Fractional order PID controller is gaining popularity because of the presence of extra degrees of freedom, which have the potential to meet up the extra degrees in terms of uncertainty, robustness, and output controllability. Distillation is the most effective separation process in the chemical and petroleum industries lacking energy sustainability. To reduce the energy consumption, one can use dividing wall distillation column (DWDC), which is proposed to be controlled by the fractional order PID controller (FOPID). We have also presented the control system for the HAD plant by implementing the FOPID controller. Both of the discussed processes are multi-input-multi-output (MIMO) system and are difficult to tune because of the presence of the interaction among the control loops. For the DWC process the traditional simplified decoupler is used, while for the HDA plant process the equivalent transfer function model approach is used to handle the MIMO system. For tuning of the FOPID controllers the optimization techniques have been used. The DWC controllers have been tuned by the ev-MOGA multi objective algorithm and the HDA plant controllers are tuned by the cuckoo search method.
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Fractional order PID controller is gaining popularity because of the presence of extra degrees of freedom, which have the potential to meet up the extra degrees in terms of uncertainty, robustness, and output controllability. Distillation is the most effective separation process in the chemical and petroleum industries lacking energy sustainability. To reduce the energy consumption, one can use dividing wall distillation column (DWDC), which is proposed to be controlled by the fractional order PID controller (FOPID). We have also presented the control system for the HAD plant by implementing the FOPID controller. Both of the discussed processes are multi-input-multi-output (MIMO) system and are difficult to tune because of the presence of the interaction among the control loops. For the DWC process the traditional simplified decoupler is used, while for the HDA plant process the equivalent transfer function model approach is used to handle the MIMO system. For tuning of the FOPID controllers the optimization techniques have been used. The DWC controllers have been tuned by the ev-MOGA multi objective algorithm and the HDA plant controllers are tuned by the cuckoo search method.
Soumya Ranjan Sahoo was born in the year 1994. He received his M. Tech in Chemical Engineering from National Institute of Technology, Rourkela, India. Dr. Madhusree Kundu, Associate Professor, hailing from the same department. The authors’ research interests include advanced control, modelling, simulation, optimization and chemometrics.
Les informations fournies dans la section « A propos du livre » peuvent faire référence à une autre édition de ce titre.
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Taschenbuch. Etat : Neu. This item is printed on demand - it takes 3-4 days longer - Neuware -Fractional order PID controller is gaining popularity because of the presence of extra degrees of freedom, which have the potential to meet up the extra degrees in terms of uncertainty, robustness, and output controllability. Distillation is the most effective separation process in the chemical and petroleum industries lacking energy sustainability. To reduce the energy consumption, one can use dividing wall distillation column (DWDC), which is proposed to be controlled by the fractional order PID controller (FOPID). We have also presented the control system for the HAD plant by implementing the FOPID controller. Both of the discussed processes are multi-input-multi-output (MIMO) system and are difficult to tune because of the presence of the interaction among the control loops. For the DWC process the traditional simplified decoupler is used, while for the HDA plant process the equivalent transfer function model approach is used to handle the MIMO system. For tuning of the FOPID controllers the optimization techniques have been used. The DWC controllers have been tuned by the ev-MOGA multi objective algorithm and the HDA plant controllers are tuned by the cuckoo search method. 128 pp. Englisch. N° de réf. du vendeur 9783659936609
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Etat : New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. Autor/Autorin: Sahoo Soumya RanjanSoumya Ranjan Sahoo was born in the year 1994. He received his M. Tech in Chemical Engineering from National Institute of Technology, Rourkela, India. Dr. Madhusree Kundu, Associate Professor, hailing from the same. N° de réf. du vendeur 158606835
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Taschenbuch. Etat : Neu. This item is printed on demand - Print on Demand Titel. Neuware -Fractional order PID controller is gaining popularity because of the presence of extra degrees of freedom, which have the potential to meet up the extra degrees in terms of uncertainty, robustness, and output controllability. Distillation is the most effective separation process in the chemical and petroleum industries lacking energy sustainability. To reduce the energy consumption, one can use dividing wall distillation column (DWDC), which is proposed to be controlled by the fractional order PID controller (FOPID). We have also presented the control system for the HAD plant by implementing the FOPID controller. Both of the discussed processes are multi-input-multi-output (MIMO) system and are difficult to tune because of the presence of the interaction among the control loops. For the DWC process the traditional simplified decoupler is used, while for the HDA plant process the equivalent transfer function model approach is used to handle the MIMO system. For tuning of the FOPID controllers the optimization techniques have been used. The DWC controllers have been tuned by the ev-MOGA multi objective algorithm and the HDA plant controllers are tuned by the cuckoo search method.VDM Verlag, Dudweiler Landstraße 99, 66123 Saarbrücken 128 pp. Englisch. N° de réf. du vendeur 9783659936609
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Taschenbuch. Etat : Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - Fractional order PID controller is gaining popularity because of the presence of extra degrees of freedom, which have the potential to meet up the extra degrees in terms of uncertainty, robustness, and output controllability. Distillation is the most effective separation process in the chemical and petroleum industries lacking energy sustainability. To reduce the energy consumption, one can use dividing wall distillation column (DWDC), which is proposed to be controlled by the fractional order PID controller (FOPID). We have also presented the control system for the HAD plant by implementing the FOPID controller. Both of the discussed processes are multi-input-multi-output (MIMO) system and are difficult to tune because of the presence of the interaction among the control loops. For the DWC process the traditional simplified decoupler is used, while for the HDA plant process the equivalent transfer function model approach is used to handle the MIMO system. For tuning of the FOPID controllers the optimization techniques have been used. The DWC controllers have been tuned by the ev-MOGA multi objective algorithm and the HDA plant controllers are tuned by the cuckoo search method. N° de réf. du vendeur 9783659936609
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Taschenbuch. Etat : Neu. Control of Plant Wide Processes Using Fractional Order Controller | Fractional order PID controllers in controlling Chemical Processes | Soumya Ranjan Sahoo (u. a.) | Taschenbuch | 128 S. | Englisch | 2016 | LAP LAMBERT Academic Publishing | EAN 9783659936609 | Verantwortliche Person für die EU: preigu GmbH & Co. KG, Lengericher Landstr. 19, 49078 Osnabrück, mail[at]preigu[dot]de | Anbieter: preigu. N° de réf. du vendeur 103176386
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