{"title":"微藻发酵连续过程的在线估计与控制策略","authors":"E. Petre, Dorin Cendrescu","doi":"10.1109/CARPATHIANCC.2015.7145108","DOIUrl":null,"url":null,"abstract":"The design of some adaptive and robust-adaptive control strategies for a microalgae fermentation process that is carried out inside a Continuous Stirred Tank Reactor (CSTR) is presented. Initially, an indirect adaptive controller is designed by coupling a linearizing controller with a new parameter estimator used for estimation of unknown kinetics. Afterwards, under the realistic assumption that the reaction kinetics are unknown, time-varying and moreover the influent flow rate is uncertain and time-varying, but some lower and upper bounds of these uncertainties are known, two robust-adaptive control structures are proposed by combining a linearizing control law with two new appropriately parameter estimators able to estimates the unknown reaction rates. Numerical simulations are included to validate the designed controllers applied to a continuous fermentation bioprocess used for microalgae production.","PeriodicalId":187762,"journal":{"name":"Proceedings of the 2015 16th International Carpathian Control Conference (ICCC)","volume":"39 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2015-05-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":"{\"title\":\"On-line estimation and control strategies for a microalgae fermentation continuous process\",\"authors\":\"E. Petre, Dorin Cendrescu\",\"doi\":\"10.1109/CARPATHIANCC.2015.7145108\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The design of some adaptive and robust-adaptive control strategies for a microalgae fermentation process that is carried out inside a Continuous Stirred Tank Reactor (CSTR) is presented. Initially, an indirect adaptive controller is designed by coupling a linearizing controller with a new parameter estimator used for estimation of unknown kinetics. Afterwards, under the realistic assumption that the reaction kinetics are unknown, time-varying and moreover the influent flow rate is uncertain and time-varying, but some lower and upper bounds of these uncertainties are known, two robust-adaptive control structures are proposed by combining a linearizing control law with two new appropriately parameter estimators able to estimates the unknown reaction rates. Numerical simulations are included to validate the designed controllers applied to a continuous fermentation bioprocess used for microalgae production.\",\"PeriodicalId\":187762,\"journal\":{\"name\":\"Proceedings of the 2015 16th International Carpathian Control Conference (ICCC)\",\"volume\":\"39 1\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2015-05-27\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"1\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Proceedings of the 2015 16th International Carpathian Control Conference (ICCC)\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1109/CARPATHIANCC.2015.7145108\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Proceedings of the 2015 16th International Carpathian Control Conference (ICCC)","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/CARPATHIANCC.2015.7145108","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
On-line estimation and control strategies for a microalgae fermentation continuous process
The design of some adaptive and robust-adaptive control strategies for a microalgae fermentation process that is carried out inside a Continuous Stirred Tank Reactor (CSTR) is presented. Initially, an indirect adaptive controller is designed by coupling a linearizing controller with a new parameter estimator used for estimation of unknown kinetics. Afterwards, under the realistic assumption that the reaction kinetics are unknown, time-varying and moreover the influent flow rate is uncertain and time-varying, but some lower and upper bounds of these uncertainties are known, two robust-adaptive control structures are proposed by combining a linearizing control law with two new appropriately parameter estimators able to estimates the unknown reaction rates. Numerical simulations are included to validate the designed controllers applied to a continuous fermentation bioprocess used for microalgae production.