Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations

This study is about the modeling of biomass growth and PHB production in batch fermentation by using the numerical integration Runge Kutta 4th Order Method. The data is obtained from two sources which are from Valappil et. al, 2007[1] and data from the experiment of Hishafi, 2009 [2]. In order to si...

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主要作者: Noor Aishah, Yumasir
格式: Undergraduates Project Papers
語言:English
出版: 2009
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http://umpir.ump.edu.my/id/eprint/848/
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spelling my.ump.umpir.8482023-11-28T07:26:45Z http://umpir.ump.edu.my/id/eprint/848/ Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations Noor Aishah, Yumasir TP Chemical technology This study is about the modeling of biomass growth and PHB production in batch fermentation by using the numerical integration Runge Kutta 4th Order Method. The data is obtained from two sources which are from Valappil et. al, 2007[1] and data from the experiment of Hishafi, 2009 [2]. In order to simulate the process, the method of ordinary differential equation, ode45 in MATLAB software was used. The ode45 provides an essential tool that will integrate a set of ordinary differential equations numerically. The calculation method of ode45 uses Runge Kutta 4th Order numerical integration. The values of the parameters of the models are determined by selecting the value that will give the least square error between the predicted model and the actual data. After the modeling process, a linear regression between the parameters of the ode(as the dependent variable) and the manipulated control variable agitation rate and initial concentration of glucose (as the independent variables) is made in order to study the effect of the manipulated variables. From the simulation, it’s found that the model for both of biomass and PHB fit the data satisfactorily. After the linear regression, it is found that the agitation rate gives more influence than initial concentration of glucose. 2009-04 Undergraduates Project Papers NonPeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/848/1/Runge%20Kutta%204th%20order%20method%20and%20matlab%20in%20modeling%20of%20biomass%20growth%20and%20product%20formation%20in%20batch%20fermentation%20using%20differential%20equations.pdf Noor Aishah, Yumasir (2009) Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations. Faculty of Chemical & Natural Resources Engineering, Universiti Malaysia Pahang.
institution Universiti Malaysia Pahang Al-Sultan Abdullah
building UMPSA Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang Al-Sultan Abdullah
content_source UMPSA Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Noor Aishah, Yumasir
Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
description This study is about the modeling of biomass growth and PHB production in batch fermentation by using the numerical integration Runge Kutta 4th Order Method. The data is obtained from two sources which are from Valappil et. al, 2007[1] and data from the experiment of Hishafi, 2009 [2]. In order to simulate the process, the method of ordinary differential equation, ode45 in MATLAB software was used. The ode45 provides an essential tool that will integrate a set of ordinary differential equations numerically. The calculation method of ode45 uses Runge Kutta 4th Order numerical integration. The values of the parameters of the models are determined by selecting the value that will give the least square error between the predicted model and the actual data. After the modeling process, a linear regression between the parameters of the ode(as the dependent variable) and the manipulated control variable agitation rate and initial concentration of glucose (as the independent variables) is made in order to study the effect of the manipulated variables. From the simulation, it’s found that the model for both of biomass and PHB fit the data satisfactorily. After the linear regression, it is found that the agitation rate gives more influence than initial concentration of glucose.
format Undergraduates Project Papers
author Noor Aishah, Yumasir
author_facet Noor Aishah, Yumasir
author_sort Noor Aishah, Yumasir
title Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
title_short Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
title_full Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
title_fullStr Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
title_full_unstemmed Runge Kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
title_sort runge kutta 4th order method and matlab in modeling of biomass growth and product formation in batch fermentation using differential equations
publishDate 2009
url http://umpir.ump.edu.my/id/eprint/848/1/Runge%20Kutta%204th%20order%20method%20and%20matlab%20in%20modeling%20of%20biomass%20growth%20and%20product%20formation%20in%20batch%20fermentation%20using%20differential%20equations.pdf
http://umpir.ump.edu.my/id/eprint/848/
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