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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2016
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Online Access: | http://hdl.handle.net/10835/15063 https://doi.org/10.1016/j.biombioe.2016.06.018 |
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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 |
_version_ |
1790609612090638336 |