Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification

TThe aim of this work was to optimize the production of fatty acid methyl ester (FAME, biodiesel) from wet Nannchloropsis gaditana microalgal biomass by direct enzymatic transesterification. This was done in order to avoid the high cost associated with the prior steps of drying and oil extraction. S...

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Published in:Biomass and Bioenergy
Main Authors: Navarro López, Elvira, Robles Medina, Alfonso, Esteban Cerdán, Luis, González Moreno, Pedro Antonio, Macías Sánchez, María Dolores, Molina Grima, Emilio
Format: Article in Journal/Newspaper
Language:English
Published: 2016
Subjects:
Online Access:http://hdl.handle.net/10835/15063
https://doi.org/10.1016/j.biombioe.2016.06.018
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record_format openpolar
spelling ftunivalmeria:oai:repositorio.ual.es:10835/15063 2024-02-11T09:57:19+01:00 Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification Navarro López, Elvira Robles Medina, Alfonso Esteban Cerdán, Luis González Moreno, Pedro Antonio Macías Sánchez, María Dolores Molina Grima, Emilio 2016-06-23 http://hdl.handle.net/10835/15063 https://doi.org/10.1016/j.biombioe.2016.06.018 en eng http://hdl.handle.net/10835/15063 doi:10.1016/j.biombioe.2016.06.018 info:eu-repo/semantics/openAccess Biodiesel Microalga Nannochloropsis gaditana Lipase Direct transesterification Polar lipid info:eu-repo/semantics/article 2016 ftunivalmeria https://doi.org/10.1016/j.biombioe.2016.06.018 2024-01-17T00:19:05Z TThe aim of this work was to optimize the production of fatty acid methyl ester (FAME, biodiesel) from wet Nannchloropsis gaditana microalgal biomass by direct enzymatic transesterification. This was done in order to avoid the high cost associated with the prior steps of drying and oil extraction. Saponifiable lipids (SLs) from microalgal biomass were transformed to FAME using the lipase Novozyme 435 (N435) from Candida antarctica as the catalyst, and finally the FAME were extracted with hexane. t-Butanol was used as the reaction medium so as to decrease lipase deactivation and increase mass transfer velocity. A FAME conversion of 99.5% was achieved using wet microalgal biomass homogenized at 140 MPa to enhance cell disruption, a N435:oil mass ratio of 0.32, methanol added in 3 stages to achieve a total of 4.6 cm3 g−1 of oil and 7.1 cm3 g−1 oil of added t-butanol, with a reaction time of 56 h. The FAME conversion decreased to 57% after catalyzing three reactions with the same lipase batch. This work shows the influence of the polar lipids contained in the microalgal biomass both on the reaction velocity and on lipase activity. Article in Journal/Newspaper Antarc* Antarctica Universidad de Almería: Repositorio Institucional Biomass and Bioenergy 93 6 12
institution Open Polar
collection Universidad de Almería: Repositorio Institucional
op_collection_id ftunivalmeria
language English
topic Biodiesel
Microalga
Nannochloropsis gaditana
Lipase
Direct transesterification
Polar lipid
spellingShingle Biodiesel
Microalga
Nannochloropsis gaditana
Lipase
Direct transesterification
Polar lipid
Navarro López, Elvira
Robles Medina, Alfonso
Esteban Cerdán, Luis
González Moreno, Pedro Antonio
Macías Sánchez, María Dolores
Molina Grima, Emilio
Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
topic_facet Biodiesel
Microalga
Nannochloropsis gaditana
Lipase
Direct transesterification
Polar lipid
description TThe aim of this work was to optimize the production of fatty acid methyl ester (FAME, biodiesel) from wet Nannchloropsis gaditana microalgal biomass by direct enzymatic transesterification. This was done in order to avoid the high cost associated with the prior steps of drying and oil extraction. Saponifiable lipids (SLs) from microalgal biomass were transformed to FAME using the lipase Novozyme 435 (N435) from Candida antarctica as the catalyst, and finally the FAME were extracted with hexane. t-Butanol was used as the reaction medium so as to decrease lipase deactivation and increase mass transfer velocity. A FAME conversion of 99.5% was achieved using wet microalgal biomass homogenized at 140 MPa to enhance cell disruption, a N435:oil mass ratio of 0.32, methanol added in 3 stages to achieve a total of 4.6 cm3 g−1 of oil and 7.1 cm3 g−1 oil of added t-butanol, with a reaction time of 56 h. The FAME conversion decreased to 57% after catalyzing three reactions with the same lipase batch. This work shows the influence of the polar lipids contained in the microalgal biomass both on the reaction velocity and on lipase activity.
format Article in Journal/Newspaper
author Navarro López, Elvira
Robles Medina, Alfonso
Esteban Cerdán, Luis
González Moreno, Pedro Antonio
Macías Sánchez, María Dolores
Molina Grima, Emilio
author_facet Navarro López, Elvira
Robles Medina, Alfonso
Esteban Cerdán, Luis
González Moreno, Pedro Antonio
Macías Sánchez, María Dolores
Molina Grima, Emilio
author_sort Navarro López, Elvira
title Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
title_short Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
title_full Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
title_fullStr Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
title_full_unstemmed Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
title_sort fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification
publishDate 2016
url http://hdl.handle.net/10835/15063
https://doi.org/10.1016/j.biombioe.2016.06.018
genre Antarc*
Antarctica
genre_facet Antarc*
Antarctica
op_relation http://hdl.handle.net/10835/15063
doi:10.1016/j.biombioe.2016.06.018
op_rights info:eu-repo/semantics/openAccess
op_doi https://doi.org/10.1016/j.biombioe.2016.06.018
container_title Biomass and Bioenergy
container_volume 93
container_start_page 6
op_container_end_page 12
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