Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin

Dihydroxystearic Acid (DHSA) is a chemical compound that belongs in the hydroxy fatty acid group which is mainly used in cosmetic industries. DHSA usually produced by the process of in-situ epoxidation of oleic acid, followed by the hydrolysis of the epoxidized oleic acid. This study focuses on the...

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Main Authors: Fathi, Abdul Hakim Masu’ud, Jamaludin, Siti Khatijah
Format: Conference or Workshop Item
Language:English
Published: 2020
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Online Access:https://ir.uitm.edu.my/id/eprint/82661/1/82661.pdf
https://ir.uitm.edu.my/id/eprint/82661/
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spelling my.uitm.ir.826612023-08-17T06:23:14Z https://ir.uitm.edu.my/id/eprint/82661/ Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin Fathi, Abdul Hakim Masu’ud Jamaludin, Siti Khatijah Chemical engineering Hydrolysis Dihydroxystearic Acid (DHSA) is a chemical compound that belongs in the hydroxy fatty acid group which is mainly used in cosmetic industries. DHSA usually produced by the process of in-situ epoxidation of oleic acid, followed by the hydrolysis of the epoxidized oleic acid. This study focuses on the kinetic modelling of the production of DHSA. The purpose of this study is to establish a kinetic model of one-pot synthesis of DHSA via continuous in-situ epoxidation and hydrolysis process and to fit the kinetic model with the experimental data to obtain the reaction rate constants (k) and activation energy (Ea). Assumptions was made which then applied to the reaction scheme in order to develop a new reaction scheme for the kinetic model. MATLAB was the software used for developing the model where ODE45 function in MATLAB were used to solve the ordinary differential equation (ODE) by applying fourth-order Runge-Kutta method. From the model, reaction rate constants (k) were determined. The reaction rate constants (k) determined were then used to obtain the activation energy (Ea) of the reaction by constructing the Arrhenius plot for the reaction at temperature 55C and 75C. 2020 Conference or Workshop Item PeerReviewed text en https://ir.uitm.edu.my/id/eprint/82661/1/82661.pdf Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin. (2020) In: UNSPECIFIED.
institution Universiti Teknologi Mara
building Tun Abdul Razak Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Mara
content_source UiTM Institutional Repository
url_provider http://ir.uitm.edu.my/
language English
topic Chemical engineering
Hydrolysis
spellingShingle Chemical engineering
Hydrolysis
Fathi, Abdul Hakim Masu’ud
Jamaludin, Siti Khatijah
Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
description Dihydroxystearic Acid (DHSA) is a chemical compound that belongs in the hydroxy fatty acid group which is mainly used in cosmetic industries. DHSA usually produced by the process of in-situ epoxidation of oleic acid, followed by the hydrolysis of the epoxidized oleic acid. This study focuses on the kinetic modelling of the production of DHSA. The purpose of this study is to establish a kinetic model of one-pot synthesis of DHSA via continuous in-situ epoxidation and hydrolysis process and to fit the kinetic model with the experimental data to obtain the reaction rate constants (k) and activation energy (Ea). Assumptions was made which then applied to the reaction scheme in order to develop a new reaction scheme for the kinetic model. MATLAB was the software used for developing the model where ODE45 function in MATLAB were used to solve the ordinary differential equation (ODE) by applying fourth-order Runge-Kutta method. From the model, reaction rate constants (k) were determined. The reaction rate constants (k) determined were then used to obtain the activation energy (Ea) of the reaction by constructing the Arrhenius plot for the reaction at temperature 55C and 75C.
format Conference or Workshop Item
author Fathi, Abdul Hakim Masu’ud
Jamaludin, Siti Khatijah
author_facet Fathi, Abdul Hakim Masu’ud
Jamaludin, Siti Khatijah
author_sort Fathi, Abdul Hakim Masu’ud
title Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
title_short Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
title_full Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
title_fullStr Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
title_full_unstemmed Kinetic modelling of Dihydroxystearic Acid (DHSA) production from palm kernel oil-based oleic acid / Abdul Hakim Masu’ud Fathi and Siti Khatijah Jamaludin
title_sort kinetic modelling of dihydroxystearic acid (dhsa) production from palm kernel oil-based oleic acid / abdul hakim masu’ud fathi and siti khatijah jamaludin
publishDate 2020
url https://ir.uitm.edu.my/id/eprint/82661/1/82661.pdf
https://ir.uitm.edu.my/id/eprint/82661/
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