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The Dos and Don’ts of Distillation Column Control

Chemical engineering research & design, 2007, Vol.85 (1), p.13-23

Skogestad, S.

2007

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Model predictive control for the self-optimized operation in wastewater treatment plants: Analysis of dynamic issues

Computers & chemical engineering, 2015-11, Vol.82, p.259-272

2015

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Internal configurations for a multi-product dividing wall column

Chemical engineering research & design, 2013-10, Vol.91 (10), p.1954-1965

2013

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Designing four-product dividing wall columns for separation of a multicomponent aromatics mixture

Chemical engineering research & design, 2011-08, Vol.89 (8), p.1155-1167

2011

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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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Thermal coupling opportunities for floating natural gas liquefaction plants

Chemical engineering research & design, 2019-07, Vol.147, p.346-353

2019

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Azeotropic phase equilibrium diagrams: a survey

Chemical Engineering Science, 2003-05, Vol.58 (10), p.1903-1953

2003

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Generalized Internal Model Control for Balancing Input/Output Disturbance Response

Industrial & engineering chemistry research, 2011-10, Vol.50 (19), p.11170-11180

2011

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Control structure design for complete chemical plants

Computers & chemical engineering, 2004-01, Vol.28 (1), p.219-234

Skogestad, Sigurd

2004

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Feasible separations and entrainer selection rules for heteroazeotropic batch distillation

Chemical engineering science, 2005-06, Vol.60 (11), p.2895-2909

2005

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Selecting appropriate control variables for a heat-integrated distillation system with prefractionator

Computers & chemical engineering, 2004-05, Vol.28 (5), p.683-691

2004

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Plantwide control: the search for the self-optimizing control structure

Journal of process control, 2000, Vol.10 (5), p.487-507

Skogestad, Sigurd

2000

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Feedback: Still the Simplest and Best Solution

Modeling, identification and control, 2009-01, Vol.30 (3), p.149-155

Skogestad, S.

2009

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Selection of Control Structure and Temperature Location for Two-Product Distillation Columns

Chemical engineering research & design, 2007, Vol.85 (3), p.293-306

2007

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Analysis and control of heteroazeotropic batch distillation

AIChE journal, 2005-04, Vol.51 (4), p.1144-1157

2005

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Time (energy) requirements in closed batch distillation arrangements

Computers & chemical engineering, 2004-05, Vol.28 (5), p.829-837

2004

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Control Structure Selection for Reactor, Separator, and Recycle Processes

Industrial & engineering chemistry research, 2003-03, Vol.42 (6), p.1225-1234

2003

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Separation of ternary heteroazeotropic mixtures in a closed multivessel batch distillation–decanter hybrid

Chemical engineering and processing, 2004, Vol.43 (3), p.291-304

2004

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Control of symmetrically interconnected plants

Automatica (Oxford), 1994-06, Vol.30 (6), p.957-973

1994

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Dividing wall columns for heterogeneous azeotropic distillation

Chemical engineering research & design, 2015-07, Vol.99, p.111-119

2015

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Time requirements for heteroazeotropic distillation in batch columns

Computers & chemical engineering, 2004-08, Vol.28 (9), p.1689-1700

2004

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Selection of variables for stabilizing control using pole vectors

IEEE transactions on automatic control, 2003-08, Vol.48 (8), p.1393-1398

2003

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Topology of ternary VLE diagrams: Elementary cells

AIChE journal, 2002-04, Vol.48 (4), p.752-759

2002

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Self-optimizing control: the missing link between steady-state optimization and control

Computers & chemical engineering, 2000-07, Vol.24 (2), p.569-575

Skogestad, Sigurd

2000

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Optimal operation of heat exchanger networks

Computers & chemical engineering, 1999-05, Vol.23 (4), p.509-522

1999

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The Dos and Don’ts of Distillation Column Control

Model predictive control for the self-optimized operation in wastewater treatment plants: Analysis of dynamic issues

Internal configurations for a multi-product dividing wall column

Designing four-product dividing wall columns for separation of a multicomponent aromatics mixture

Simple analytic rules for model reduction and PID controller tuning

Thermal coupling opportunities for floating natural gas liquefaction plants

Azeotropic phase equilibrium diagrams: a survey

Generalized Internal Model Control for Balancing Input/Output Disturbance Response

Control structure design for complete chemical plants

Feasible separations and entrainer selection rules for heteroazeotropic batch distillation

Selecting appropriate control variables for a heat-integrated distillation system with prefractionator

Plantwide control: the search for the self-optimizing control structure

Feedback: Still the Simplest and Best Solution

Selection of Control Structure and Temperature Location for Two-Product Distillation Columns

Analysis and control of heteroazeotropic batch distillation

Time (energy) requirements in closed batch distillation arrangements

Control Structure Selection for Reactor, Separator, and Recycle Processes

Separation of ternary heteroazeotropic mixtures in a closed multivessel batch distillation–decanter hybrid

Control of symmetrically interconnected plants

Dividing wall columns for heterogeneous azeotropic distillation

Time requirements for heteroazeotropic distillation in batch columns

Selection of variables for stabilizing control using pole vectors

Topology of ternary VLE diagrams: Elementary cells

Self-optimizing control: the missing link between steady-state optimization and control

Optimal operation of heat exchanger networks

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