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Optimal PI and PID control of first-order plus delay processes and evaluation of the original and improved SIMC rules

Journal of process control, 2018-10, Vol.70, p.36-46

2018

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Simple analytic rules for model reduction and PID controller tuning

Journal of process control, 2003-06, Vol.13 (4), p.291-309

Skogestad, Sigurd

2003

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Simple analytic rules for model reduction and PID controller tuning

Modeling, identification and control, 2004-04, Vol.25 (2), p.85-120

SKOGESTAD, Sigurd

2004

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Plantwide control - A review and a new design procedure

Modeling, identification and control, 2000-10, Vol.21 (4), p.209-240

2000

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Optimal measurement combinations as controlled variables

Journal of process control, 2009, Vol.19 (1), p.138-148

2009

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An industrial and academic perspective on plantwide control

Annual reviews in control, 2011-04, Vol.35 (1), p.99-110

2011

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Controllability analysis of two-phase pipeline-riser systems at riser slugging conditions

Control engineering practice, 2007-05, Vol.15 (5), p.567-581

2007

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Dynamics and control of distillation columns : a critical survey

Modeling, identification and control, 1997-07, Vol.18 (3), p.177-217

SKOGESTAD, S

1997

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Optimal Operation of Heat Exchanger Networks with Changing Active Constraint Regions

Computer Aided Chemical Engineering, 2022, Vol.49, p.421-426

2022

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Small-scale experiments on stabilizing riser slug flow

Chemical engineering research & design, 2010-02, Vol.88 (2), p.213-228

2010

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Changing between Active Constraint Regions for Optimal Operation: Classical Advanced Control versus Model Predictive Control

Computer Aided Chemical Engineering, 2018, Vol.43, p.1015-1020

2018

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Comparison of Simple Feedback Control Structures for Constrained Optimal Operation

IFAC-PapersOnLine, 2022, Vol.55 (7), p.883-888

2022

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Optimal operation of simple refrigeration cycles

Computers & chemical engineering, 2007-05, Vol.31 (5), p.712-721

2007

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Economic back-off selection based on optimal multivariable controller

IFAC Proceedings Volumes, 2012, Vol.45 (15), p.792-797

2012

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Transformed Manipulated Variables for Linearization, Decoupling and Perfect Disturbance Rejection

IFAC-PapersOnLine, 2020, Vol.53 (2), p.4052-4057

2020

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Optimal Operation with Changing Active Constraint Regions using Classical Advanced Control⁎⁎This work was partly supported by the Norwegian Research Council under HighEFF (Centre for an Energy Efficient and Competitive Industry for the Future)

IFAC-PapersOnLine, 2018, Vol.51 (18), p.440-445

2018

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Systematic Design of Split Range Controllers

IFAC-PapersOnLine, 2019, Vol.52 (1), p.898-903

2019

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Systematic Design of Split Range Controllers ⁎⁎This work is partly funded by HighEFF – Centre for an Energy Effcient and Competitive Industry for the Future. The authors gratefully acknowledge the financial support from the Research Council of Norway and user partners of HighEFF, an 8 year Research Centre under the FME-scheme (Centre for Environment-friendly Energy Research, 257632/E20)

IFAC-PapersOnLine, 2019, Vol.52 (1), p.898-903

2019

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Feedforward Control under the Presence of Uncertainty

European journal of control, 2004, Vol.10 (1), p.30-46

2004

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Optimal Operation with Changing Active Constraint Regions using Classical Advanced Control

IFAC-PapersOnLine, 2018, Vol.51 (18), p.440-445

2018

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Improved PI control for a surge tank satisfying level constraints⁎⁎This work was supported in part by the Norwegian Research Council under the project SUBPRO (Subsea production and processing)

IFAC-PapersOnLine, 2018, Vol.51 (4), p.835-840

2018

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Two-degree-of-freedom controller design for an ill-conditioned distillation process using μ-synthesis

IEEE transactions on control systems technology, 1999, Vol.7 (1), p.12-21

1999

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Optimal selection of sensor network and backed-off operating point based on economics

2013 European Control Conference (ECC), 2013, p.4472-4477

2013

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IEEE_Xplore

Temperature Cascade Control of Distillation Columns

Industrial & engineering chemistry research, 1996-02, Vol.35 (2), p.475-484

1996

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Lower Limit on Controller Gain for Acceptable Disturbance Rejection

IFAC Proceedings Volumes, 2004-01, Vol.37 (1), p.499-503

Skogestad, Sigurd

2004

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Optimal PI and PID control of first-order plus delay processes and evaluation of the original and improved SIMC rules

Simple analytic rules for model reduction and PID controller tuning

Simple analytic rules for model reduction and PID controller tuning

Plantwide control - A review and a new design procedure

Optimal measurement combinations as controlled variables

An industrial and academic perspective on plantwide control

Controllability analysis of two-phase pipeline-riser systems at riser slugging conditions

Dynamics and control of distillation columns : a critical survey

Optimal Operation of Heat Exchanger Networks with Changing Active Constraint Regions

Small-scale experiments on stabilizing riser slug flow

Changing between Active Constraint Regions for Optimal Operation: Classical Advanced Control versus Model Predictive Control

Comparison of Simple Feedback Control Structures for Constrained Optimal Operation

Optimal operation of simple refrigeration cycles

Economic back-off selection based on optimal multivariable controller

Transformed Manipulated Variables for Linearization, Decoupling and Perfect Disturbance Rejection

Optimal Operation with Changing Active Constraint Regions using Classical Advanced Control⁎⁎This work was partly supported by the Norwegian Research Council under HighEFF (Centre for an Energy Efficient and Competitive Industry for the Future)

Systematic Design of Split Range Controllers

Feedforward Control under the Presence of Uncertainty

Optimal Operation with Changing Active Constraint Regions using Classical Advanced Control

Improved PI control for a surge tank satisfying level constraints⁎⁎This work was supported in part by the Norwegian Research Council under the project SUBPRO (Subsea production and processing)

Two-degree-of-freedom controller design for an ill-conditioned distillation process using μ-synthesis

Optimal selection of sensor network and backed-off operating point based on economics

Temperature Cascade Control of Distillation Columns

Lower Limit on Controller Gain for Acceptable Disturbance Rejection

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