Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery

This study recovered γ-oryzanol from rice bran acid oil (RBAO), following an initial enzymatic esterification/transesterification to selectively convert its glyceride impurities into fatty acid ethyl esters (FAEEs) or biodiesel. γ-oryzanol was then deprotonated and separated from the biodiesel into...

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Published in:Biofuel Research Journal
Main Author: Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
Format: Article
Language:English
Published: Green Wave Publishing of Canada 2023
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85162941385&doi=10.18331%2fBRJ2023.10.2.3&partnerID=40&md5=117f0ee396bcf20fe9301eeb23280e45
id 2-s2.0-85162941385
spelling 2-s2.0-85162941385
Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
2023
Biofuel Research Journal
10
2
10.18331/BRJ2023.10.2.3
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85162941385&doi=10.18331%2fBRJ2023.10.2.3&partnerID=40&md5=117f0ee396bcf20fe9301eeb23280e45
This study recovered γ-oryzanol from rice bran acid oil (RBAO), following an initial enzymatic esterification/transesterification to selectively convert its glyceride impurities into fatty acid ethyl esters (FAEEs) or biodiesel. γ-oryzanol was then deprotonated and separated from the biodiesel into the resulting aqueous phase via acid-base extraction. Herein, we determine the effects of varying reaction conditions, i.e., ethanol:RBAO molar ratio, temperature, reaction time, enzyme loading, and agitation speed, on the degrees of glyceride removal, γ-oryzanol loss, free fatty acid (FFA) remaining, and biodiesel content. Up to 100% glyceride removal was achieved with a relatively high biodiesel yield (84%) and γ-oryzanol loss as low as 26% under our most suitable reaction conditions (5:1 ethanol:RBAO molar ratio, 40 °C, 24 h reaction time, 10%wt enzyme loading, 200 rpm agitation). Furthermore, of the remaining oryzanol, up to 94% was recovered by the acid-base extraction with 2-4 M ethanolic NaOH solution. Our results suggest that a combination of enzymatic esterification/transesterification with subsequent acid-base extraction offers an efficient alternative approach to the simultaneous production of biodiesel and γ-oryzanol recovery from low-cost RBAO. Based on our analysis of techno-economic and environmental sustainability, integration of the present method into a rice bran oil refinery would make the process profitable, with the minimum use of toxic chemicals and energy. © 2023 BRTeam. All rights reserved.
Green Wave Publishing of Canada
22928782
English
Article
All Open Access; Gold Open Access
author Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
spellingShingle Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
author_facet Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
author_sort Usaku C.; Yahya A.B.; Daisuk P.; Shotipruk A.
title Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
title_short Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
title_full Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
title_fullStr Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
title_full_unstemmed Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
title_sort Enzymatic esterification/transesterification of rice bran acid oil for subsequent γ-oryzanol recovery
publishDate 2023
container_title Biofuel Research Journal
container_volume 10
container_issue 2
doi_str_mv 10.18331/BRJ2023.10.2.3
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85162941385&doi=10.18331%2fBRJ2023.10.2.3&partnerID=40&md5=117f0ee396bcf20fe9301eeb23280e45
description This study recovered γ-oryzanol from rice bran acid oil (RBAO), following an initial enzymatic esterification/transesterification to selectively convert its glyceride impurities into fatty acid ethyl esters (FAEEs) or biodiesel. γ-oryzanol was then deprotonated and separated from the biodiesel into the resulting aqueous phase via acid-base extraction. Herein, we determine the effects of varying reaction conditions, i.e., ethanol:RBAO molar ratio, temperature, reaction time, enzyme loading, and agitation speed, on the degrees of glyceride removal, γ-oryzanol loss, free fatty acid (FFA) remaining, and biodiesel content. Up to 100% glyceride removal was achieved with a relatively high biodiesel yield (84%) and γ-oryzanol loss as low as 26% under our most suitable reaction conditions (5:1 ethanol:RBAO molar ratio, 40 °C, 24 h reaction time, 10%wt enzyme loading, 200 rpm agitation). Furthermore, of the remaining oryzanol, up to 94% was recovered by the acid-base extraction with 2-4 M ethanolic NaOH solution. Our results suggest that a combination of enzymatic esterification/transesterification with subsequent acid-base extraction offers an efficient alternative approach to the simultaneous production of biodiesel and γ-oryzanol recovery from low-cost RBAO. Based on our analysis of techno-economic and environmental sustainability, integration of the present method into a rice bran oil refinery would make the process profitable, with the minimum use of toxic chemicals and energy. © 2023 BRTeam. All rights reserved.
publisher Green Wave Publishing of Canada
issn 22928782
language English
format Article
accesstype All Open Access; Gold Open Access
record_format scopus
collection Scopus
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