Numerical modeling of epoxidation palm kernel oil based oleic acid

The epoxidized of vegetable oil is one of the important chemical processes to produce commercial goods such as plastics, lubricants, and paints. A good kinetic model is necessary to predict the process outcome, especially for the big scale productions in which very helpf...

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Published in:International Journal of Engineering and Technology(UAE)
Main Author: Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
Format: Article
Language:English
Published: Science Publishing Corporation Inc 2018
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85059276483&doi=10.14419%2fijet.v7i4.40.24417&partnerID=40&md5=dc305ee053bbd870b581919bafc61567
id 2-s2.0-85059276483
spelling 2-s2.0-85059276483
Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
Numerical modeling of epoxidation palm kernel oil based oleic acid
2018
International Journal of Engineering and Technology(UAE)
7
4
10.14419/ijet.v7i4.40.24417
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85059276483&doi=10.14419%2fijet.v7i4.40.24417&partnerID=40&md5=dc305ee053bbd870b581919bafc61567
The epoxidized of vegetable oil is one of the important chemical processes to produce commercial goods such as plastics, lubricants, and paints. A good kinetic model is necessary to predict the process outcome, especially for the big scale productions in which very helpful in predicting the actual production. In this study, the kinetic model of the epoxidation process of palm kernel oil was investigated. The kinetic model was developed based on the laboratory works done by Jumain [1]. The mathematical model was established and implements into the MATLAB by integrating numerically using a fourth order Runge-Kutta method. The reaction rates parameters denote as k 11 , k 12 , k 13 , and k 22 were then estimated using the Hooke-Jeeves algorithm until the convergence values obtained. After 100 increments, the reaction rates parameters are k 11 = 0.1875 mol/L.min, k 12 = 0.9997 mol/L.min, k 21 = 0.0625 mol/L.min and k 22 = 0.0000 mol/L with an absolute error of 0.0857. Good agreement was found between experiment and simulation. Based on the converged kinetic values, the evolution of the concentration for all the species was simulated. After the end of the simulations, the computed concentration of the epoxide is approximately 1.5169 mol/L. © 2018 Authors.
Science Publishing Corporation Inc
2227524X
English
Article

author Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
spellingShingle Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
Numerical modeling of epoxidation palm kernel oil based oleic acid
author_facet Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
author_sort Yamin A.F.M.; Jalil M.J.; Adnan I.; Vsiduru V.G.
title Numerical modeling of epoxidation palm kernel oil based oleic acid
title_short Numerical modeling of epoxidation palm kernel oil based oleic acid
title_full Numerical modeling of epoxidation palm kernel oil based oleic acid
title_fullStr Numerical modeling of epoxidation palm kernel oil based oleic acid
title_full_unstemmed Numerical modeling of epoxidation palm kernel oil based oleic acid
title_sort Numerical modeling of epoxidation palm kernel oil based oleic acid
publishDate 2018
container_title International Journal of Engineering and Technology(UAE)
container_volume 7
container_issue 4
doi_str_mv 10.14419/ijet.v7i4.40.24417
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85059276483&doi=10.14419%2fijet.v7i4.40.24417&partnerID=40&md5=dc305ee053bbd870b581919bafc61567
description The epoxidized of vegetable oil is one of the important chemical processes to produce commercial goods such as plastics, lubricants, and paints. A good kinetic model is necessary to predict the process outcome, especially for the big scale productions in which very helpful in predicting the actual production. In this study, the kinetic model of the epoxidation process of palm kernel oil was investigated. The kinetic model was developed based on the laboratory works done by Jumain [1]. The mathematical model was established and implements into the MATLAB by integrating numerically using a fourth order Runge-Kutta method. The reaction rates parameters denote as k 11 , k 12 , k 13 , and k 22 were then estimated using the Hooke-Jeeves algorithm until the convergence values obtained. After 100 increments, the reaction rates parameters are k 11 = 0.1875 mol/L.min, k 12 = 0.9997 mol/L.min, k 21 = 0.0625 mol/L.min and k 22 = 0.0000 mol/L with an absolute error of 0.0857. Good agreement was found between experiment and simulation. Based on the converged kinetic values, the evolution of the concentration for all the species was simulated. After the end of the simulations, the computed concentration of the epoxide is approximately 1.5169 mol/L. © 2018 Authors.
publisher Science Publishing Corporation Inc
issn 2227524X
language English
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