes with heat exchangers
• Elsevier Editorial System(tm) for Computers & Chemical Engineering Manuscript Draft
• Application of Plantwide Control to the HDA Process. I -Steady-State Optimization and Self-Optimizing
• Application of Plantwide Control to the HDA Process. II -Regulatory Control
• Selection of control structure and temperature location for two-product distillation Eduardo Shigueo Hori, Sigurd Skogestad*
• MAXIMUM GAIN RULE FOR SELECTING CONTROLLED VARIABLES
• Elsevier Editorial System(tm) for Journal of Process Control Manuscript Draft
• SIMPLE IMPLEMENTATION OF DYNAMIC OPTIMAL Sridharakumar Narasimhan , Sigurd Skogestad ,1
• Submitted to special issue ChERD. This version revised 22 Nov. 2006 The dos and don'ts of distillation column control
• Elsevier Editorial System(tm) for Journal of Process Control Manuscript Draft
• CONTROLLABILITY OF PROCESSES WITH LARGE Sigurd Skogestad ,1
• Offset-free tracking with MPC with model mismatch: Experimental results
• Control Design for Serial Processes Audun Faanes
• Controller Design for Serial Processes Audun Faanes
• Controller Design for Serial Processes Audun Faanes
• Selection of Controlled Variables and Robust Setpoints Marius S. Govatsmark and Sigurd Skogestad
• Optimal Operation of closed cycles for heating and Jrgen B. Jensen Sigurd Skogestad
• ARTICLE IN PRESS Chemical Engineering Science ( )
• Feedforward Control under the Presence of Uncertainty
• MINIMIZATION OF STATE DEVIATIONS USING PERFECT INDIRECT CONTROL
• Integration of optimal operation and control Sigurd SKOGESTAD
• Near-optimal operation by self-optimizing control: From process con-trol to marathon running and business systems
• SEPARATION OF TERNARY HETEROAZEOTROPIC MIXTURES IN A CLOSED MULTIVESSEL BATCH DISTILLATION-DECANTER HYBRID
• Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements
• Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements
• ARTICLE IN PRESS Chemical Engineering Science ( )
• Selection of variables for stabilizing control using pole Kjetil Havre
• Selection of variables for stabilizing control using pole Kjetil Havre
• Self-optimizing control: From key performance indicators to control of biological systems 1
• 0510152025303540 0510152025303540
• Achievable performance of multivariable systems with unstable zeros and poles
• A Systematic Approach to the Design of Buffer Tanks
• EFFECT OF RHP ZEROS AND POLES ON PERFORMANCE IN MULTIVARIABLE SYSTEMS K. Havre 1 and S. Skogestad 2
• Evaluation of selfoptimising control structures for an integrated
• EXPERIMENTAL VERIFICATION OF DYNAMIC OPERATION OF
• STUDIES ON OPTIMAL OPERATION AND CONTROL OF
• 0510152025303540 0510152025303540
• 1. INTRODUCTION The thermally integrated "Petlyuk" arrangement has several appealing features. For the separation of a three-compo-
• Control of fuel cell power output Federico Zenith, Sigurd Skogestad *
• Forpeerreview Control structure design for optimal operation of
• Self-optimizing control of a large-scale plant: The Tennessee Eastman process
• Minimum Energy for the four-product Kaibel-column Ivar J. Halvorsen, SINTEF, Norway and Sigurd Skogestad, NTNU, Norway
• Anti-slug control experiments on a small-scale two-phase Heidi Sivertsen and Sigurd Skogestad
• Computers and Chemical Engineering xxx (2003) xxxxxx Control structure design for complete chemical plants
• To: Editorial office, Computers and Chemical Engineering From: Sigurd Skogestad
• DYNAMICS AND CONTROL OF DISTILLATION COLUMNS -A CRITICAL SURVEY
• Modelling and Control of Activated Sludge Processes
• Optimized Control Structure for a Wastewater Treatment Benchmark
• Industrial Implementation of a Coordinator MPC for Maximizing Throughput at a
• Computational approach for adjudging Feasibility of Acceptable Disturbance Rejection Vinay Kariwala and Sigurd Skogestad
• Selfoptimizing control: Basis issues and Taylor series analysis
• A Method for Selection of Controlled Variables and Robust Setpoints
• selfoptimizing Engineering
• PARTITIONED PETLYUK ARRANGEMENTS FOR QUATERNARY SEPARATIONS
• Two Degree of Freedom Controller Design for an Illconditioned Distillation Process Using synthesis
• Integrated Design, Operation and Control of Batch Extractive Distillation with a Middle Vessel
• 654 Ind. Eng. Chem. Res. 1991,30,654-661 PROCESS ENGINEERING AND DESIGN
• Limit cycles with imperfect valves: Implications for controllability of processes with large gains
• Int. J. Automation and Control, Vol. 1, No. 4, 2007 295 -Interaction measure for unstable systems
• Computerschem.EngngVol. 20, No. 12, pp. 1491-1498,1996 Pergamon Copyright 1996ElsevierScienceLtd
• Computers and Chemical Engineering 29 (2004) 127137 Near-optimal operation by self-optimizing control: from process
• Buffer Tank Design for Acceptable Control Performance Audun Faanes and Sigurd Skogestad*
• T. Larsson, S. Skogestad, C.C. Yu Control of reactor, separator with recycle. Control of reactor, separator with recycle.
• Bilevel programming for analysis of low-complexity control of linear systems with constraints
• Time scale separation and the link between open-loop and closed-loop dynamics
• Chemical Engineering Science 58 (2003) 19031953 www.elsevier.com/locate/ces
• Control Engineering Practice ] (]]]]) ]]]]]] Controllability analysis of two-phase pipeline-riser systems at riser
• CASCADE CONTROL EXPERIMENTS OF RISER SLUG FLOW USING TOPSIDE MEASUREMENTS
• Computers and Chemical Engineering 31 (2007) 712721 Optimal operation of simple refrigeration cycles
• Optimal operation of a Petlyuk Distillation Column: Energy Savings by Over-fractionation
• The null space method for selecting optimal measurement combinations as controlled
• Problems with Specifying Tmin in the Design of Processes with Heat Exchangers Jrgen Bauck Jensen and Sigurd Skogestad*
• ANALYSIS AND CONTROL OF DISTILLATION COLUMNS Sigurd Skogestad, Chem. Eng., Norwegian Inst. of Tech. (NTH), N-7034 Trondheim, Norway
• ADCHEM 2006 International Symposium on Advanced Control of Chemical Processes
• European Symposium on Computer Aided Process Engineering ESCAPE20 S. Pierucci and G. Buzzi Ferraris (Editors)
• Optimal Output Selection for Control of Batch Processes Hkon Dahl-Olsen, Sridharakumar Narasimhan and Sigurd Skogestad
• Optimal Operation of a Waste Incineration Plant for District Heating Johannes Jaschke, Helge Smedsrud, Sigurd Skogestad*, Henrik Manum
• CLOSED OPERATION OF MULTIVESSEL BATCH DISTILLATION -EXPERIMENTAL VERIFICATION
• STUDIES ON MODELING AND CONTROL OF CONTINUOUS BIOTECHNICAL PROCESSES
• OPTIMAL STARTUP PROCEDURES FOR BATCH DISTILLATION E. SRENSEN 2 AND S. SKOGESTAD 1
• Two Degree of Freedom Controller Design for an Illconditioned Distillation Process Using synthesis
• Probably the best simple PID tuning rules in the world Sigurd Skogestad
• Selfoptimizing control of a largescale plant: The Tennessee Eastman process
• INPUT OUTPUT SELECTION AND PARTIAL CONTROL Kjetil Havre1 and Sigurd Skogestad2
• Control Engineering Practice 15 (2007) 12221237 Application of plantwide control to the HDA process. I--steady-state
• Self-consistent inventory control Elvira Marie B. Aske,, and Sigurd Skogestad,
• Control and optimal operation of simple heat pump cycles Jrgen B. Jensen and Sigurd Skogestad
• AICHE Annual Meeting, Washington DC, Nov. 1988 VARIABLE SELECTION FOR DECENTRALIZED CONTROL
• Economically Efficient Operation of CO2 Capturing Process Part I: Self-optimizing Procedure for Selecting the Best Controlled Variables
• Azeotropic Phase Equilibrium Diagrams: , E. K. Hilmen
• Explicit MPC with output feedback using self-optimizing control
• DYCOPS-5 Symposium: Corfu, Greece, June 8-10, 1998 1. INTRODUCTION
• Selection of variables for stabilizing control using pole Kjetil Havre
• Computers and Chemical Engineering 28 (2004) 829837 Time (energy) requirements in closed batch distillation arrangements
• Computers and Chemical Engineering 28 (2004) 683691 Selecting appropriate control variables for a heat-integrated
• 10th International Symposium on Process Systems Engineering -PSE2009 Rita Maria de Brito Alves, Claudio Augusto Oller do Nascimento and Evaristo
• A Comparative Analysis of Numerical Methods for Solving Systems of Nonlinear Algebraic Equations
• Integrated Column Designs for Minimum Energy and Entropy Requirements in Multicomponent Distillation
• Ind. Eng. Chem. Res. 1994,33, 631-640 631 PROCESS DESIGN AND CONTROL
• PROCESS DESIGN AND CONTROL Comparison of Various Control Configurations for Continuous
• The null space method for selecting optimal measurement combinations as controlled
• Analysis of Instability in an Industrial Ammonia Reactor
• T. Larsson, S. Skogestad Control of a industrial heat integrated distillation column Control of a industrial
• MIQP formulation for Controlled Variable Selection in Self Optimizing Control Ramprasad Yelchuru*, Sigurd Skogestad*, Henrik Manum*
• POTENTIAL ENERGY SAVINGS OF MULTIVESSEL BATCH DISTILLATION
• On-line optimization of a crude unit heat exchanger Statoil Mongstad
• TOTAL REFLUX OPERATION OF MULTIVESSEL BATCH DISTILLATION
• SELECTION OF VARIABLES FOR REGULATORY CONTROL USING POLE VECTORS
• Analysis of Closed Multivessel Batch Distillation of Ternary Azeotropic Mixtures
• MULTIVESSEL BATCH DISTILLATION 1 SIGURD SKOGESTAD 2 , BERND WITTGENS,
• STUDIES ON ROBUST MULTIVARIABLE DISTILLATION CONTROL
• Optimalty of SVD controllers Morten Hovd Richard D. Braatz \Lambda Sigurd Skogestad y
• Probably the best simple PID tuning rules in the world Sigurd Skogestad
• THE DYNAMIC BEHAVIOR OF CASCADE PROCESSES --WITH APPLICATION TO DISTILLATION COLUMNS
• Implementation issues for realtime optimization of a crude unit heat exchanger network
• Indirect online optimization through setpoint control Ivar J. Halvorsen 1 and Sigurd Skogestad
• CONTROLLABILITY Controllability
• Effect of Varying Controller Parameters in Closed-Loop Subspace Identification
• DIRECTIONS AND FACTORIZATIONS OF ZEROS AND POLES IN MULTIVARIABLE SYSTEMS
• Self-Optimizing Control of a Large-Scale Plant: The Tennessee Eastman Process
• ~ UTT E RWORTH El N E M A N N
• Limits of Disturbance Rejection for Indirect Control Vinay Kariwala and Sigurd Skogestad
• Model Predictive Control of a Kaibel Distillation Column
• Can the Operating Leaves of a Distillation Column Really Be Tshepo S. Modise, Michaela Tapp, Diane Hildebrandt,* and David Glasser
• STUDIES ON THE DYNAMICS AND OPERATION
• A SYSTEMATIC APPROACH TO DISTILLATION COLUMN CONTROL Sigurd Skogestad \Lambda
• Online optimization and choice of optimization variables for control of heat exchanger networks
• SELECTION OF FEEDBACK VARIABLES FOR IMPLEMENTING OPTIMIZING CONTROL SCHEMES K. Havre 1 , J. Morud and S. Skogestad 2
• Studies on selection of controlled variables
• Plantwide control --A review and a new design procedure Truls Larsson and Sigurd Skogestad y
• Truls Larsson, Sigurd Skogestad Introduction to MPC Introduction to MPC
• @o/oohyh#v' 's +rys#'f#vv+vt p'#...'y +#...p#...r+ s'... h v#rt...h#rq Qr#y'x
• AICHE Annual Meeting, Washington DC, Nov. 1988 VARIABLE SELECTION FOR DECENTRALIZED CONTROL
• ROBUST MULTIVARIABLE CONTROL USING H 1 METHODS
• CONTROLLABILITY MEASURES FOR DISTURBANCE Sigurd Skogestad \Lambda and Erik A. Wolff
• Pergamon Chemical Engineering Science, Vol. 51, No. 22, pp. 4949 4962, 1996 Copyright 1996 Elsevier Science Ltd
• Single-cycle mixed-fluid LNG process Part II: Optimal operation
• chemical engineering research and design 8 8 ( 2 0 1 0 ) 213228 Contents lists available at ScienceDirect
• Control structure selection for the deethanizer column from Mongstad/Statoil
• Automaaca, Vol.30.No.6. pp. 957-973.1994 CopyrightC) 1994ElsevierScienceLtd
• Achievable performance of multivariable systems with unstable zeros and poles K. HAVRE{{ and S. SKOGESTAD{*
• Limitations imposed by lower layer control configurations. Truls Larsson and Sigurd Skogestad
• Computerscheat.Engng,Vol. 21, Suppl., pp. $249-$254, 1997 Pergamon ~ 1997 Elsevier Science Ltd
• A SYSTEMATIC APPROACH TO DISTILLATION COLUMN CONTROL Sigurd Skogestad
• STABILIZING CONTROL AND CONTROLLABILITY
• On the Trade-off between Energy Consumption and Food Quality Loss in Supermarket Refrigeration Systems
• Application of Plantwide Control to the HDA Process. IIsRegulatory Control Antonio C. B. de Araujo, Eduardo S. Hori, and Sigurd Skogestad*
• Coordinator MPC with focus on maximizing throughput E.M.B. Askeab
• PROCESS DESIGN AND CONTROL Perfect Steady-State Indirect Control
• THE DOS AND DONTS OF DISTILLATION COLUMN CONTROL
• Computers and Chemical Engineering xxx (2004) xxxxxx Time requirements for heteroazeotropic distillation in batch columns
• Computers and Chemical Engineering 28 (2004) 16891700 Time requirements for heteroazeotropic distillation in batch columns
• COMBINATIONS OF MEASUREMENTS AS CONTROLLED VARIABLES: APPLICATION
• On-line optimization and choice of optimization variables for control of heat exchanger networks
• Ind. Eng. Chem. Res. 1991,30, 2555-2564 2555 Presence of Persistent Unknown Disturbances. AZChE J. 1980,
• Ind. Eng. Chem. Res. 1991,30,2019-2020 2019 where the Pk(xl)are defined as follows
• Ind. Eng. Chem. Res. 1987,26, 2029-2035 2029 Effect of Disturbance Directions on Closed-Loop
• Identification of Low Order Models for Large Scale Processes
• THROUGHPUT MAXIMIZATION BY IMPROVED BOTTLENECK CONTROL
• Control and optimal operation of simple heat pump cycles
• Draft -/home/ivarh/thesis/book/DistillationTheory_ch.fm Version: 11 August 2000
• Effect of Varying Controller Parameters in Closed-Loop Subspace Identification
• Ind. Eng. Chem. Res. 1991,30, 2543-2555 2543 PROCESS ENGINEERING AND DESIGN
• Optimized Control Structure for a Wastewater Treatment Benchmark
• Minimum Energy Diagrams for Multieffect Distillation Arrangements
• Stabilization of severe slugging based on a low-dimensional nonlinear model
• PERFORMANCE LIMITATIONS FOR UNSTABLE SISO Kjetil Havre 1 Sigurd Skogestad 2
• A Systematic Approach to the Design of Buffer Tanks
• DESIGN MODIFICATIONS FOR IMPROVED CONTROLLABILITY
• Engineering Introduction
• Plantwide control: The search for the selfoptimizing control structure
• European Symp. on Computer Application in the Chemical Industry, Erlangen, 23 26 April, 1989
• Achievable performance of multivariable systems with unstable zeros and poles
• INTEGRATED DESIGN AND CONTROL OF HEAT EXCHANGER NETWORKS
• An aggregation model reduction method for one-dimensional distributed systems.
• Chemical Engineers Science. Vol. 42, No. 7, pp. 1765-1780. 1987. OWXJ-2509/87 S3.00+0.00 Primed in Great Britain. 8 1987 Pergamon Journals Ltd.
• Author's personal copy Optimal measurement combinations as controlled variables
• Norwegian University of Science and Technology
• Condenser Cooling water 8 9 10 11 12
• SVD Controllers for H2-, H1-, and -Optimal Morten Hovd
• IMC-like Analytical H design with S/SP mixed sensitivity consideration: Utility in PID tuning guidance6
• This article was published in an Elsevier journal. The attached copy is furnished to the author for non-commercial research and
• Computerschem.EngngVol.20, Suppl.,pp. S1257-S1262,1996 Copyright 1996ElsevierScience Ltd
• Control structure design: New developments and future directions Vinay Kariwala and Sigurd Skogestad
• Chapter 6: Refrigeration Process Control: A Formal Design Approach 111 66.. RREEFFRRIIGGEERRAATTIIOONN PPRROOCCEESSSS
• Optimally Invariant Variable Combinations for Nonlinear Systems
• THE DYNAMICS OF CHEMICAL REACTORS WITH HEAT INTEGRATION
• EXPERIMENTAL SIMULATION OF DISTILLATION COLUMN PROFILE MAPS
• A New Approach to Explicit MPC Using Self-Optimizing Control
• Complex Distillation Arrangements 23.May 2001 by I.Halvorsen NTNU Department of Chemical Engineering
• DistillationTheory.fm 2 September 1999 Distillation Theory.
• MULTIVESSEL BATCH DISTILLATION EXPERIMENTAL VERIFICATION
• 1. INTRODUCTION The thermally integrated ``Petlyuk'' arrangement has several appealing features. For the separation of a threecompo
• SHORTCUT MODELS FOR DISTILLATION COLUMNS I. STEADYSTATE BEHAVIOR
• Control structure selection for Reactor, Separator and Recycle Process
• TOWARDS INTEGRATING DESIGN AND CONTROL: USE OF FREQUENCYDEPENDENT TOOLS FOR
• Complex Distillation Arrangements : Extending the Petlyuk Ideas
• Multivessel Batch Distillation Potential Energy Savings
• Control structure selection of a deethanizer column with partial condenser Proceedings of European Congress of Chemical Engineering (ECCE-6)
• Tuning PI controllers based on H Weighted Sensitivity S. Alcntara, S. Skogestad, C. Grimholt, C. Pedret, R. Vilanova
• 1 Introduction 5 2 Distillation control (will place this in other chapters) 7
• Johannes Jschke Invariants for Optimal Operation
• Active constraint regions for optimal operation of chemical processes -Part I: Application to a
• NCO tracking and Self-optimizing Control in the Context of Real-Time Optimization
• Self-optimizing Invariants in Dynamic Optimization Johannes Jaschke, Miroslav Fikar and Sigurd Skogestad
• Active constraint regions for optimal operation of chemical processes -Part II: Application to
• Energy efficient distillation Ivar J. Halvorsen a,*, Sigurd Skogestad b
• Magnus Glosli Jacobsen Identifying active constraint re-
• Introduction and goals H Weighted Sensitivity Getting the PI tuning rules Tuning guidelines and examples Conclusions Tuning PI controllers based on
• chemical engineering research and design 8 9 ( 2 0 1 1 ) 11551167 Contents lists available at ScienceDirect
• 1 Generalized Internal Model Control for Balancing Input/Output 2 Disturbance Response
• Universitat Autnoma de Barcelona Analytical design of feedback
• Published: July 12, 2011 r 2011 American Chemical Society 10093 dx.doi.org/10.1021/ie200706d |Ind. Eng. Chem. Res. 2011, 50, 1009310101
• Published: August 11, 2011 r 2011 American Chemical Society 11170 dx.doi.org/10.1021/ie200717z |Ind. Eng. Chem. Res. 2011, 50, 1117011180
• P1: TIX/XYZ P2: ABC JWST135-c11 JWST135-Rangaiah November 14, 2011 9:28 Printer: Yet to come
• An Aggregation Model Reduction Method for One-Dimensional Distributed Systems
• Published: June 10, 2011 r 2011 American Chemical Society 8571 dx.doi.org/10.1021/ie1024358 |Ind. Eng. Chem. Res. 2011, 50, 85718584
• Application of Balanced Truncation to Nonlinear Ivan Dones *, Sigurd Skogestad +1
• Optimization of Low-Level Controllers and High-Level Polymer Grade Changes
• Analytical design of feedback compensators based on Robustness/Performance and
• Active constraint regions for optimal operation of distillation columns
• Optimal Controlled Variables for Polynomial Systems Johannes Jaschke, Sigurd Skogestad
• Economically Efficient Operation of CO2 Capturing Process Part II: Control Layer
• Active constraint regions for optimal operation of distillation columns
• Published: November 17, 2011 r 2011 American Chemical Society 425 dx.doi.org/10.1021/ie2014058 |Ind. Eng. Chem. Res. 2012, 51, 425433
• Optimal PI-Control and Verification of the SIMC Tuning Rule
• Quantitative methods for Regulatory layer selection Ramprasad Yelchuru, Sigurd Skogestad
• 1M. Panahi, S. Skogestad ' Optimal Operation of a CO2 Capturing Plant for a Wide Range of Disturbances' Optimal Operation of a CO2 Capturing
• Economically Efficient Operation of CO2 Capturing Process Part II: Control Layer
• Published: August 07, 2011 r 2011 American Chemical Society 11226 dx.doi.org/10.1021/ie2012196 |Ind. Eng. Chem. Res. 2011, 50, 1122611236
• Tuning PI controllers based on H Weighted Sensitivity S. Alcntara, S. Skogestad, C. Grimholt, C. Pedret, R. Vilanova
• Self-optimizing Invariants in Dynamic Optimization Johannes Jaschke, Miroslav Fikar and Sigurd Skogestad
• Title ? First A. AuthorS*econd B. Author, Jr. **
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Controlled Variables Selection for a Gas-to-Liquids Process
• Optimal Controlled Variable Selection with Structural Constraints Using MIQP
• Ramprasad Yelchuru Quantitative methods for
• 1M. Panahi, S. Skogestad ' Controlled Variables Selection for a Natural Gas to Liquids (GTL) process' Controlled Variables Selection for a
• Optimal Controlled Variables for Polynomial Systems Johannes Jaschke, Sigurd Skogestad
• Journal of Process Control 21 (2011) 14071416 Contents lists available at ScienceDirect
• P1: TIX/XYZ P2: ABC JWST135-c11 JWST135-Rangaiah November 14, 2011 9:28 Printer: Yet to come
• Chemical Engineering and Processing 52 (2012) 112124 Contents lists available at SciVerse ScienceDirect
• NCO tracking and Self-optimizing Control in the Context of Real-Time Optimization
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Loss Method: A Static Estimator Applied for Product Composition Estimation
• An aggregation model reduction method for one-dimensional distributed parameter systems
• Optimal Controlled Variable Selection with Structural Constraints Using MIQP
• This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research
• NCO tracking and Self-optimizing Control in the Context of Real-Time Optimization
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Optimal Design of Energy-Efficient Integrated Distillation Processes for
• Self-optimizing Invariants in Dynamic Optimization Johannes Jaschke, Miroslav Fikar and Sigurd Skogestad
• Measurement Polynomials as Controlled Johannes Jaschke, Sigurd Skogestad
• An aggregation model reduction method for one-dimensional distributed systems
• Simplified Dynamical Models for Control of Severe Slugging in Multiphase Risers Esmaeil Jahanshahi. Sigurd Skogestad
• 21st European Symposium on Computer Aided Process Engineering ESCAPE 21 E.N. Pistikopoulos, M.C. Georgiadis and A.C. Kokossis (Editors)
• The SIMC method for smooth PID controller Sigurd Skogestad and Chriss Grimholt
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Optimal Operation of a CO2 Capturing Plant for a Wide Range of Disturbances
• Measurement polynomials as controlled variables Exercises
• Multi-Product Dividing Wall Columns: A Simple and Effective Assessment and Conceptual Design Procedure
• OPTIMAL CONTROLLED VARIABLE SELECTION FOR INDIVIDUAL PROCESS UNITS IN SELF OPTIMIZING CONTROL
• Optimal Operation by Controlling the Gradient to Zero
• O c t O b e r / 2 0 11 www.controlglobal.com 47 D i s t r i b u t e D C o n t r o l
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Active Constraint Regions for Economically Optimal Operation of Distillation
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Active Vapor Split Control for Fully Coupled Columns: Experimental Studies
• Active constraint regions for optimal operation of chemical processes -Part I: Application to a
• AUTHOR'SPROOF Book ID: 300199_1_En, Date: 2012-01-09, Proof No: 1, UNCORRECTED PROOF
• An Aggregation Model Reduction Method for One-Dimensional Distributed Systems
• Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler Optimal Measurement Selection for Controlled Variables for Kaibel Distillation