Johan Grievink | Delft University of Technology (original) (raw)
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Papers by Johan Grievink
Computer Aided Chemical Engineering, 2007
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Analytical Biochemistry, 1974
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Industrial Engineering Chemistry Research, 2008
... the compartment integration is carried out by introducing a superstructure and finding the op... more ... the compartment integration is carried out by introducing a superstructure and finding the optimal configuration using ... 47. This theory will now be applied to the multiobjective design cases for a ... (1) Steady-State Entropy Production Profile in a MTBE Reactive Distillation Column. ...
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Computer Aided Chemical Engineering, 2002
This paper presents an approach to analyse the controllability of process alternatives based on t... more This paper presents an approach to analyse the controllability of process alternatives based on the optimal closed-loop performance. The approach presented by Tousain and Meeuse (2001) is extended to include the robustness properties in terms of two different uncertainty models: parametric uncertainty and co-prime factor uncertainty. The simulation results on a distillation column demonstrate that the optimal design parameters using the nominal closed-loop controllability will not alter after introducing the robustness criterion.
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Computer Aided Chemical Engineering, 2003
... editors) 92003Publishedby ElsevierScienceB.V. Multilevel modelling of spatial structures in r... more ... editors) 92003Publishedby ElsevierScienceB.V. Multilevel modelling of spatial structures in reac-tive distillation units CP Almeida-Rivera, PLJ Swinkels ... Sev-eral promising advantages may be derived from the combination of reaction and separation units in a single apparatus ...
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Computer Aided Chemical Engineering, 2002
ABSTRACT
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Fundamentals of Conversion Processes, 2014
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Computer Aided Chemical Engineering, 2002
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Computer Aided Chemical Engineering, 2002
This paper presents an approach to analyse the controllability of process alternatives based on t... more This paper presents an approach to analyse the controllability of process alternatives based on the optimal closed-loop performance. The approach presented by Tousain and Meeuse (2001) is extended to include the robustness properties in terms of two different uncertainty models: parametric uncertainty and co-prime factor uncertainty. The simulation results on a distillation column demonstrate that the optimal design parameters using
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Computer Aided Process and Product Engineering, 2006
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Computer Aided Chemical Engineering, 2002
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Computer Aided Chemical Engineering, 2000
ABSTRACT
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Computer Aided Chemical Engineering, 2008
The application of model reduction techniques in the context of dynamic optimization of chemical ... more The application of model reduction techniques in the context of dynamic optimization of chemical plants operation is investigated. The focus is on the derivation and use of reduced models for the design and implementation of optimal dynamic operation in large-scale chemical ...
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Computer Aided Chemical Engineering, 2011
Abstract Process systems & models have structural and behavioural features, which can... more Abstract Process systems & models have structural and behavioural features, which can be exploited for model reduction. A reduction approach is introduced addressing both features, while systematically going through the usual model development steps. Thus, the reduction is not applied only at mathematical and numerical level, but at physical and systemic level as well. The benefit is that the model reduction is achieved while retaining the topological structure of the processand the meaning of the variables. The application of the approach ...
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ABSTRACT
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Computer Aided Chemical Engineering, 2007
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Bookmarks Related papers MentionsView impact
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Analytical Biochemistry, 1974
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Industrial Engineering Chemistry Research, 2008
... the compartment integration is carried out by introducing a superstructure and finding the op... more ... the compartment integration is carried out by introducing a superstructure and finding the optimal configuration using ... 47. This theory will now be applied to the multiobjective design cases for a ... (1) Steady-State Entropy Production Profile in a MTBE Reactive Distillation Column. ...
Bookmarks Related papers MentionsView impact
Computer Aided Chemical Engineering, 2002
This paper presents an approach to analyse the controllability of process alternatives based on t... more This paper presents an approach to analyse the controllability of process alternatives based on the optimal closed-loop performance. The approach presented by Tousain and Meeuse (2001) is extended to include the robustness properties in terms of two different uncertainty models: parametric uncertainty and co-prime factor uncertainty. The simulation results on a distillation column demonstrate that the optimal design parameters using the nominal closed-loop controllability will not alter after introducing the robustness criterion.
Bookmarks Related papers MentionsView impact
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Computer Aided Chemical Engineering, 2003
... editors) 92003Publishedby ElsevierScienceB.V. Multilevel modelling of spatial structures in r... more ... editors) 92003Publishedby ElsevierScienceB.V. Multilevel modelling of spatial structures in reac-tive distillation units CP Almeida-Rivera, PLJ Swinkels ... Sev-eral promising advantages may be derived from the combination of reaction and separation units in a single apparatus ...
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Computer Aided Chemical Engineering, 2002
ABSTRACT
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Fundamentals of Conversion Processes, 2014
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Computer Aided Chemical Engineering, 2002
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Computer Aided Chemical Engineering, 2002
This paper presents an approach to analyse the controllability of process alternatives based on t... more This paper presents an approach to analyse the controllability of process alternatives based on the optimal closed-loop performance. The approach presented by Tousain and Meeuse (2001) is extended to include the robustness properties in terms of two different uncertainty models: parametric uncertainty and co-prime factor uncertainty. The simulation results on a distillation column demonstrate that the optimal design parameters using
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Computer Aided Process and Product Engineering, 2006
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Computer Aided Chemical Engineering, 2002
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Computer Aided Chemical Engineering, 2000
ABSTRACT
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Computer Aided Chemical Engineering, 2008
The application of model reduction techniques in the context of dynamic optimization of chemical ... more The application of model reduction techniques in the context of dynamic optimization of chemical plants operation is investigated. The focus is on the derivation and use of reduced models for the design and implementation of optimal dynamic operation in large-scale chemical ...
Bookmarks Related papers MentionsView impact
Computer Aided Chemical Engineering, 2011
Abstract Process systems & models have structural and behavioural features, which can... more Abstract Process systems & models have structural and behavioural features, which can be exploited for model reduction. A reduction approach is introduced addressing both features, while systematically going through the usual model development steps. Thus, the reduction is not applied only at mathematical and numerical level, but at physical and systemic level as well. The benefit is that the model reduction is achieved while retaining the topological structure of the processand the meaning of the variables. The application of the approach ...
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ABSTRACT
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