{"title":"Main-steam temperature control for ultra-supercritical unit using Multi-Model Predictive strategy","authors":"Dingfang Li, Hong Zhou","doi":"10.1109/ASSCC.2012.6523260","DOIUrl":null,"url":null,"abstract":"A Multi-Model Predictive Control (MMPC) strategy based on dynamic matrix algorithm is proposed and applied to the main-steam temperature control of a ultra-supercritical once through boiler-turbine system in this paper. Firstly, models and corresponding controllers can change with the changing operating point via a multi-model switching technique so as to achieve robustness. Secondly, by multi-step prediction, rolling optimization and feedback correction, the plant output is optimized at each sampling interval so as to obtain better dynamic performance. Thirdly, due to good real-time tracking performance, the system can respond faster. Furthermore, in order to inhibit the sudden disturbance, a inner loop of proportional is added to form a cascade MMPC-P controller. Simulation shows much better robustness and dynamic performance for various kinds of electric load demand changes and parameters variations via this strategy than the conventional PID method.","PeriodicalId":341348,"journal":{"name":"2012 10th International Power & Energy Conference (IPEC)","volume":"5 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2012-11-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"2","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"2012 10th International Power & Energy Conference (IPEC)","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/ASSCC.2012.6523260","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
A Multi-Model Predictive Control (MMPC) strategy based on dynamic matrix algorithm is proposed and applied to the main-steam temperature control of a ultra-supercritical once through boiler-turbine system in this paper. Firstly, models and corresponding controllers can change with the changing operating point via a multi-model switching technique so as to achieve robustness. Secondly, by multi-step prediction, rolling optimization and feedback correction, the plant output is optimized at each sampling interval so as to obtain better dynamic performance. Thirdly, due to good real-time tracking performance, the system can respond faster. Furthermore, in order to inhibit the sudden disturbance, a inner loop of proportional is added to form a cascade MMPC-P controller. Simulation shows much better robustness and dynamic performance for various kinds of electric load demand changes and parameters variations via this strategy than the conventional PID method.