Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters

Fatty acid methyl ester, also known as biodiesel, is a sustainable and clean-burning fuel that can be a substitute for conventional diesel. However, the production of biodiesel requires higher costs compared to conventional diesel. The cost of production can be reduced by using waste cooking oil (WC...

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Published in:Malaysian Journal of Chemistry
Main Author: Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
Format: Article
Language:English
Published: Malaysian Institute of Chemistry 2024
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209945343&doi=10.55373%2fmjchem.v26i5.315&partnerID=40&md5=522a446657527ebda6080660bec04846
id 2-s2.0-85209945343
spelling 2-s2.0-85209945343
Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
2024
Malaysian Journal of Chemistry
26
5
10.55373/mjchem.v26i5.315
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209945343&doi=10.55373%2fmjchem.v26i5.315&partnerID=40&md5=522a446657527ebda6080660bec04846
Fatty acid methyl ester, also known as biodiesel, is a sustainable and clean-burning fuel that can be a substitute for conventional diesel. However, the production of biodiesel requires higher costs compared to conventional diesel. The cost of production can be reduced by using waste cooking oil (WCO) as feedstock. In this study, biodiesel production was carried out via transesterification using WCO as feedstock, and potassium hydroxide (KOH)/bentonite catalyst was used as a heterogeneous catalyst. Different molar ratios of KOH/bentonite catalysts (1:2, 1:3, 1:4, 1:5, and 1:6) were prepared by the impregnation of bentonite with KOH at 60 °C for 6 h. Both raw bentonite and KOH/bentonite catalyst were characterized using thermogravimetric analysis (TGA), Brunauer-Emmett-Teller (BET) surface analysis, X-ray diffraction (XRD), Fourier transform infrared (FTIR) spectroscopy, and scanning electron microscopy (SEM). The decrease of BET surface area in raw bentonite and KOH/bentonite catalyst and the presence of potassium oxide phase in the XRD pattern showed that KOH was successfully impregnated into the pores of bentonite. Moreover, SEM analysis indicated that the granular size of KOH/bentonite was higher than raw bentonite due to aggregation. A high free fatty acid (FFA) conversion of 27.55% was obtained at an optimum molar ratio of KOH/bentonite of 1:5 under the reaction parameters of methanol-to-oil molar ratio of 6:1, reaction temperature of 60 °C, catalyst concentration of 3 wt.%, and reaction time of 3 h. The reusability test determined that the performance of the KOH/bentonite catalyst decreased from 27.55% to 13.73% in FFA conversion. This research reveals that KOH/bentonite catalyst has great potential to produce biodiesel using of WCO as feedstock. © 2024 Malaysian Institute of Chemistry. All rights reserved.
Malaysian Institute of Chemistry
15112292
English
Article

author Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
spellingShingle Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
author_facet Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
author_sort Shukor N.A.S.; Yusof I.; Samad W.Z.; Saleh S.H.; Hamzah N.
title Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
title_short Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
title_full Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
title_fullStr Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
title_full_unstemmed Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
title_sort Synthesis and Characterization of KOH/Bentonite Catalyst for Transesterification of Waste Cooking Oil into Fatty Acid Methyl Esters
publishDate 2024
container_title Malaysian Journal of Chemistry
container_volume 26
container_issue 5
doi_str_mv 10.55373/mjchem.v26i5.315
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85209945343&doi=10.55373%2fmjchem.v26i5.315&partnerID=40&md5=522a446657527ebda6080660bec04846
description Fatty acid methyl ester, also known as biodiesel, is a sustainable and clean-burning fuel that can be a substitute for conventional diesel. However, the production of biodiesel requires higher costs compared to conventional diesel. The cost of production can be reduced by using waste cooking oil (WCO) as feedstock. In this study, biodiesel production was carried out via transesterification using WCO as feedstock, and potassium hydroxide (KOH)/bentonite catalyst was used as a heterogeneous catalyst. Different molar ratios of KOH/bentonite catalysts (1:2, 1:3, 1:4, 1:5, and 1:6) were prepared by the impregnation of bentonite with KOH at 60 °C for 6 h. Both raw bentonite and KOH/bentonite catalyst were characterized using thermogravimetric analysis (TGA), Brunauer-Emmett-Teller (BET) surface analysis, X-ray diffraction (XRD), Fourier transform infrared (FTIR) spectroscopy, and scanning electron microscopy (SEM). The decrease of BET surface area in raw bentonite and KOH/bentonite catalyst and the presence of potassium oxide phase in the XRD pattern showed that KOH was successfully impregnated into the pores of bentonite. Moreover, SEM analysis indicated that the granular size of KOH/bentonite was higher than raw bentonite due to aggregation. A high free fatty acid (FFA) conversion of 27.55% was obtained at an optimum molar ratio of KOH/bentonite of 1:5 under the reaction parameters of methanol-to-oil molar ratio of 6:1, reaction temperature of 60 °C, catalyst concentration of 3 wt.%, and reaction time of 3 h. The reusability test determined that the performance of the KOH/bentonite catalyst decreased from 27.55% to 13.73% in FFA conversion. This research reveals that KOH/bentonite catalyst has great potential to produce biodiesel using of WCO as feedstock. © 2024 Malaysian Institute of Chemistry. All rights reserved.
publisher Malaysian Institute of Chemistry
issn 15112292
language English
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