{"title":"间歇式搅拌釜反应器中反应物转化动力学的数值分析","authors":"Linas Petkevičius, R. Baronas","doi":"10.1109/AIEEE.2018.8592423","DOIUrl":null,"url":null,"abstract":"The paper presents a non-linear mathematical model of the batch stirred tank reactor with spherical catalyst particles as microreactors. The different initial conditions are investigated. The influence of the diffusion modulus, the Biot number and the inverse adsorption capacity on the process duration has been numerically investigated. The simulation results showed that process durations might be different by magnitude of order just by different initial microreactor injections. The digital simulation was carried out using the finite difference technique.","PeriodicalId":198244,"journal":{"name":"2018 IEEE 6th Workshop on Advances in Information, Electronic and Electrical Engineering (AIEEE)","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2018-11-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Numerical Analysis of the Dynamics of Reactant Conversion in Batch Stirred Tank Reactor\",\"authors\":\"Linas Petkevičius, R. Baronas\",\"doi\":\"10.1109/AIEEE.2018.8592423\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The paper presents a non-linear mathematical model of the batch stirred tank reactor with spherical catalyst particles as microreactors. The different initial conditions are investigated. The influence of the diffusion modulus, the Biot number and the inverse adsorption capacity on the process duration has been numerically investigated. The simulation results showed that process durations might be different by magnitude of order just by different initial microreactor injections. The digital simulation was carried out using the finite difference technique.\",\"PeriodicalId\":198244,\"journal\":{\"name\":\"2018 IEEE 6th Workshop on Advances in Information, Electronic and Electrical Engineering (AIEEE)\",\"volume\":null,\"pages\":null},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2018-11-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"2018 IEEE 6th Workshop on Advances in Information, Electronic and Electrical Engineering (AIEEE)\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1109/AIEEE.2018.8592423\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"2018 IEEE 6th Workshop on Advances in Information, Electronic and Electrical Engineering (AIEEE)","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/AIEEE.2018.8592423","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Numerical Analysis of the Dynamics of Reactant Conversion in Batch Stirred Tank Reactor
The paper presents a non-linear mathematical model of the batch stirred tank reactor with spherical catalyst particles as microreactors. The different initial conditions are investigated. The influence of the diffusion modulus, the Biot number and the inverse adsorption capacity on the process duration has been numerically investigated. The simulation results showed that process durations might be different by magnitude of order just by different initial microreactor injections. The digital simulation was carried out using the finite difference technique.
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