Continuous aqueous two-phase extraction of ?-lactalbumin from whey in conventional rotating disc contactor

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dc.contributor.authorKalaivani, S.
dc.contributor.authorIyyaswami, I.
dc.date.accessioned2026-02-05T09:32:59Z
dc.date.issued2016
dc.description.abstractThe differential partitioning of ?-La to the PEG-rich phase and ?-Lg to the salt-rich phase was studied in the continuous extractor, rotating disc contactor (RDC), using polyethylene glycol (PEG) 1000–trisodium citrate system. The performance of the extractor was evaluated in terms of holdup, mass transfer coefficient, extraction efficiency, and recovery by studying the operating variables such as phase velocities and rotor speed. The process conditions for the maximum dispersed phase mass transfer coefficient and recovery of ?-La was also obtained and reported. © 2016 Taylor & Francis.
dc.identifier.citationSeparation Science and Technology, 2016, 51, 14, pp. 2411-2419
dc.identifier.issn1496395
dc.identifier.urihttps://doi.org/10.1080/01496395.2016.1202278
dc.identifier.urihttps://idr.nitk.ac.in/handle/123456789/25914
dc.publisherTaylor and Francis Inc. 325 Chestnut St, Suite 800 Philadelphia PA 19106
dc.subjectExtraction
dc.subjectAqueous two-phase extraction
dc.subjectContinuous aqueous two-phase extractions
dc.subjectDifferential partitioning
dc.subjectExtraction efficiencies
dc.subjectOperating variables
dc.subjectRotating disc contactor
dc.subjectTri-sodium citrates
dc.subjectWhey proteins
dc.subjectMass transfer
dc.titleContinuous aqueous two-phase extraction of ?-lactalbumin from whey in conventional rotating disc contactor

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