Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System

Detalhes bibliográficos
Autor(a) principal: Martins, Margarida
Data de Publicação: 2021
Outros Autores: Mesquita, Leonardo M. de Souza, Vaz, Bárbara M.C., Dias, Ana C.R.V., Torres-Acosta, Mario A., Quéguineur, Benoit, Coutinho, João A.P., Ventura, Sónia P.M.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10773/35550
Resumo: There is a strong industrial interest in the development of greener and more sustainable processes based on the use of renewable resources, and a biorefinery based on marine resources, such as macroalgae, stands as a major opportunity toward that end. In this work, Saccharina latissima (Linnaeus), a brown macroalga, was used as a source of pigments to develop an integrated platform that is able to promote the extraction and separation of chlorophyll and fucoxanthin in one single step. The process was studied, and its operational conditions were optimized with yields of extraction of chlorophyll and fucoxanthin of 4.93 ± 0.22 mgchl·gdry biomass-1 and 1956 ± 84 μgfuco·gdry biomass-1, respectively. These results were achieved with extraction systems composed of 84% of an aqueous solution of a tensioactive phosphonium-based ionic liquid (IL) at 350 mM + 16% of sunflower oil, during 40 min, using a solid-liquid ratio of 0.017 gdry biomass·mLsolvent-1. After the separation of both aqueous IL-rich and oil-rich phases, the IL content in both phases was investigated, the oil phase being free of IL. Envisioning the industrial potential of the process developed in this work, the recovery of the IL from the aqueous IL-rich phase of the initial system was attempted by a back-extraction using organic solvents immiscible in water, being shown that 82% of the IL can be recovered and reused in new cycles of extraction. The environmental and economic impacts of the final process proposed for the extraction and fractionation of chlorophyll and fucoxanthin were evaluated. Different scenarios were considered, but summing up the main results, the solvents' recycling allowed better results, proving the economic and environmental viability of the overall process
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spelling Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water SystemThere is a strong industrial interest in the development of greener and more sustainable processes based on the use of renewable resources, and a biorefinery based on marine resources, such as macroalgae, stands as a major opportunity toward that end. In this work, Saccharina latissima (Linnaeus), a brown macroalga, was used as a source of pigments to develop an integrated platform that is able to promote the extraction and separation of chlorophyll and fucoxanthin in one single step. The process was studied, and its operational conditions were optimized with yields of extraction of chlorophyll and fucoxanthin of 4.93 ± 0.22 mgchl·gdry biomass-1 and 1956 ± 84 μgfuco·gdry biomass-1, respectively. These results were achieved with extraction systems composed of 84% of an aqueous solution of a tensioactive phosphonium-based ionic liquid (IL) at 350 mM + 16% of sunflower oil, during 40 min, using a solid-liquid ratio of 0.017 gdry biomass·mLsolvent-1. After the separation of both aqueous IL-rich and oil-rich phases, the IL content in both phases was investigated, the oil phase being free of IL. Envisioning the industrial potential of the process developed in this work, the recovery of the IL from the aqueous IL-rich phase of the initial system was attempted by a back-extraction using organic solvents immiscible in water, being shown that 82% of the IL can be recovered and reused in new cycles of extraction. The environmental and economic impacts of the final process proposed for the extraction and fractionation of chlorophyll and fucoxanthin were evaluated. Different scenarios were considered, but summing up the main results, the solvents' recycling allowed better results, proving the economic and environmental viability of the overall processAmerican Chemical Society2022-12-22T17:02:53Z2021-01-01T00:00:00Z2021info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10773/35550eng2168-048510.1021/acssuschemeng.0c09110Martins, MargaridaMesquita, Leonardo M. de SouzaVaz, Bárbara M.C.Dias, Ana C.R.V.Torres-Acosta, Mario A.Quéguineur, BenoitCoutinho, João A.P.Ventura, Sónia P.M.info:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2024-02-22T12:08:18Zoai:ria.ua.pt:10773/35550Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-20T03:06:29.323385Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse
dc.title.none.fl_str_mv Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
title Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
spellingShingle Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
Martins, Margarida
title_short Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
title_full Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
title_fullStr Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
title_full_unstemmed Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
title_sort Extraction and Fractionation of Pigments from Saccharina latissima (Linnaeus, 2006) Using an Ionic Liquid + Oil + Water System
author Martins, Margarida
author_facet Martins, Margarida
Mesquita, Leonardo M. de Souza
Vaz, Bárbara M.C.
Dias, Ana C.R.V.
Torres-Acosta, Mario A.
Quéguineur, Benoit
Coutinho, João A.P.
Ventura, Sónia P.M.
author_role author
author2 Mesquita, Leonardo M. de Souza
Vaz, Bárbara M.C.
Dias, Ana C.R.V.
Torres-Acosta, Mario A.
Quéguineur, Benoit
Coutinho, João A.P.
Ventura, Sónia P.M.
author2_role author
author
author
author
author
author
author
dc.contributor.author.fl_str_mv Martins, Margarida
Mesquita, Leonardo M. de Souza
Vaz, Bárbara M.C.
Dias, Ana C.R.V.
Torres-Acosta, Mario A.
Quéguineur, Benoit
Coutinho, João A.P.
Ventura, Sónia P.M.
description There is a strong industrial interest in the development of greener and more sustainable processes based on the use of renewable resources, and a biorefinery based on marine resources, such as macroalgae, stands as a major opportunity toward that end. In this work, Saccharina latissima (Linnaeus), a brown macroalga, was used as a source of pigments to develop an integrated platform that is able to promote the extraction and separation of chlorophyll and fucoxanthin in one single step. The process was studied, and its operational conditions were optimized with yields of extraction of chlorophyll and fucoxanthin of 4.93 ± 0.22 mgchl·gdry biomass-1 and 1956 ± 84 μgfuco·gdry biomass-1, respectively. These results were achieved with extraction systems composed of 84% of an aqueous solution of a tensioactive phosphonium-based ionic liquid (IL) at 350 mM + 16% of sunflower oil, during 40 min, using a solid-liquid ratio of 0.017 gdry biomass·mLsolvent-1. After the separation of both aqueous IL-rich and oil-rich phases, the IL content in both phases was investigated, the oil phase being free of IL. Envisioning the industrial potential of the process developed in this work, the recovery of the IL from the aqueous IL-rich phase of the initial system was attempted by a back-extraction using organic solvents immiscible in water, being shown that 82% of the IL can be recovered and reused in new cycles of extraction. The environmental and economic impacts of the final process proposed for the extraction and fractionation of chlorophyll and fucoxanthin were evaluated. Different scenarios were considered, but summing up the main results, the solvents' recycling allowed better results, proving the economic and environmental viability of the overall process
publishDate 2021
dc.date.none.fl_str_mv 2021-01-01T00:00:00Z
2021
2022-12-22T17:02:53Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
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10.1021/acssuschemeng.0c09110
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dc.publisher.none.fl_str_mv American Chemical Society
publisher.none.fl_str_mv American Chemical Society
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