Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts

The esterification of free fatty acids (FFA) in used cooking oil was investigated using gelular ion exchange resins, SK104H and SK1BH catalysts. Characterization methods such as Fourier transform-infra red (FT-IR) spectroscopy, particle size distribution (PSD), scanning electron microscopy (SEM), el...

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Main Authors: Nursofia, Mohd Yunus, Nurul Asmawati, Roslan, Chin, S. Y., Sumaiya, Zainal Abidin
Format: Article
Language:English
English
Published: Elsevier Ltd 2016
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/13866/
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http://umpir.ump.edu.my/id/eprint/13866/1/Esterification%20of%20Free%20Fatty%20Acid%20in%20Used%20Cooking%20Oil%20Using%20Gelular%20Exchange%20Resin%20as%20Catalysts.pdf
http://umpir.ump.edu.my/id/eprint/13866/7/fkksa-2016-sumaiya-estirification%20of%20free%20fatty.pdf
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spelling ump-138662017-12-14T02:41:34Z http://umpir.ump.edu.my/id/eprint/13866/ Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts Nursofia, Mohd Yunus Nurul Asmawati, Roslan Chin, S. Y. Sumaiya, Zainal Abidin TP Chemical technology The esterification of free fatty acids (FFA) in used cooking oil was investigated using gelular ion exchange resins, SK104H and SK1BH catalysts. Characterization methods such as Fourier transform-infra red (FT-IR) spectroscopy, particle size distribution (PSD), scanning electron microscopy (SEM), elemental analysis (CHNS) and acid capacity analysis were conducted to determine the physicochemical properties of the catalysts. These catalysts were then subjected to a screening study to select the best performance catalyst, which further subjected to esterification reaction using one-variable-at-a-time (OVAAT) method. Using OVAAT method, the effect of mass transfer resistance, catalyst loading, reaction temperature and methanol to oil mass ratio were studied to optimize esterification reaction conditions. The conversion of FFA in the used cooking oil was successfully achieved 88% under optimal conditions of 18:1 methanol to oil mass ratio, reaction temperature of 60oC, catalyst loading of 3.0 wt. % and 300 rpm of stirring speed. Excellence catalytic performance may attributed to the smallest average particle size, high sulfur content and high acid capacity value of SK104H, resulting high conversion of FFA. Elsevier Ltd 2016 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/13866/1/Esterification%20of%20Free%20Fatty%20Acid%20in%20Used%20Cooking%20Oil%20Using%20Gelular%20Exchange%20Resin%20as%20Catalysts.pdf application/pdf en cc_by_nc_nd http://umpir.ump.edu.my/id/eprint/13866/7/fkksa-2016-sumaiya-estirification%20of%20free%20fatty.pdf Nursofia, Mohd Yunus and Nurul Asmawati, Roslan and Chin, S. Y. and Sumaiya, Zainal Abidin (2016) Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts. Procedia Engineering, 148. pp. 1274-1281. ISSN 1877-7058 http://dx.doi.org/10.1016/j.proeng.2016.06.450 doi:10.1016/j.proeng.2016.06.450
repository_type Digital Repository
institution_category Local University
institution Universiti Malaysia Pahang
building UMP Institutional Repository
collection Online Access
language English
English
topic TP Chemical technology
spellingShingle TP Chemical technology
Nursofia, Mohd Yunus
Nurul Asmawati, Roslan
Chin, S. Y.
Sumaiya, Zainal Abidin
Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
description The esterification of free fatty acids (FFA) in used cooking oil was investigated using gelular ion exchange resins, SK104H and SK1BH catalysts. Characterization methods such as Fourier transform-infra red (FT-IR) spectroscopy, particle size distribution (PSD), scanning electron microscopy (SEM), elemental analysis (CHNS) and acid capacity analysis were conducted to determine the physicochemical properties of the catalysts. These catalysts were then subjected to a screening study to select the best performance catalyst, which further subjected to esterification reaction using one-variable-at-a-time (OVAAT) method. Using OVAAT method, the effect of mass transfer resistance, catalyst loading, reaction temperature and methanol to oil mass ratio were studied to optimize esterification reaction conditions. The conversion of FFA in the used cooking oil was successfully achieved 88% under optimal conditions of 18:1 methanol to oil mass ratio, reaction temperature of 60oC, catalyst loading of 3.0 wt. % and 300 rpm of stirring speed. Excellence catalytic performance may attributed to the smallest average particle size, high sulfur content and high acid capacity value of SK104H, resulting high conversion of FFA.
format Article
author Nursofia, Mohd Yunus
Nurul Asmawati, Roslan
Chin, S. Y.
Sumaiya, Zainal Abidin
author_facet Nursofia, Mohd Yunus
Nurul Asmawati, Roslan
Chin, S. Y.
Sumaiya, Zainal Abidin
author_sort Nursofia, Mohd Yunus
title Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
title_short Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
title_full Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
title_fullStr Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
title_full_unstemmed Esterification of Free Fatty Acid in Used Cooking Oil Using Gelular Exchange Resin as Catalysts
title_sort esterification of free fatty acid in used cooking oil using gelular exchange resin as catalysts
publisher Elsevier Ltd
publishDate 2016
url http://umpir.ump.edu.my/id/eprint/13866/
http://umpir.ump.edu.my/id/eprint/13866/
http://umpir.ump.edu.my/id/eprint/13866/
http://umpir.ump.edu.my/id/eprint/13866/1/Esterification%20of%20Free%20Fatty%20Acid%20in%20Used%20Cooking%20Oil%20Using%20Gelular%20Exchange%20Resin%20as%20Catalysts.pdf
http://umpir.ump.edu.my/id/eprint/13866/7/fkksa-2016-sumaiya-estirification%20of%20free%20fatty.pdf
first_indexed 2023-09-18T22:16:57Z
last_indexed 2023-09-18T22:16:57Z
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