Please use this identifier to cite or link to this item:
https://idr.nitk.ac.in/jspui/handle/123456789/10376Full metadata record
| DC Field | Value | Language |
|---|---|---|
| dc.contributor.author | Kalaivani, S. | |
| dc.contributor.author | Regupathi, I. | |
| dc.date.accessioned | 2020-03-31T08:19:02Z | - |
| dc.date.available | 2020-03-31T08:19:02Z | - |
| dc.date.issued | 2016 | |
| dc.identifier.citation | Separation Science and Technology (Philadelphia), 2016, Vol.51, 14, pp.2411-2419 | en_US |
| dc.identifier.uri | http://idr.nitk.ac.in/jspui/handle/123456789/10376 | - |
| dc.description.abstract | The 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. | en_US |
| dc.title | Continuous aqueous two-phase extraction of ?-lactalbumin from whey in conventional rotating disc contactor | en_US |
| dc.type | Article | en_US |
| Appears in Collections: | 1. Journal Articles | |
Files in This Item:
There are no files associated with this item.
Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.