{"title":"基于多模型预测策略的超超临界机组主蒸汽温度控制","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":"{\"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}","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}
Main-steam temperature control for ultra-supercritical unit using Multi-Model Predictive strategy
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.