Protic ionic liquids as constituent of aqueous two-phase system based on acetonitrile: Synthesis, phase diagrams and genipin pre-purification

dc.contributor.authorAlves Camêlo, Lídia Cristina
dc.contributor.authorde Souza Dias Santos, Gabriela
dc.contributor.authorLucena de Souza, Ranyere
dc.contributor.authorFaria Soares, Cleide Mara
dc.contributor.authorBrandão Pereira, Jorge Fernando [UNESP]
dc.contributor.authorLima, Álvaro Silva
dc.contributor.institutionUniversidade Tiradentes
dc.contributor.institutionInstituto de Tecnologia e Pesquisa
dc.contributor.institutionUniversidade Estadual Paulista (Unesp)
dc.date.accessioned2020-12-12T01:07:08Z
dc.date.available2020-12-12T01:07:08Z
dc.date.issued2020-03-01
dc.description.abstractThe aim of this study was to evaluate the formation of aqueous two-phase systems (ATPS) based on different protic ionic liquids (PIL), synthesized using amines, and organic or inorganic acid, and acetonitrile (ACN). The ATPSs are used to pre-purify genipin from genipap (Genipa americana L.). All PILs (purity above 98%) were able to form ATPSs with ACN, the size of the biphasic region being directly dependent on salting-out aptitude of PIL anions and relative hydrophilicity of the corresponding cations. The highest solid–liquid extraction of genipin from genipap was achieved by using aqueous ACN solution at 75% (16.79 ± 0.06 mg g−1 dry raw material) as extractant. After the extraction stage, the ATPS was used as an integrated platform to pre-purify the genipin present in the extract. Three different overall mixture point compositions were tested, and those formed by [MEA][H2Cit] (25 wt%) + ACN (45 wt%) + water (30 wt%) at 298.15 ± 1.00 K and 0.10 ± 0.01 MPa showed the highest selectivity (S = 4.202 ± 0.009) and recovery of genipin in top phase (RTG = 56.74 ± 0.04%), and the purification factor in top phase was 5.9 fold.en
dc.description.affiliationPrograma de Pós-Graduação em Engenharia de Processos Universidade Tiradentes, Av. Murilo Dantas 300, Farolândia
dc.description.affiliationInstituto de Tecnologia e Pesquisa, Av. Murilo Dantas 300, Prédio do ITP, Farolândia
dc.description.affiliationDepartment of Bioprocesses and Biotechnology School of Pharmaceutical Sciences São Paulo State University (UNESP), Rodovia Araraquara-Jaú Km 01, Campos Ville
dc.description.affiliationUnespDepartment of Bioprocesses and Biotechnology School of Pharmaceutical Sciences São Paulo State University (UNESP), Rodovia Araraquara-Jaú Km 01, Campos Ville
dc.description.sponsorshipCoordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
dc.description.sponsorshipConselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
dc.description.sponsorshipFundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
dc.description.sponsorshipFundação de Apoio à Pesquisa e à Inovação Tecnológica do Estado de Sergipe
dc.description.sponsorshipIdFAPESP: 2014/16424-7
dc.description.sponsorshipIdCNPq: 304672/2015-7
dc.identifierhttp://dx.doi.org/10.1016/j.fluid.2019.112425
dc.identifier.citationFluid Phase Equilibria, v. 507.
dc.identifier.doi10.1016/j.fluid.2019.112425
dc.identifier.issn0378-3812
dc.identifier.scopus2-s2.0-85075940647
dc.identifier.urihttp://hdl.handle.net/11449/198230
dc.language.isoeng
dc.relation.ispartofFluid Phase Equilibria
dc.sourceScopus
dc.subjectExtraction
dc.subjectGenipin
dc.subjectIntegrated process
dc.subjectPhase equilibria
dc.subjectProtic ionic liquid
dc.titleProtic ionic liquids as constituent of aqueous two-phase system based on acetonitrile: Synthesis, phase diagrams and genipin pre-purificationen
dc.typeArtigo
unesp.author.orcid0000-0003-1682-7929 0000-0003-1682-7929[3]
unesp.author.orcid0000-0002-0603-8187 0000-0002-0603-8187[6]

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