Please use this identifier to cite or link to this item: http://hdl.handle.net/10773/34808
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dc.contributor.authorVicente, Filipa A.pt_PT
dc.contributor.authorCastro, Leonor S.pt_PT
dc.contributor.authorMondal, Dibyendupt_PT
dc.contributor.authorCoutinho, João A. P.pt_PT
dc.contributor.authorTavares, Ana P. M.pt_PT
dc.contributor.authorVentura, Sónia P. M.pt_PT
dc.contributor.authorFreire, Mara G.pt_PT
dc.date.accessioned2022-09-28T09:52:44Z-
dc.date.available2022-09-28T09:52:44Z-
dc.date.issued2022-05-01-
dc.identifier.issn1383-5866pt_PT
dc.identifier.urihttp://hdl.handle.net/10773/34808-
dc.description.abstractImmunoglobulin Y (IgY) represents an important class of antibodies, being present in egg yolk, with relevant medical applications and involving non-invasive methods of extraction. However, due to the complexity of egg yolk, the purification levels required for use in most medical applications demands the application of multi-step and cost-intensive techniques. Therefore, it is of upmost importance to develop a biocompatible and cost-effective downstream process to purify IgY from egg yolk. In this work, IgY was purified from the egg yolk water-soluble protein fraction (WSPF) by the application of thermoresponsive aqueous micellar two-phase systems (AMTPS) composed of the non-ionic surfactant Triton X-114 and surface-active ionic liquids (SAILs) as co-surfactants. The best thermoresponsive systems allowed, in a single step, to recover IgY in the surfactant-poor phase with a purity level of 69%, and up to 73% if consecutive extraction cycles are performed, while maintaining the structural integrity of the antibodies. Considering these results, a downstream process was designed and proposed, consisting of four main steps: (i) recovery of the WSPF; (ii) purification of IgY by applying AMTPS; (iii) isolation of the IgY from the main solvents using an ultrafiltration step; (iv) recycling of the AMTPS phase-forming components by precipitating the contaminant proteins.pt_PT
dc.language.isoengpt_PT
dc.publisherElsevierpt_PT
dc.relationinfo:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F50011%2F2020/PTpt_PT
dc.relationinfo:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDP%2F50011%2F2020/PTpt_PT
dc.relationinfo:eu-repo/grantAgreement/FCT/FARH/SFRH%2FBD%2F101683%2F2014/PTpt_PT
dc.relation2020/05090/BDpt_PT
dc.relationCEECIND/2020/01867pt_PT
dc.relationinfo:eu-repo/grantAgreement/EC/H2020/899921/EUpt_PT
dc.rightsopenAccesspt_PT
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/pt_PT
dc.subjectImmunoglobulin Ypt_PT
dc.subjectPurificationpt_PT
dc.subjectThermoresponsive systempt_PT
dc.subjectMicellar systemspt_PT
dc.subjectSurfactantspt_PT
dc.subjectSurface-active ionic liquidspt_PT
dc.titlePurification of immunoglobulin Y from egg yolk using thermoresponsive aqueous micellar two-phase systems comprising ionic liquidspt_PT
dc.typearticlept_PT
dc.description.versionpublishedpt_PT
dc.peerreviewedyespt_PT
degois.publication.titleSeparation and Purification Technologypt_PT
degois.publication.volume288pt_PT
dc.identifier.doi10.1016/j.seppur.2022.120589pt_PT
dc.identifier.essn1873-3794pt_PT
dc.identifier.articlenumber120589pt_PT
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DQ - Artigos

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