{"title":"Start-up and Shut-down Conditions for Iterative Real-Time Optimization Methods","authors":"A. R. G. Mukkula, Afaq Ahmad, S. Engell","doi":"10.1109/ICC47138.2019.9123183","DOIUrl":null,"url":null,"abstract":"Iterative real-time optimization methods are able to identify the real process optimum in the presence of structural and parametric plant-model mismatch. However, upon converging to the process optimum they may suffer from generating ongoing process perturbations in response to measurement noise which are inefficient. In this paper, we propose a strategy for the shut-down of the iterative optimization schemes upon convergence to the plant optimum and a strategy for the start-up of the iterative optimization when a change in the process behavior occurs, in order to avoid a loss of performance. We employ techniques from statistical process monitoring to formulate appropriate conditions to detect a change in the process. The performance of the proposed start-up and shut-down strategies in combination with a powerful real-time optimization method namely, modifier adaptation with quadratic approximation (MAWQA), is analyzed using a chemical engineering case study.","PeriodicalId":231050,"journal":{"name":"2019 Sixth Indian Control Conference (ICC)","volume":"30 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2019-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"2","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"2019 Sixth Indian Control Conference (ICC)","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/ICC47138.2019.9123183","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 2
Abstract
Iterative real-time optimization methods are able to identify the real process optimum in the presence of structural and parametric plant-model mismatch. However, upon converging to the process optimum they may suffer from generating ongoing process perturbations in response to measurement noise which are inefficient. In this paper, we propose a strategy for the shut-down of the iterative optimization schemes upon convergence to the plant optimum and a strategy for the start-up of the iterative optimization when a change in the process behavior occurs, in order to avoid a loss of performance. We employ techniques from statistical process monitoring to formulate appropriate conditions to detect a change in the process. The performance of the proposed start-up and shut-down strategies in combination with a powerful real-time optimization method namely, modifier adaptation with quadratic approximation (MAWQA), is analyzed using a chemical engineering case study.