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http://hdl.handle.net/10773/34808
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DC Field | Value | Language |
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dc.contributor.author | Vicente, Filipa A. | pt_PT |
dc.contributor.author | Castro, Leonor S. | pt_PT |
dc.contributor.author | Mondal, Dibyendu | pt_PT |
dc.contributor.author | Coutinho, João A. P. | pt_PT |
dc.contributor.author | Tavares, Ana P. M. | pt_PT |
dc.contributor.author | Ventura, Sónia P. M. | pt_PT |
dc.contributor.author | Freire, Mara G. | pt_PT |
dc.date.accessioned | 2022-09-28T09:52:44Z | - |
dc.date.available | 2022-09-28T09:52:44Z | - |
dc.date.issued | 2022-05-01 | - |
dc.identifier.issn | 1383-5866 | pt_PT |
dc.identifier.uri | http://hdl.handle.net/10773/34808 | - |
dc.description.abstract | Immunoglobulin 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.iso | eng | pt_PT |
dc.publisher | Elsevier | pt_PT |
dc.relation | info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F50011%2F2020/PT | pt_PT |
dc.relation | info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDP%2F50011%2F2020/PT | pt_PT |
dc.relation | info:eu-repo/grantAgreement/FCT/FARH/SFRH%2FBD%2F101683%2F2014/PT | pt_PT |
dc.relation | 2020/05090/BD | pt_PT |
dc.relation | CEECIND/2020/01867 | pt_PT |
dc.relation | info:eu-repo/grantAgreement/EC/H2020/899921/EU | pt_PT |
dc.rights | openAccess | pt_PT |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | pt_PT |
dc.subject | Immunoglobulin Y | pt_PT |
dc.subject | Purification | pt_PT |
dc.subject | Thermoresponsive system | pt_PT |
dc.subject | Micellar systems | pt_PT |
dc.subject | Surfactants | pt_PT |
dc.subject | Surface-active ionic liquids | pt_PT |
dc.title | Purification of immunoglobulin Y from egg yolk using thermoresponsive aqueous micellar two-phase systems comprising ionic liquids | pt_PT |
dc.type | article | pt_PT |
dc.description.version | published | pt_PT |
dc.peerreviewed | yes | pt_PT |
degois.publication.title | Separation and Purification Technology | pt_PT |
degois.publication.volume | 288 | pt_PT |
dc.identifier.doi | 10.1016/j.seppur.2022.120589 | pt_PT |
dc.identifier.essn | 1873-3794 | pt_PT |
dc.identifier.articlenumber | 120589 | pt_PT |
Appears in Collections: | CICECO - Artigos DQ - Artigos |
Files in This Item:
File | Description | Size | Format | |
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1-s2.0-S1383586622001496-main (2).pdf | 2 MB | Adobe PDF | View/Open |
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