{"title":"常微分方程函数求解器(ode45)在间歇反应动力学建模与仿真中的应用","authors":"C. Anyigor, J. Afiukwa","doi":"10.5251/AJSIR.2013.4.3.285.287","DOIUrl":null,"url":null,"abstract":"This study presents the simulation of modelled chemical reaction in a batch reactor using the Matlab ordinary differential equation function solver (ODE45). Modelling and optimisation of actual batch reaction rate constants under isothermal condition was implemented on a set of experimental data. The data was simulated using hypothetical isothermal rate constants, 1 2 with the initial concentration profile of the reaction: and respectively between reaction time of minutes. The Process model developed was employed to optimise the rate constant (K) at which maximum yield of the desired product was achieved. Results showed maximum product yield, ‘D’ at 1= with a reaction by-product, ‘E’ at 2 = within 40 minutes reaction time. This study is intended to benefit industrial operations which aim at achieving optimum yield of a reaction process in a record time.","PeriodicalId":7661,"journal":{"name":"American Journal of Scientific and Industrial Research","volume":"2019 1","pages":"285-287"},"PeriodicalIF":0.0000,"publicationDate":"2013-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"3","resultStr":"{\"title\":\"Application of matlab ordinary differential equation function solver (ode45) in modelling and simulation of batch reaction kinetics\",\"authors\":\"C. Anyigor, J. Afiukwa\",\"doi\":\"10.5251/AJSIR.2013.4.3.285.287\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"This study presents the simulation of modelled chemical reaction in a batch reactor using the Matlab ordinary differential equation function solver (ODE45). Modelling and optimisation of actual batch reaction rate constants under isothermal condition was implemented on a set of experimental data. The data was simulated using hypothetical isothermal rate constants, 1 2 with the initial concentration profile of the reaction: and respectively between reaction time of minutes. The Process model developed was employed to optimise the rate constant (K) at which maximum yield of the desired product was achieved. Results showed maximum product yield, ‘D’ at 1= with a reaction by-product, ‘E’ at 2 = within 40 minutes reaction time. This study is intended to benefit industrial operations which aim at achieving optimum yield of a reaction process in a record time.\",\"PeriodicalId\":7661,\"journal\":{\"name\":\"American Journal of Scientific and Industrial Research\",\"volume\":\"2019 1\",\"pages\":\"285-287\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2013-06-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"3\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"American Journal of Scientific and Industrial Research\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.5251/AJSIR.2013.4.3.285.287\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"American Journal of Scientific and Industrial Research","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.5251/AJSIR.2013.4.3.285.287","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Application of matlab ordinary differential equation function solver (ode45) in modelling and simulation of batch reaction kinetics
This study presents the simulation of modelled chemical reaction in a batch reactor using the Matlab ordinary differential equation function solver (ODE45). Modelling and optimisation of actual batch reaction rate constants under isothermal condition was implemented on a set of experimental data. The data was simulated using hypothetical isothermal rate constants, 1 2 with the initial concentration profile of the reaction: and respectively between reaction time of minutes. The Process model developed was employed to optimise the rate constant (K) at which maximum yield of the desired product was achieved. Results showed maximum product yield, ‘D’ at 1= with a reaction by-product, ‘E’ at 2 = within 40 minutes reaction time. This study is intended to benefit industrial operations which aim at achieving optimum yield of a reaction process in a record time.