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Continuous counter-current two-phase aqueous extraction.

J B Joshi1, S B Sawant, K S Rao

  • 1Department of Chemical Technology, University of Bombay, India.

Bioseparation
|January 1, 1990
PubMed
Summary
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Continuous counter-current columns offer convenient protein extraction using aqueous two-phase systems. This study details design parameters for various columns, comparing their efficiency for optimal protein recovery.

Area of Science:

  • Biochemical Engineering
  • Separation Science
  • Process Design

Background:

  • Protein extraction is crucial in biotechnology and pharmaceuticals.
  • Aqueous two-phase systems (ATPS) offer a gentle method for protein partitioning.
  • Efficient contactor design is key for scalable ATPS applications.

Purpose of the Study:

  • To provide a detailed analysis of continuous counter-current column operation for protein extraction using ATPS.
  • To compare the performance of different column types (spray, packed, plate, York-Scheibel) for protein recovery.
  • To offer a step-by-step design procedure and identify future research needs.

Main Methods:

  • Detailed discussion of design parameters for spray, packed, plate, and York-Scheibel columns.

Related Experiment Videos

  • Evaluation of polymer-polymer and polymer-salt ATPS for protein partitioning.
  • Comparative analysis of operating and extraction efficiencies for various contactor types.
  • Main Results:

    • Continuous counter-current column operation simplifies contacting in ATPS for protein extraction.
    • Specific design considerations and performance data are presented for different column configurations.
    • Both polymer-polymer and polymer-salt systems demonstrate effectiveness for protein recovery.

    Conclusions:

    • Continuous column contactors are suitable for industrial-scale protein recovery via ATPS.
    • The choice of column design impacts overall extraction efficiency and operational convenience.
    • Further data are needed to refine design procedures and optimize protein recovery processes.