{"title":"溶液聚合反应器的非线性控制","authors":"A. K. Adebekun, F. Schork","doi":"10.23919/ACC.1989.4790349","DOIUrl":null,"url":null,"abstract":"The paper focusses on reference model control of a continuous stirred tank reactor for solution polymerization of methylmethacrylate. The reactor is a nonsquare plant with more outputs than inputs. Two schemes are employed both of which under certain conditions, ensure global stabilization of the reactor.","PeriodicalId":383719,"journal":{"name":"1989 American Control Conference","volume":"82 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"1989-06-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"2","resultStr":"{\"title\":\"Nonlinear Control of a Solution Polymerization Reactor\",\"authors\":\"A. K. Adebekun, F. Schork\",\"doi\":\"10.23919/ACC.1989.4790349\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The paper focusses on reference model control of a continuous stirred tank reactor for solution polymerization of methylmethacrylate. The reactor is a nonsquare plant with more outputs than inputs. Two schemes are employed both of which under certain conditions, ensure global stabilization of the reactor.\",\"PeriodicalId\":383719,\"journal\":{\"name\":\"1989 American Control Conference\",\"volume\":\"82 1\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1989-06-21\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"2\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"1989 American Control Conference\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.23919/ACC.1989.4790349\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"1989 American Control Conference","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.23919/ACC.1989.4790349","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Nonlinear Control of a Solution Polymerization Reactor
The paper focusses on reference model control of a continuous stirred tank reactor for solution polymerization of methylmethacrylate. The reactor is a nonsquare plant with more outputs than inputs. Two schemes are employed both of which under certain conditions, ensure global stabilization of the reactor.
求助内容：
应助结果提醒方式：
京公网安备 11010802042870号
