Constrained MPC under closed-loop uncertainty
The importance of closed-loop uncertainty predictions in robust model-predictive control (MPC) has been discussed by a number of authors in previous years [(A. Bemporad, 1998), (D. Mayne, 2000), (B. Kouvaritakis, 2000)]. The proposed controllers often rely upon invariant sets and require that input...
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description | The importance of closed-loop uncertainty predictions in robust model-predictive control (MPC) has been discussed by a number of authors in previous years [(A. Bemporad, 1998), (D. Mayne, 2000), (B. Kouvaritakis, 2000)]. The proposed controllers often rely upon invariant sets and require that input constraints are inactive at the final steady-state [(B. Kouvaritakis, 2000), (M. V. Kothare et al., 1996)]. The controller discussed in this paper avoids this limiting assumption while maintaining robust output constraint handling. This paper emphasises the often negative effects of probabilistic input constraints and proposes a method based upon multiple uncertainty regions to deal with these effects. The proposed controller solves a second-order cone program (SOCP) at each execution in order to determine the set of control moves that optimizes the expected performance of the closed-loop system while maintaining the uncertain process outputs and inputs within their allowable bounds. Case studies illustrate the performance of the new controller when plant/model mismatch is present. |
doi_str_mv | 10.23919/ACC.2004.1384037 |
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Case studies illustrate the performance of the new controller when plant/model mismatch is present.</description><subject>Chemical engineering</subject><subject>Control systems</subject><subject>Equations</subject><subject>Open loop systems</subject><subject>Predictive models</subject><subject>Robust control</subject><subject>Robustness</subject><subject>Steady-state</subject><subject>Time varying systems</subject><subject>Uncertainty</subject><issn>0743-1619</issn><issn>2378-5861</issn><isbn>9780780383357</isbn><isbn>0780383354</isbn><fulltext>true</fulltext><rsrctype>conference_proceeding</rsrctype><creationdate>2004</creationdate><recordtype>conference_proceeding</recordtype><sourceid>6IE</sourceid><sourceid>RIE</sourceid><recordid>eNotkEtLw0AUhQcfYK39AeKmK3cT7507z2UJvqCiC12HNHMDkTSpmWTRf2-ghQMfHD7O4ghxj5ApChieNnmeKQCdIXkN5C7EQpHz0niLl2IVnIc55ImMuxILcJokWgw34jalXwAMwcJCyLzv0jiUTcdx_fGVr6cu8rCu2j5xlG3fH-am4mGcjfF4J67rsk28OnMpfl6ev_M3uf18fc83W9kg2VEaa0ywwRvHTFA7YxENEiNqwyZqZSoonYseFDrlq5INqLCDHUejo6ppKR5Pu4eh_5s4jcW-SRW3bdlxP6VCBQ-ovZ_Fh5PYMHNxGJp9ORyL8yX0DxFMUGI</recordid><startdate>20040101</startdate><enddate>20040101</enddate><creator>Warren, A.L.</creator><creator>Marlin, T.E.</creator><general>IEEE</general><scope>6IE</scope><scope>6IH</scope><scope>CBEJK</scope><scope>RIE</scope><scope>RIO</scope><scope>7SC</scope><scope>7SP</scope><scope>7TB</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>JQ2</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope></search><sort><creationdate>20040101</creationdate><title>Constrained MPC under closed-loop uncertainty</title><author>Warren, A.L. ; Marlin, T.E.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-i136t-5655969857ee30f75611513e1145e5d425c0a77d8021728cae5029b0bed54d2f3</frbrgroupid><rsrctype>conference_proceedings</rsrctype><prefilter>conference_proceedings</prefilter><language>eng</language><creationdate>2004</creationdate><topic>Chemical engineering</topic><topic>Control systems</topic><topic>Equations</topic><topic>Open loop systems</topic><topic>Predictive models</topic><topic>Robust control</topic><topic>Robustness</topic><topic>Steady-state</topic><topic>Time varying systems</topic><topic>Uncertainty</topic><toplevel>online_resources</toplevel><creatorcontrib>Warren, A.L.</creatorcontrib><creatorcontrib>Marlin, T.E.</creatorcontrib><collection>IEEE Electronic Library (IEL) Conference Proceedings</collection><collection>IEEE Proceedings Order Plan (POP) 1998-present by volume</collection><collection>IEEE Xplore All Conference Proceedings</collection><collection>IEEE Electronic Library (IEL)</collection><collection>IEEE Proceedings Order Plans (POP) 1998-present</collection><collection>Computer and Information Systems Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering 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></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>Warren, A.L.</au><au>Marlin, T.E.</au><format>book</format><genre>proceeding</genre><ristype>CONF</ristype><atitle>Constrained MPC under closed-loop uncertainty</atitle><btitle>2004 American Control Conference Proceedings; Volume 5 of 6</btitle><stitle>ACC</stitle><date>2004-01-01</date><risdate>2004</risdate><volume>5</volume><spage>4607</spage><epage>4612 vol.5</epage><pages>4607-4612 vol.5</pages><issn>0743-1619</issn><eissn>2378-5861</eissn><isbn>9780780383357</isbn><isbn>0780383354</isbn><abstract>The importance of closed-loop uncertainty predictions in robust model-predictive control (MPC) has been discussed by a number of authors in previous years [(A. Bemporad, 1998), (D. Mayne, 2000), (B. Kouvaritakis, 2000)]. The proposed controllers often rely upon invariant sets and require that input constraints are inactive at the final steady-state [(B. Kouvaritakis, 2000), (M. V. Kothare et al., 1996)]. The controller discussed in this paper avoids this limiting assumption while maintaining robust output constraint handling. This paper emphasises the often negative effects of probabilistic input constraints and proposes a method based upon multiple uncertainty regions to deal with these effects. The proposed controller solves a second-order cone program (SOCP) at each execution in order to determine the set of control moves that optimizes the expected performance of the closed-loop system while maintaining the uncertain process outputs and inputs within their allowable bounds. 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subjects | Chemical engineering Control systems Equations Open loop systems Predictive models Robust control Robustness Steady-state Time varying systems Uncertainty |
title | Constrained MPC under closed-loop uncertainty |
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