A self-tuning controller for chemical processes
An adaptive controller is presented that is able to perform effectively in the presence of nonlinearities and of model uncertainty typical of industrial processes. The controller incorporates a minimum variance part and a caution part. The latter is independent of the estimated model and becomes dom...
Gespeichert in:
Veröffentlicht in: | AIChE journal 1987-01, Vol.33 (3), p.401-409 |
---|---|
Hauptverfasser: | , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 409 |
---|---|
container_issue | 3 |
container_start_page | 401 |
container_title | AIChE journal |
container_volume | 33 |
creator | Papadoulis, A V Tsiligiannis, C A Svoronos, S A |
description | An adaptive controller is presented that is able to perform effectively in the presence of nonlinearities and of model uncertainty typical of industrial processes. The controller incorporates a minimum variance part and a caution part. The latter is independent of the estimated model and becomes dominant in the case of a large mismatch between plant and estimated model. Application to a simulated nonlinear continuous stirred-tank reactor demonstrates its effectiveness, even when other adaptive controllers give unsatisfactory performance. |
format | Article |
fullrecord | <record><control><sourceid>proquest</sourceid><recordid>TN_cdi_proquest_miscellaneous_745669836</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>24671282</sourcerecordid><originalsourceid>FETCH-LOGICAL-p636-15c06f8662d494c1f9079b4614ae97dab0382992df51c65722299d47e1384d523</originalsourceid><addsrcrecordid>eNp9jc1KAzEURrNQsFbfIStdDSY3yU2yLMU_KHTTfUmTGx1JJ3Uy8_4O6NrVx4HDd67YSgghO2m0vGG3rX0tBNbBij1teKOSu2ke-uGDxzpMYy2FRp7ryOMnnfsYCr-MNVJr1O7YdQ6l0f3frtnh5fmwfet2-9f37WbXXVDhEooCs0OEpL2OMnth_Umj1IG8TeEklAPvIWUjIxoLsFDSlqRyOhlQa_b4e7uEv2dq0_Hct0ilhIHq3I5WG0TvFC7mw78maLQSHKgfZW1LpQ</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>24671282</pqid></control><display><type>article</type><title>A self-tuning controller for chemical processes</title><source>Access via Wiley Online Library</source><creator>Papadoulis, A V ; Tsiligiannis, C A ; Svoronos, S A</creator><creatorcontrib>Papadoulis, A V ; Tsiligiannis, C A ; Svoronos, S A</creatorcontrib><description>An adaptive controller is presented that is able to perform effectively in the presence of nonlinearities and of model uncertainty typical of industrial processes. The controller incorporates a minimum variance part and a caution part. The latter is independent of the estimated model and becomes dominant in the case of a large mismatch between plant and estimated model. Application to a simulated nonlinear continuous stirred-tank reactor demonstrates its effectiveness, even when other adaptive controllers give unsatisfactory performance.</description><identifier>ISSN: 0001-1541</identifier><language>eng</language><subject>adaptive control ; chemical plants ; process control ; simulation</subject><ispartof>AIChE journal, 1987-01, Vol.33 (3), p.401-409</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784</link.rule.ids></links><search><creatorcontrib>Papadoulis, A V</creatorcontrib><creatorcontrib>Tsiligiannis, C A</creatorcontrib><creatorcontrib>Svoronos, S A</creatorcontrib><title>A self-tuning controller for chemical processes</title><title>AIChE journal</title><description>An adaptive controller is presented that is able to perform effectively in the presence of nonlinearities and of model uncertainty typical of industrial processes. The controller incorporates a minimum variance part and a caution part. The latter is independent of the estimated model and becomes dominant in the case of a large mismatch between plant and estimated model. Application to a simulated nonlinear continuous stirred-tank reactor demonstrates its effectiveness, even when other adaptive controllers give unsatisfactory performance.</description><subject>adaptive control</subject><subject>chemical plants</subject><subject>process control</subject><subject>simulation</subject><issn>0001-1541</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1987</creationdate><recordtype>article</recordtype><recordid>eNp9jc1KAzEURrNQsFbfIStdDSY3yU2yLMU_KHTTfUmTGx1JJ3Uy8_4O6NrVx4HDd67YSgghO2m0vGG3rX0tBNbBij1teKOSu2ke-uGDxzpMYy2FRp7ryOMnnfsYCr-MNVJr1O7YdQ6l0f3frtnh5fmwfet2-9f37WbXXVDhEooCs0OEpL2OMnth_Umj1IG8TeEklAPvIWUjIxoLsFDSlqRyOhlQa_b4e7uEv2dq0_Hct0ilhIHq3I5WG0TvFC7mw78maLQSHKgfZW1LpQ</recordid><startdate>19870101</startdate><enddate>19870101</enddate><creator>Papadoulis, A V</creator><creator>Tsiligiannis, C A</creator><creator>Svoronos, S A</creator><scope>7SC</scope><scope>8FD</scope><scope>JQ2</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>7TC</scope></search><sort><creationdate>19870101</creationdate><title>A self-tuning controller for chemical processes</title><author>Papadoulis, A V ; Tsiligiannis, C A ; Svoronos, S A</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-p636-15c06f8662d494c1f9079b4614ae97dab0382992df51c65722299d47e1384d523</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1987</creationdate><topic>adaptive control</topic><topic>chemical plants</topic><topic>process control</topic><topic>simulation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Papadoulis, A V</creatorcontrib><creatorcontrib>Tsiligiannis, C A</creatorcontrib><creatorcontrib>Svoronos, S A</creatorcontrib><collection>Computer and Information Systems Abstracts</collection><collection>Technology Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Mechanical Engineering Abstracts</collection><jtitle>AIChE journal</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Papadoulis, A V</au><au>Tsiligiannis, C A</au><au>Svoronos, S A</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A self-tuning controller for chemical processes</atitle><jtitle>AIChE journal</jtitle><date>1987-01-01</date><risdate>1987</risdate><volume>33</volume><issue>3</issue><spage>401</spage><epage>409</epage><pages>401-409</pages><issn>0001-1541</issn><abstract>An adaptive controller is presented that is able to perform effectively in the presence of nonlinearities and of model uncertainty typical of industrial processes. The controller incorporates a minimum variance part and a caution part. The latter is independent of the estimated model and becomes dominant in the case of a large mismatch between plant and estimated model. Application to a simulated nonlinear continuous stirred-tank reactor demonstrates its effectiveness, even when other adaptive controllers give unsatisfactory performance.</abstract><tpages>9</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0001-1541 |
ispartof | AIChE journal, 1987-01, Vol.33 (3), p.401-409 |
issn | 0001-1541 |
language | eng |
recordid | cdi_proquest_miscellaneous_745669836 |
source | Access via Wiley Online Library |
subjects | adaptive control chemical plants process control simulation |
title | A self-tuning controller for chemical processes |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-22T11%3A30%3A09IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=A%20self-tuning%20controller%20for%20chemical%20processes&rft.jtitle=AIChE%20journal&rft.au=Papadoulis,%20A%20V&rft.date=1987-01-01&rft.volume=33&rft.issue=3&rft.spage=401&rft.epage=409&rft.pages=401-409&rft.issn=0001-1541&rft_id=info:doi/&rft_dat=%3Cproquest%3E24671282%3C/proquest%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=24671282&rft_id=info:pmid/&rfr_iscdi=true |