Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column

The process involved is a pilot scale packed distillation column that separates a mixture of methanol and water. The performances of two discrete time controllers that different parameter tuning techniques were used for each of them were examined in the face of the set point tracking of the overhead...

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Main Authors: Semin ALTUNTAŞ, Hale HAPOĞLU
Format: Article
Language:English
Published: Turkish Chemical Society 2020-05-01
Series:Journal of the Turkish Chemical Society Section B: Chemical Engineering
Subjects:
Online Access:https://dergipark.org.tr/tr/pub/jotcsb/issue/52550/645001
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spelling doaj-f0166411f4b14fd388c0abac691878812020-11-25T02:50:40ZengTurkish Chemical SocietyJournal of the Turkish Chemical Society Section B: Chemical Engineering2564-69072020-05-01312934 Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column Semin ALTUNTAŞ0https://orcid.org/0000-0003-3183-8650Hale HAPOĞLU1Ankara University, Ankara, TurkeyAnkara University, Ankara, TurkeyThe process involved is a pilot scale packed distillation column that separates a mixture of methanol and water. The performances of two discrete time controllers that different parameter tuning techniques were used for each of them were examined in the face of the set point tracking of the overhead product composition. The success of the discrete time controllers were assessed by means of the rise time and integral of the square error (ISE) criteria. A discrete time proportional integral controller with two terms was obtained by using the velocity form of controller law. For this controller, the proportional sensitivity term (Kc) and the other term were determined by creating root locus diagram and replacing the closed loop poles to the appropriate location in unit circle of z-plane. The most successful proposed controller action was obtained with Kc of 0.95 and integral time constant of 2.375 min according to rise time of 3.7 min and ISE criteria of 1.08. The discrete time proportional integral derivative (PID) controller with six parameters as P=0.009185, I=0.01835, D=0, N=100, b=1, c=1 that were tuned by using Simulink control design and 1 min sampling time was applied to the process. The same controller performance with six parameters of P=1.164, I=0.5319, D=-0.01481, N=3.783, b=0.1233, c=0.01017 was investigated by choosing 0.5 min sampling time. By comparing all the performances obtained, it can be said that the discrete time controller with two terms tuned by the suggested approach can easily be applied to obtain the most desired performance.https://dergipark.org.tr/tr/pub/jotcsb/issue/52550/645001discrete time controllerpacked distillation columnroot locusclosed loop pole placement
collection DOAJ
language English
format Article
sources DOAJ
author Semin ALTUNTAŞ
Hale HAPOĞLU
spellingShingle Semin ALTUNTAŞ
Hale HAPOĞLU
Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
Journal of the Turkish Chemical Society Section B: Chemical Engineering
discrete time controller
packed distillation column
root locus
closed loop pole placement
author_facet Semin ALTUNTAŞ
Hale HAPOĞLU
author_sort Semin ALTUNTAŞ
title Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
title_short Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
title_full Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
title_fullStr Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
title_full_unstemmed Application of Discrete Time Controllers to A Pilot Scale Packed Distillation Column
title_sort application of discrete time controllers to a pilot scale packed distillation column
publisher Turkish Chemical Society
series Journal of the Turkish Chemical Society Section B: Chemical Engineering
issn 2564-6907
publishDate 2020-05-01
description The process involved is a pilot scale packed distillation column that separates a mixture of methanol and water. The performances of two discrete time controllers that different parameter tuning techniques were used for each of them were examined in the face of the set point tracking of the overhead product composition. The success of the discrete time controllers were assessed by means of the rise time and integral of the square error (ISE) criteria. A discrete time proportional integral controller with two terms was obtained by using the velocity form of controller law. For this controller, the proportional sensitivity term (Kc) and the other term were determined by creating root locus diagram and replacing the closed loop poles to the appropriate location in unit circle of z-plane. The most successful proposed controller action was obtained with Kc of 0.95 and integral time constant of 2.375 min according to rise time of 3.7 min and ISE criteria of 1.08. The discrete time proportional integral derivative (PID) controller with six parameters as P=0.009185, I=0.01835, D=0, N=100, b=1, c=1 that were tuned by using Simulink control design and 1 min sampling time was applied to the process. The same controller performance with six parameters of P=1.164, I=0.5319, D=-0.01481, N=3.783, b=0.1233, c=0.01017 was investigated by choosing 0.5 min sampling time. By comparing all the performances obtained, it can be said that the discrete time controller with two terms tuned by the suggested approach can easily be applied to obtain the most desired performance.
topic discrete time controller
packed distillation column
root locus
closed loop pole placement
url https://dergipark.org.tr/tr/pub/jotcsb/issue/52550/645001
work_keys_str_mv AT seminaltuntas applicationofdiscretetimecontrollerstoapilotscalepackeddistillationcolumn
AT halehapoglu applicationofdiscretetimecontrollerstoapilotscalepackeddistillationcolumn
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