Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification

Abstract Acid oil, a by‐product of vegetable oil refining, was enzymatically converted to fatty acid methyl esters (FAME). Acid oil contained free fatty acids (FFA), acylglycerols, and lipophilic compounds. First, acylglycerols (11 wt%) were hydrolyzed at 30 °C by 20 units Candida rugosa lipase/g‐mi...

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Published in:Journal of the American Oil Chemists' Society
Main Authors: Watanabe, Yomi, Nagao, Toshihiro, Nishida, Yutaka, Takagi, Yoshiaki, Shimada, Yuji
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2007
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Online Access:http://dx.doi.org/10.1007/s11746-007-1143-4
https://onlinelibrary.wiley.com/doi/full/10.1007/s11746-007-1143-4
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spelling crwiley:10.1007/s11746-007-1143-4 2024-09-15T17:40:34+00:00 Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification Watanabe, Yomi Nagao, Toshihiro Nishida, Yutaka Takagi, Yoshiaki Shimada, Yuji 2007 http://dx.doi.org/10.1007/s11746-007-1143-4 https://onlinelibrary.wiley.com/doi/full/10.1007/s11746-007-1143-4 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor Journal of the American Oil Chemists' Society volume 84, issue 11, page 1015-1021 ISSN 0003-021X 1558-9331 journal-article 2007 crwiley https://doi.org/10.1007/s11746-007-1143-4 2024-08-13T04:16:08Z Abstract Acid oil, a by‐product of vegetable oil refining, was enzymatically converted to fatty acid methyl esters (FAME). Acid oil contained free fatty acids (FFA), acylglycerols, and lipophilic compounds. First, acylglycerols (11 wt%) were hydrolyzed at 30 °C by 20 units Candida rugosa lipase/g‐mixture with 40 wt% water. The resulting oil layer containing 92 wt% FFA was used for the next reaction, methyl esterification of FFA to FAME by immobilized Candida antarctica lipase. A mixture of 66 wt% oil layer and 34 wt% methanol (5 mol for FFA) were shaken at 30 °C with 1.0 wt% lipase. The degree of esterification reached 96% after 24 h. The resulting reaction mixture was then dehydrated and subjected to the second esterification that was conducted with 2.2 wt% methanol (5 mol for residual FFA) and 1.0 wt% immobilized lipase. The degree of esterification of residual FFA reached 44%. The degree increased successfully to 72% (total degree of esterification 99%) by conducting the reaction in the presence of 10 wt% glycerol, because water in the oil layer was attracted to the glycerol layer. Over 98% of total esterification was maintained, even though the first and the second esterification reactions were repeated every 24 h for 40 days. The enzymatic process comprising hydrolysis and methyl esterification produced an oil containing 91 wt% FAME, 1 wt% FFA, 1 wt% acylglycerols, and 7 wt% lipophilic compounds. Article in Journal/Newspaper Antarc* Antarctica Wiley Online Library Journal of the American Oil Chemists' Society 84 11 1015 1021
institution Open Polar
collection Wiley Online Library
op_collection_id crwiley
language English
description Abstract Acid oil, a by‐product of vegetable oil refining, was enzymatically converted to fatty acid methyl esters (FAME). Acid oil contained free fatty acids (FFA), acylglycerols, and lipophilic compounds. First, acylglycerols (11 wt%) were hydrolyzed at 30 °C by 20 units Candida rugosa lipase/g‐mixture with 40 wt% water. The resulting oil layer containing 92 wt% FFA was used for the next reaction, methyl esterification of FFA to FAME by immobilized Candida antarctica lipase. A mixture of 66 wt% oil layer and 34 wt% methanol (5 mol for FFA) were shaken at 30 °C with 1.0 wt% lipase. The degree of esterification reached 96% after 24 h. The resulting reaction mixture was then dehydrated and subjected to the second esterification that was conducted with 2.2 wt% methanol (5 mol for residual FFA) and 1.0 wt% immobilized lipase. The degree of esterification of residual FFA reached 44%. The degree increased successfully to 72% (total degree of esterification 99%) by conducting the reaction in the presence of 10 wt% glycerol, because water in the oil layer was attracted to the glycerol layer. Over 98% of total esterification was maintained, even though the first and the second esterification reactions were repeated every 24 h for 40 days. The enzymatic process comprising hydrolysis and methyl esterification produced an oil containing 91 wt% FAME, 1 wt% FFA, 1 wt% acylglycerols, and 7 wt% lipophilic compounds.
format Article in Journal/Newspaper
author Watanabe, Yomi
Nagao, Toshihiro
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
spellingShingle Watanabe, Yomi
Nagao, Toshihiro
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
author_facet Watanabe, Yomi
Nagao, Toshihiro
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
author_sort Watanabe, Yomi
title Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
title_short Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
title_full Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
title_fullStr Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
title_full_unstemmed Enzymatic Production of Fatty Acid Methyl Esters by Hydrolysis of Acid Oil Followed by Esterification
title_sort enzymatic production of fatty acid methyl esters by hydrolysis of acid oil followed by esterification
publisher Wiley
publishDate 2007
url http://dx.doi.org/10.1007/s11746-007-1143-4
https://onlinelibrary.wiley.com/doi/full/10.1007/s11746-007-1143-4
genre Antarc*
Antarctica
genre_facet Antarc*
Antarctica
op_source Journal of the American Oil Chemists' Society
volume 84, issue 11, page 1015-1021
ISSN 0003-021X 1558-9331
op_rights http://onlinelibrary.wiley.com/termsAndConditions#vor
op_doi https://doi.org/10.1007/s11746-007-1143-4
container_title Journal of the American Oil Chemists' Society
container_volume 84
container_issue 11
container_start_page 1015
op_container_end_page 1021
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