Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column

In this simulation study the operation of a naphtha redistillation column (a column with two feeds and three products) was analyzed with the application of Aspen HYSYS® software. The simulator, structure of local controllers and the product-quality estimators were based on the data of an industrial...

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Main Authors: Szabó László, Stocz Klára Kubovicsné, Szabó Laura, Németh Sándor, Szeifert Ferenc
Format: Article
Language:English
Published: University of Pannonia 2017-10-01
Series:Hungarian Journal of Industry and Chemistry
Subjects:
Online Access:http://www.degruyter.com/view/j/hjic.2017.45.issue-1/hjic-2017-0004/hjic-2017-0004.xml?format=INT
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author Szabó László
Stocz Klára Kubovicsné
Szabó Laura
Németh Sándor
Szeifert Ferenc
author_facet Szabó László
Stocz Klára Kubovicsné
Szabó Laura
Németh Sándor
Szeifert Ferenc
author_sort Szabó László
collection DOAJ
description In this simulation study the operation of a naphtha redistillation column (a column with two feeds and three products) was analyzed with the application of Aspen HYSYS® software. The simulator, structure of local controllers and the product-quality estimators were based on the data of an industrial column in the Danube Refinery. The aim of the analysis was to identify the dynamic and steady-state effects of heating and cooling as well as the sidestream of product qualities. The relationship between the tray temperatures and the quality of the products was also identified and inferential calculations were made. Based on the identified relationships, a twolevel hierarchical control structure was developed. On the lowest level of the hierarchy are the local controllers of flowrates, liquid levels, pressure and duty. The inferential calculations are important components of the controller which serve as the controlled variables at the coordination level. The inputs of the estimators are the process data of the column, e.g. temperature, pressure and flowrate. On the top level of the control hierarchical structure the quality of the products are controlled by manipulating the setpoint of the local controllers. Based on the analysis of the Controlled Variable – Manipulated Variable relationship, closed-loop quality control was achieved with PID controllers. The result of the analysis may form the basis of Advanced Process Controller implementation.
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spelling doaj.art-ecf00c2448f9472dab572f75a101868f2022-12-22T03:01:55ZengUniversity of PannoniaHungarian Journal of Industry and Chemistry0133-02762450-51022017-10-01451172210.1515/hjic-2017-0004hjic-2017-0004Dynamic Simulator-Based APC Design for a Naphtha Redistillation ColumnSzabó László0Stocz Klára Kubovicsné1Szabó Laura2Németh Sándor3Szeifert Ferenc4Department of Technology and Development, MOL Plc., Olajmunkás u 2., Százhalombatta, H-2443, HungaryDepartment of Technology and Development, MOL Plc., Olajmunkás u 2., Százhalombatta, H-2443, HungaryDepartment of Technology and Development, MOL Plc., Olajmunkás u 2., Százhalombatta, H-2443, HungaryDepartment of Process Engineering, University of Pannonia, Egyetem u 10., Veszprém, H-8200, HungaryDepartment of Process Engineering, University of Pannonia, Egyetem u 10., Veszprém, H-8200, HungaryIn this simulation study the operation of a naphtha redistillation column (a column with two feeds and three products) was analyzed with the application of Aspen HYSYS® software. The simulator, structure of local controllers and the product-quality estimators were based on the data of an industrial column in the Danube Refinery. The aim of the analysis was to identify the dynamic and steady-state effects of heating and cooling as well as the sidestream of product qualities. The relationship between the tray temperatures and the quality of the products was also identified and inferential calculations were made. Based on the identified relationships, a twolevel hierarchical control structure was developed. On the lowest level of the hierarchy are the local controllers of flowrates, liquid levels, pressure and duty. The inferential calculations are important components of the controller which serve as the controlled variables at the coordination level. The inputs of the estimators are the process data of the column, e.g. temperature, pressure and flowrate. On the top level of the control hierarchical structure the quality of the products are controlled by manipulating the setpoint of the local controllers. Based on the analysis of the Controlled Variable – Manipulated Variable relationship, closed-loop quality control was achieved with PID controllers. The result of the analysis may form the basis of Advanced Process Controller implementation.http://www.degruyter.com/view/j/hjic.2017.45.issue-1/hjic-2017-0004/hjic-2017-0004.xml?format=INTdistillationmultilevel controlMIMOinferentialnaphtha distillationplant data
spellingShingle Szabó László
Stocz Klára Kubovicsné
Szabó Laura
Németh Sándor
Szeifert Ferenc
Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
Hungarian Journal of Industry and Chemistry
distillation
multilevel control
MIMO
inferential
naphtha distillation
plant data
title Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
title_full Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
title_fullStr Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
title_full_unstemmed Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
title_short Dynamic Simulator-Based APC Design for a Naphtha Redistillation Column
title_sort dynamic simulator based apc design for a naphtha redistillation column
topic distillation
multilevel control
MIMO
inferential
naphtha distillation
plant data
url http://www.degruyter.com/view/j/hjic.2017.45.issue-1/hjic-2017-0004/hjic-2017-0004.xml?format=INT
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AT nemethsandor dynamicsimulatorbasedapcdesignforanaphtharedistillationcolumn
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