On interfacing model predictive controllers with low-level loops
| DC Field | Value | Language |
|---|---|---|
| dc.contributor.author | Lee, Yongho | ko |
| dc.contributor.author | Park, Sunwon | ko |
| dc.contributor.author | Lee, JayHyung | ko |
| dc.date.accessioned | 2013-02-27T13:16:19Z | - |
| dc.date.available | 2013-02-27T13:16:19Z | - |
| dc.date.created | 2012-02-06 | - |
| dc.date.created | 2012-02-06 | - |
| dc.date.created | 2012-02-06 | - |
| dc.date.issued | 2000-01 | - |
| dc.identifier.citation | INDUSTRIAL ENGINEERING CHEMISTRY RESEARCH, v.39, no.1, pp.92 - 102 | - |
| dc.identifier.issn | 0888-5885 | - |
| dc.identifier.uri | http://hdl.handle.net/10203/68791 | - |
| dc.description.abstract | Two options that arise in the implementation of a model-based control system on a process with low-level proportional-integral-derivative control loops are discussed. Strengths and drawbacks of the two options are examined and modifications are proposed. Simulation results for a continuous stirred tank reactor and a distillation column are presented to demonstrate the performance improvements resulting from the modifications. | - |
| dc.language | English | - |
| dc.publisher | AMER CHEMICAL SOC | - |
| dc.title | On interfacing model predictive controllers with low-level loops | - |
| dc.type | Article | - |
| dc.identifier.wosid | 000084646000014 | - |
| dc.identifier.scopusid | 2-s2.0-0033977321 | - |
| dc.type.rims | ART | - |
| dc.citation.volume | 39 | - |
| dc.citation.issue | 1 | - |
| dc.citation.beginningpage | 92 | - |
| dc.citation.endingpage | 102 | - |
| dc.citation.publicationname | INDUSTRIAL ENGINEERING CHEMISTRY RESEARCH | - |
| dc.identifier.doi | 10.1021/ie990372k | - |
| dc.contributor.localauthor | Park, Sunwon | - |
| dc.contributor.localauthor | Lee, JayHyung | - |
| dc.contributor.nonIdAuthor | Lee, Yongho | - |
| dc.description.isOpenAccess | N | - |
| dc.type.journalArticle | Article | - |
| dc.subject.keywordPlus | IDENTIFICATION | - |
| dc.subject.keywordPlus | SYSTEMS | - |
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