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Downstream Processes BIE/CEE 5930/6930 Spring 2010
13

Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Dec 20, 2015

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Page 1: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Downstream Processes

BIE/CEE 5930/6930Spring 2010

Page 2: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Aqueous Two-phase Extraction

• Made by combining two water-soluble polymers or a polymer and salt in water

• Above a “critical concentration” phase separation occurs – Two immiscible liquid phases are formed– One phase is enriched in one polymer and other phase is

enriched in other polymer or salt

Page 3: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

• Can be used to separate proteins, cells, cell organelles, nucleic acids, polysaccharides.

• Examples– Polymer/polymer: Poly-ethylene glycol (PEG)/Dextran– Polymer/salt: PEG/(NH4)2SO4 (ammonium sulfate)

Page 4: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Aqueous Two-phase Extraction• PEG-water phase is

typically lighter and floats

• Water-salt or water-dextran phases are heavier

• Typical concentrations– PEG/Dextran: 10%:15%– PEG/salt: 15%:15%

Page 5: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Factors that Affect Protein Partitioning

• Protein Molecular Weight• Protein charge and surface properties• Polymer(s) molecular weight• Phase composition of the system• Salt effects• Affinity ligands attached to the polymers

Page 6: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Aqueous Two-phase Extraction• Cells and cell debris settle to the bottom phase or stay at

the interface• Protein can stay in either phase• Partition coefficient is a function of protein size and

properties

ConstantBoltzmann theisk

molecule theof properties on thedependent constant a is

re temperatuabsolute theis

protein theofweight molecular theis

exp

T

M

kT

MK

Page 7: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

constant gas theis

number Faraday is

protein theof charge surfacenet theis

phaseheavy andlight for potential electrical are and

polymer and protein between parameters ninteractio are and

phase andlight in 2polymer of ionsconcentrat are ,

phase andlight in 1polymer of ionsconcentrat are ,

where

)()()(ln

21

22

11

222111

R

F

Z

aa

xy

xy

RT

ZFyxayxaK

yx

pp

yxpp

Page 8: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Aqueous Two-phase Extraction

Page 9: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

• Below the line is a single phase

• On the line is two phases

• The tie-line connect compositions that are in equilibrium

Page 10: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Typical concentrations of systems:

• PEG – Dextran 10% w/w PEG, 15% Dextran

• PEG – Salt 15% w/w PEG, 15% Salt

Page 11: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Effect of Salt Concentration

Page 12: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Effect of protein molecular weight

Page 13: Downstream Processes BIE/CEE 5930/6930 Spring 2010.

Typical process flow diagram