{"title":"MGAS固定床煤气炉控制策略评价","authors":"S. Reddy, A. Farell","doi":"10.1109/SSST.1993.522785","DOIUrl":null,"url":null,"abstract":"The MGAS (METC Gasifier Advanced Simulation) model is used to simulate a moving-bed gasifier. The MGAS code is written in FORTRAN and takes into account details in specifying the reactor geometry, reaction kinetics, etc. Steady-state control analysis tools that use MGAS to uncover the optimal control strategies are demonstrated. These strategies are compared with those that are known to be suitable in the actual gasifier.","PeriodicalId":260036,"journal":{"name":"1993 (25th) Southeastern Symposium on System Theory","volume":"1 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"1993-03-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":"{\"title\":\"Evaluation of control strategies for fixed-bed coal gasifiers using MGAS\",\"authors\":\"S. Reddy, A. Farell\",\"doi\":\"10.1109/SSST.1993.522785\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The MGAS (METC Gasifier Advanced Simulation) model is used to simulate a moving-bed gasifier. The MGAS code is written in FORTRAN and takes into account details in specifying the reactor geometry, reaction kinetics, etc. Steady-state control analysis tools that use MGAS to uncover the optimal control strategies are demonstrated. These strategies are compared with those that are known to be suitable in the actual gasifier.\",\"PeriodicalId\":260036,\"journal\":{\"name\":\"1993 (25th) Southeastern Symposium on System Theory\",\"volume\":\"1 1\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1993-03-07\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"1\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"1993 (25th) Southeastern Symposium on System Theory\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1109/SSST.1993.522785\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"1993 (25th) Southeastern Symposium on System Theory","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/SSST.1993.522785","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Evaluation of control strategies for fixed-bed coal gasifiers using MGAS
The MGAS (METC Gasifier Advanced Simulation) model is used to simulate a moving-bed gasifier. The MGAS code is written in FORTRAN and takes into account details in specifying the reactor geometry, reaction kinetics, etc. Steady-state control analysis tools that use MGAS to uncover the optimal control strategies are demonstrated. These strategies are compared with those that are known to be suitable in the actual gasifier.