Development of heterogeneous base catalyst for transesterification reaction

Among the many possible clean fuel sources, biodiesel derived from vegetable oil (VO) attracts attention as a promising one for substitution or blending with conventional diesel-based fuels. The current process utilizes alkali hydroxide dissolved in methanol for catalyzing the transesterification. H...

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Main Author: Norashikin, Mohd Hatta
Format: Undergraduates Project Papers
Language:English
Published: 2010
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Online Access:http://umpir.ump.edu.my/id/eprint/3196/1/CD5634_NORASHIKIN_MOHD_HATTA.pdf
http://umpir.ump.edu.my/id/eprint/3196/
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spelling my.ump.umpir.31962021-07-02T07:58:42Z http://umpir.ump.edu.my/id/eprint/3196/ Development of heterogeneous base catalyst for transesterification reaction Norashikin, Mohd Hatta TP Chemical technology Among the many possible clean fuel sources, biodiesel derived from vegetable oil (VO) attracts attention as a promising one for substitution or blending with conventional diesel-based fuels. The current process utilizes alkali hydroxide dissolved in methanol for catalyzing the transesterification. However, the homogeneous catalyst gives a problem to environmental which would be leading the environmentally toxic. Therefore, the heterogeneous base catalyst should be developing to replace the homogeneous base catalyst as prevention. Here, the Calcium Oxide (CaO) loaded on Alumina (CaO/Al2O3) is used as the heterogeneous base catalyst for transesterification of Palm Oil and Methanol. The CaO/Al2O3 was prepared by using impregnation method and calcined at 650°C for 5 hours and characterized by Fourier Transfer Infrared Spectroscopy (FT-IR) and Scanning Electron Microscope (SEM). Both of equipment showed that Calcium Oxide is successfully supported by Alumina which 50% Calcium Oxide loading on Alumina is the best result. Then the catalyst was tested for the transesterification between palm oil and methanol. The transesterification reaction between palm oil and methanol is carried out at different parameter such as reaction temperature, mass ratio of catalyst to oil and molar ratio of methanol to oil. Then, the sample is analyzed using Gas Chromatography (GC). The result showed that the higher conversion of biodiesel is obtained by adding CaO catalyst of 3.5%, reaction temperature of 65°C and molar ratio of methanol to oil of 14:1. The higher total conversion of biodiesel is 48.82%. As a conclusion, the biodiesel conversion increased when there are increase in reaction temperature, amount of catalyst loading and molar ratio of methanol to oil. 2010-12 Undergraduates Project Papers NonPeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/3196/1/CD5634_NORASHIKIN_MOHD_HATTA.pdf Norashikin, Mohd Hatta (2010) Development of heterogeneous base catalyst for transesterification reaction. Faculty of Chemical & Natural Resources Engineering , Universiti Malaysia Pahang .
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Norashikin, Mohd Hatta
Development of heterogeneous base catalyst for transesterification reaction
description Among the many possible clean fuel sources, biodiesel derived from vegetable oil (VO) attracts attention as a promising one for substitution or blending with conventional diesel-based fuels. The current process utilizes alkali hydroxide dissolved in methanol for catalyzing the transesterification. However, the homogeneous catalyst gives a problem to environmental which would be leading the environmentally toxic. Therefore, the heterogeneous base catalyst should be developing to replace the homogeneous base catalyst as prevention. Here, the Calcium Oxide (CaO) loaded on Alumina (CaO/Al2O3) is used as the heterogeneous base catalyst for transesterification of Palm Oil and Methanol. The CaO/Al2O3 was prepared by using impregnation method and calcined at 650°C for 5 hours and characterized by Fourier Transfer Infrared Spectroscopy (FT-IR) and Scanning Electron Microscope (SEM). Both of equipment showed that Calcium Oxide is successfully supported by Alumina which 50% Calcium Oxide loading on Alumina is the best result. Then the catalyst was tested for the transesterification between palm oil and methanol. The transesterification reaction between palm oil and methanol is carried out at different parameter such as reaction temperature, mass ratio of catalyst to oil and molar ratio of methanol to oil. Then, the sample is analyzed using Gas Chromatography (GC). The result showed that the higher conversion of biodiesel is obtained by adding CaO catalyst of 3.5%, reaction temperature of 65°C and molar ratio of methanol to oil of 14:1. The higher total conversion of biodiesel is 48.82%. As a conclusion, the biodiesel conversion increased when there are increase in reaction temperature, amount of catalyst loading and molar ratio of methanol to oil.
format Undergraduates Project Papers
author Norashikin, Mohd Hatta
author_facet Norashikin, Mohd Hatta
author_sort Norashikin, Mohd Hatta
title Development of heterogeneous base catalyst for transesterification reaction
title_short Development of heterogeneous base catalyst for transesterification reaction
title_full Development of heterogeneous base catalyst for transesterification reaction
title_fullStr Development of heterogeneous base catalyst for transesterification reaction
title_full_unstemmed Development of heterogeneous base catalyst for transesterification reaction
title_sort development of heterogeneous base catalyst for transesterification reaction
publishDate 2010
url http://umpir.ump.edu.my/id/eprint/3196/1/CD5634_NORASHIKIN_MOHD_HATTA.pdf
http://umpir.ump.edu.my/id/eprint/3196/
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score 13.159267