Kalaivani, S.Iyyaswami, I.2026-02-052016Separation Science and Technology, 2016, 51, 14, pp. 2411-24191496395https://doi.org/10.1080/01496395.2016.1202278https://idr.nitk.ac.in/handle/123456789/25914The 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.ExtractionAqueous two-phase extractionContinuous aqueous two-phase extractionsDifferential partitioningExtraction efficienciesOperating variablesRotating disc contactorTri-sodium citratesWhey proteinsMass transfer