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Primal–dual feedback-optimizing control with override for real-time optimization

Journal of process control, 2024-06, Vol.138, Article 103208

2024

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A Rigorous Model for Evaluating Moving Window Soft Sensors for Industrial Distillation Processes

Chemical engineering transactions, 2018-10, Vol.69

2018

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Dividing Wall Columns for Natural Gas Liquefaction Plants

Chemical engineering transactions, 2018-10, Vol.69

2018

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Operation of Integrated Three-Product (Petlyuk) Distillation Columns

Industrial & engineering chemistry research, 1995-06, Vol.34 (6), p.2094-2103

1995

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Correction to “Systematic Design of Active Constraint Switching Using Classical Advanced Control Structures”

Industrial & engineering chemistry research, 2020-05, Vol.59 (19), p.9342-9342

2020

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Optimal operation of heat exchanger networks with stream split: Only temperature measurements are required: Manfred Morari Special Issue

Computers & chemical engineering, 2014, Vol.70, p.35-49

2014

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Decentralized control for optimal operation under changing active constraints

Computer Aided Chemical Engineering, 2023, Vol.52, p.1699-1704

2023

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Input transformation for linearization, decoupling and disturbance rejection with application to steam networks

Computer Aided Chemical Engineering, 2021, Vol.50, p.1021-1027

2021

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Complex distillation arrangements: Extending the petlyuk ideas

Computers & chemical engineering, 1997, Vol.21, p.S237-S242

1997

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Problems with Specifying ΔTmin in the Design of Processes with Heat Exchangers

Industrial & engineering chemistry research, 2008-05, Vol.47 (9), p.3071-3075

2008

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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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Economically efficient operation of CO 2 capturing process part I: Self-optimizing procedure for selecting the best controlled variables

Chemical engineering and processing, 2011, Vol.50 (3), p.247-253

2011

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A comparative study of distributed feedback-optimizing control strategies

Computer Aided Chemical Engineering, 2023, Vol.52, p.613-618

2023

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A Sensory-Motor Control Model of Animal Flight Explains Why Bats Fly Differently in Light Versus Dark: e1002046

PLoS biology, 2015-01, Vol.13 (1)

2015

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Identification and analysis of possible splits for azeotropic mixtures. 2. Method for simple columns

Chemical engineering science, 2012, Vol.69 (1), p.159-169

2012

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Multiple steady states in ideal two-product distillation

AIChE journal, 1991-04, Vol.37 (4), p.499-511

1991

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Problems with Specifying ∇Tmin in the Design of Processes with Heat Exchangers

Industrial & engineering chemistry research, 2008, Vol.47 (9), p.3071-3075

2008

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Necessary and sufficient conditions for robust reliable control in the presence of model uncertainties and system component failures: Manfred Morari Special Issue

Computers & chemical engineering, 2014, Vol.70, p.67-77

2014

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Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column

Industrial & engineering chemistry research, 2003-02, Vol.42 (3), p.596-604

2003

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Approach for efficient computation of disturbance rejection measures for feedback control

Journal of process control, 2007-07, Vol.17 (6), p.501-508

2007

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Corrections and comments from the author on the paper “Simple analytic rules for model reduction and PID controller tuning”, Journal of Process Control 13 (2003) 291–309

Journal of process control, 2004-06, Vol.14 (4), p.465-465

Skogestad, Sigurd

2004

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Identification and analysis of possible splits for azeotropic mixtures—1. Method for column sections

Chemical engineering science, 2011, Vol.66 (12), p.2512-2522

2011

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Optimal operation of simple refrigeration cycles

Computers & chemical engineering, 2007-12, Vol.31 (12), p.1590-1601

2007

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Control structure designfora CO2 -refrigeration system with heat recovery

Computer Aided Chemical Engineering, 2019, Vol.46, p.1243-1248

2019

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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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Primal–dual feedback-optimizing control with override for real-time optimization

A Rigorous Model for Evaluating Moving Window Soft Sensors for Industrial Distillation Processes

Dividing Wall Columns for Natural Gas Liquefaction Plants

Operation of Integrated Three-Product (Petlyuk) Distillation Columns

Correction to “Systematic Design of Active Constraint Switching Using Classical Advanced Control Structures”

Optimal operation of heat exchanger networks with stream split: Only temperature measurements are required: Manfred Morari Special Issue

Decentralized control for optimal operation under changing active constraints

Input transformation for linearization, decoupling and disturbance rejection with application to steam networks

Complex distillation arrangements: Extending the petlyuk ideas

Problems with Specifying ΔTmin in the Design of Processes with Heat Exchangers

Optimal Operation of Heat Exchanger Networks with Changing Active Constraint Regions

Economically efficient operation of CO 2 capturing process part I: Self-optimizing procedure for selecting the best controlled variables

A comparative study of distributed feedback-optimizing control strategies

A Sensory-Motor Control Model of Animal Flight Explains Why Bats Fly Differently in Light Versus Dark: e1002046

Identification and analysis of possible splits for azeotropic mixtures. 2. Method for simple columns

Multiple steady states in ideal two-product distillation

Problems with Specifying ∇Tmin in the Design of Processes with Heat Exchangers

Necessary and sufficient conditions for robust reliable control in the presence of model uncertainties and system component failures: Manfred Morari Special Issue

Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column

Approach for efficient computation of disturbance rejection measures for feedback control

Corrections and comments from the author on the paper “Simple analytic rules for model reduction and PID controller tuning”, Journal of Process Control 13 (2003) 291–309

Identification and analysis of possible splits for azeotropic mixtures—1. Method for column sections

Optimal operation of simple refrigeration cycles

Control structure designfora CO2 -refrigeration system with heat recovery

Optimal operation of simple refrigeration cycles

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