Aqueous two-phase systems for protein separation: Phase separation and applications
Author
dc.contributor.author
Asenjo de Leuze, Juan
Author
dc.contributor.author
Andrews Farrow, Bárbara
es_CL
Admission date
dc.date.accessioned
2013-12-20T18:25:51Z
Available date
dc.date.available
2013-12-20T18:25:51Z
Publication date
dc.date.issued
2010
Cita de ítem
dc.identifier.citation
Journal of Chromatography A, 1238 (2012) 1– 10
en_US
Identifier
dc.identifier.other
doi:10.1016/j.chroma.2012.03.049
Identifier
dc.identifier.uri
https://repositorio.uchile.cl/handle/2250/125820
General note
dc.description
Artículo de publicación ISI
en_US
Abstract
dc.description.abstract
Aqueous two-phase systems (ATPS) that are formed by mixing a polymer (usually polyethylene glycol,
PEG) and a salt (e.g. phosphate, sulphate or citrate) or two polymers, and water can be effectively used
for the separation and purification of proteins. The partitioning between both phases is dependent on the
surface properties of the proteins and on the composition of the two phase system as has been recently
reviewed by Asenjo and Andrews [1]. This paper analyses and reviews some elements that are important
for implementation of these processes which are related to phase separation and continuous processing
of ATPS. Phase separation for ATPS formed by PEG and salts has been studied and has been found to
depend on which of the phases is continuous. Profiles of dispersion heights can be represented as a
fraction of the initial height and are independent of the dimensions of the separator. This is important
for the design of large scale aqueous two-phase separations. The kinetics of phase separation has been
investigated as a function of the physical properties of the system. The settling rate is a crucial parameter
for equipment design and it has been studied as a function of viscosity and density of the phases as
well as the interfacial tension between them. Correlations that describe the rate of phase separation
have been developed. Working in a continuous bottom-phase region is advantageous to ensure fast
separation. A mathematical model to describe the continuous, study state operation of these systems has
been investigated. Two simulations to show the effect of phase ratio on purification have been carried
out which clearly show the effectivity of using such models. The practical application of ATPS has been
demonstrated in many cases including a number of industrial applications with excellent levels of purity
and yield. Examples include the purification of -amylase and the large scale “in situ” purification of IGF-
1 carried out by Genentech. The production scale purification of chymosin from recombinant Aspergillus
supernatant is the most successful industrial application of this technology. Other applications include
the separation and purification of human -antitrypsin from transgenic sheep milk, the purification of
monoclonal antibodies, tPA from CHO supernatant and recombinant VLPs (virus like particles) from yeast
cells.