Production of FAME from acid oil model using immobilized Candida antarctica lipase

Abstract Acid oil is a by‐product in the neutralization step of vegetable oil refining and is an alternative source of biodiesel fuel. A model substrate of acid oil, which is composed of TAG and FFA, was used in experiments on the conversion to FAME by immobilized Candida antarctica lipase. FFA in t...

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Published in:Journal of the American Oil Chemists' Society
Main Authors: Watanabe, Yomi, Pinsirodom, Praphan, Nagao, Toshihiro, Kobayashi, Takashi, Nishida, Yutaka, Takagi, Yoshiaki, Shimada, Yuji
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2005
Subjects:
Online Access:https://doi.org/10.1007/s11746-005-1150-x
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1007%2Fs11746-005-1150-x
http://onlinelibrary.wiley.com/wol1/doi/10.1007/s11746-005-1150-x/fullpdf
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author Watanabe, Yomi
Pinsirodom, Praphan
Nagao, Toshihiro
Kobayashi, Takashi
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
author_facet Watanabe, Yomi
Pinsirodom, Praphan
Nagao, Toshihiro
Kobayashi, Takashi
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
author_sort Watanabe, Yomi
collection Wiley Online Library
container_issue 11
container_start_page 825
container_title Journal of the American Oil Chemists' Society
container_volume 82
description Abstract Acid oil is a by‐product in the neutralization step of vegetable oil refining and is an alternative source of biodiesel fuel. A model substrate of acid oil, which is composed of TAG and FFA, was used in experiments on the conversion to FAME by immobilized Candida antarctica lipase. FFA in the mixture of TAG/FFA were efficiently esterified with methanol (MeOH), but the water generated by the esterification significantly inhibited methanolysis of TAG. We thus attempted to convert a mixture of TAG/FFA to FAME by a two‐step process comprising methyl esterification of FFA and methanolysis of TAG by immobilized C. antarctica lipase. The first reaction was conducted at 30°C in a mixture of TAG/FFA (1∶1, wt/wt) and 10 wt% MeOH using 0.5 wt% immobilized lipase, resulting in efficient esterification of FFA. The reaction mixture after 24 h was composed of 49.1 wt% TAG, 1.3 wt% FFA, 49.1 wt% FAME, and negligible amounts of DAG and MAG (<0.5 wt%). The reaction mixture was then dehydrated and used as a substrate for the second reaction, which was conducted at 30°C in a solution of the dehydrated mixture and 5.5 wt% MeOH using 6 wt% immobilized lipase. The activity of the lipase increased gradually when the reaction was repeated by transferring the enzyme to a fresh substrate mixture. The activity reached a maximum after 6 cycles, and the content of FAME achieved was >98.5 wt% after a 24‐h reaction. The immobilized lipase was very stable in the first‐and second‐step reactions and could be used for >100 d without significant loss of activity.
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op_source Journal of the American Oil Chemists' Society
volume 82, issue 11, page 825-831
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spelling crwiley:10.1007/s11746-005-1150-x 2025-01-16T19:37:24+00:00 Production of FAME from acid oil model using immobilized Candida antarctica lipase Watanabe, Yomi Pinsirodom, Praphan Nagao, Toshihiro Kobayashi, Takashi Nishida, Yutaka Takagi, Yoshiaki Shimada, Yuji 2005 https://doi.org/10.1007/s11746-005-1150-x https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1007%2Fs11746-005-1150-x http://onlinelibrary.wiley.com/wol1/doi/10.1007/s11746-005-1150-x/fullpdf en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor Journal of the American Oil Chemists' Society volume 82, issue 11, page 825-831 ISSN 0003-021X 1558-9331 journal-article 2005 crwiley https://doi.org/10.1007/s11746-005-1150-x 2024-12-09T19:49:25Z Abstract Acid oil is a by‐product in the neutralization step of vegetable oil refining and is an alternative source of biodiesel fuel. A model substrate of acid oil, which is composed of TAG and FFA, was used in experiments on the conversion to FAME by immobilized Candida antarctica lipase. FFA in the mixture of TAG/FFA were efficiently esterified with methanol (MeOH), but the water generated by the esterification significantly inhibited methanolysis of TAG. We thus attempted to convert a mixture of TAG/FFA to FAME by a two‐step process comprising methyl esterification of FFA and methanolysis of TAG by immobilized C. antarctica lipase. The first reaction was conducted at 30°C in a mixture of TAG/FFA (1∶1, wt/wt) and 10 wt% MeOH using 0.5 wt% immobilized lipase, resulting in efficient esterification of FFA. The reaction mixture after 24 h was composed of 49.1 wt% TAG, 1.3 wt% FFA, 49.1 wt% FAME, and negligible amounts of DAG and MAG (<0.5 wt%). The reaction mixture was then dehydrated and used as a substrate for the second reaction, which was conducted at 30°C in a solution of the dehydrated mixture and 5.5 wt% MeOH using 6 wt% immobilized lipase. The activity of the lipase increased gradually when the reaction was repeated by transferring the enzyme to a fresh substrate mixture. The activity reached a maximum after 6 cycles, and the content of FAME achieved was >98.5 wt% after a 24‐h reaction. The immobilized lipase was very stable in the first‐and second‐step reactions and could be used for >100 d without significant loss of activity. Article in Journal/Newspaper Antarc* Antarctica Wiley Online Library Journal of the American Oil Chemists' Society 82 11 825 831
spellingShingle Watanabe, Yomi
Pinsirodom, Praphan
Nagao, Toshihiro
Kobayashi, Takashi
Nishida, Yutaka
Takagi, Yoshiaki
Shimada, Yuji
Production of FAME from acid oil model using immobilized Candida antarctica lipase
title Production of FAME from acid oil model using immobilized Candida antarctica lipase
title_full Production of FAME from acid oil model using immobilized Candida antarctica lipase
title_fullStr Production of FAME from acid oil model using immobilized Candida antarctica lipase
title_full_unstemmed Production of FAME from acid oil model using immobilized Candida antarctica lipase
title_short Production of FAME from acid oil model using immobilized Candida antarctica lipase
title_sort production of fame from acid oil model using immobilized candida antarctica lipase
url https://doi.org/10.1007/s11746-005-1150-x
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1007%2Fs11746-005-1150-x
http://onlinelibrary.wiley.com/wol1/doi/10.1007/s11746-005-1150-x/fullpdf