10
2013 http://informahealthcare.com/bty ISSN: 0738-8551 (print), 1549-7801 (electronic) Crit Rev Biotechnol, Early Online: 1–10 ! 2013 Informa Healthcare USA, Inc. DOI: 10.3109/07388551.2013.794125 REVIEW ARTICLE Aqueous two-phase systems strategies to establish novel bioprocesses for stem cells recovery Mirna Gonza ´lez-Gonza ´lez and Marco Rito-Palomares Centro de Biotecnologı ´a-FEMSA, Tecnolo ´gico de Monterrey, Monterrey, NL, Me ´xico Abstract During the past decade, stem cell transplantation has emerged as a novel therapeutic alternative for several diseases. Nevertheless, numerous challenges regarding the recovery and purification steps must be addressed to supply the number of cells required and in the degree of purity needed for clinical treatments. Currently, there is a wide range of methodologies available for stem cells isolation. Nevertheless, there is not a golden standard method that accomplishes all requirements. A desirable recovery method for stem cells has to guarantee high purity and should be sensitive, rapid, quantitative, scalable, non- or minimally invasive to preserve viability and differentiation capacity of the purified cells. In this context, aqueous two- phase systems (ATPS) represent a promising alternative to fulfill the mentioned requirements, promoting the use of stem cell-based therapies for incurable diseases. This practical review focuses on presenting the bases for the development of a novel and scalable bioprocess for the purification of stem cells, with a case scenario of CD133 þ cells. The bioengineering strategies include the application of immunoaffinity ATPS in its multiple variants, including antibody- polymer conjugation, antibody addition and antibody immobilization. Conclusions are drawn in the light of the potential generic implementation of these strategies as an initial step in the establishment of bioprocesses for the purification of stem cells. Keywords Affinity partitioning, ATPS, CD133 þ cells, scale-up, stem/progenitor cells isolation, purification History Received 17 July 2012 Revised 14 March 2013 Accepted 3 April 2013 Published online 16 May 2013 Introduction Stem cells are distinguished for their unique characteristics of self-renewal, proliferation and differentiation capacities. These properties have attracted the attention of researchers due to the potential results that can be achieved with stem cell transplantation. In this sense, purified stem cells have been used as a therapeutic alternative for several incurable, chronic and degenerative diseases, including critical limb ischemia (Burt et al., 2010), chronic ischemic heart disease (Stamm et al., 2007), amyotrophic lateral sclerosis (ALS) (Martinez et al., 2009) and chronic lymphocytic leukemia (Isidori et al., 2007). However, to apply these treatments, special attention must be given to the recovery and purification stages to guarantee the purity and number of stem cells required for a successful transplantation procedure. Isolation of highly purified stem cells is essential for the development of cell- based therapeutics to guarantee removal of undifferentiated and other unwanted cells that could be tumor forming. A desirable recovery method for stem cells has to assure high purity and should be sensitive, rapid, quantitative, scalable, non- or minimally invasive to preserve viability and bio- logical functions (e.g. differentiation capacity) of the purified cells (Gonza ´lez-Gonza ´lez et al., 2012a; Pethig et al., 2010). Currently, there is a wide range of methodologies available for stem cells isolation. These techniques can be classified into three categories: (1) isopycnic centrifugation, including density gradient and cell culture; (2) immunochemical, employing immune labeling; and (3) novel, tagless procedures (Gonza ´lez-Gonza ´lez et al., 2012a). Table 1 highlights the advantages, limitations and performance parameters of some of the current methods employed for stem cell separation that require immuno-tags. In this context, the major constraints of employing immune-affinity separation methodologies are the availability of suitable antibodies and possible elimination of important primitive cell subsets that have not expressed the selection marker (Wognum et al., 2003). Another possible drawback is the need of removing the antibody from the isolated cells, particularly when the antibody alters the surface characteristic of the cells and affects its subsequent use (Tsukamoto et al., 2009). In this context, immunochemical affinity techniques including MACS (Magnetic Activated Cell Sorting) and FACS (Fluorescence Activated Cell Sorting) have become one of the most exploited methods for stem cells purification. This is due to the high specificity conferred by the cell surface marker (cluster of differentiation, CD) that they employ as molecular tagging. For example, one of the most recently used CD for identification of stem cells is the novel CD133. CD133, a five-transmembrane stem cell glycoprotein Address for correspondence: Marco Rito-Palomares, Centro de Biotec- nologı ´a-FEMSA, Tecnolo ´gico de Monterrey. Campus Monterrey, Ave. Eugenio Garza Sada 2501 Sur, Monterrey, NL 64849, Me ´xico. Tel: (52) 81 8328-4132. Fax: (52) 81 8328-4136. E-mail: [email protected] Critical Reviews in Biotechnology Downloaded from informahealthcare.com by 201.100.25.11 on 05/21/13 For personal use only.

Aqueous two-phase systems strategies to establish novel bioprocesses for stem cells recovery

  • Upload
    itesm

  • View
    0

  • Download
    0

Embed Size (px)

Citation preview

2013

http://informahealthcare.com/btyISSN: 0738-8551 (print), 1549-7801 (electronic)

Crit Rev Biotechnol, Early Online: 1–10! 2013 Informa Healthcare USA, Inc. DOI: 10.3109/07388551.2013.794125

REVIEW ARTICLE

Aqueous two-phase systems strategies to establish novel bioprocessesfor stem cells recovery

Mirna Gonzalez-Gonzalez and Marco Rito-Palomares

Centro de Biotecnologıa-FEMSA, Tecnologico de Monterrey, Monterrey, NL, Mexico

Abstract

During the past decade, stem cell transplantation has emerged as a novel therapeuticalternative for several diseases. Nevertheless, numerous challenges regarding the recovery andpurification steps must be addressed to supply the number of cells required and in the degreeof purity needed for clinical treatments. Currently, there is a wide range of methodologiesavailable for stem cells isolation. Nevertheless, there is not a golden standard method thataccomplishes all requirements. A desirable recovery method for stem cells has to guaranteehigh purity and should be sensitive, rapid, quantitative, scalable, non- or minimally invasive topreserve viability and differentiation capacity of the purified cells. In this context, aqueous two-phase systems (ATPS) represent a promising alternative to fulfill the mentioned requirements,promoting the use of stem cell-based therapies for incurable diseases. This practical reviewfocuses on presenting the bases for the development of a novel and scalable bioprocess for thepurification of stem cells, with a case scenario of CD133þ cells. The bioengineering strategiesinclude the application of immunoaffinity ATPS in its multiple variants, including antibody-polymer conjugation, antibody addition and antibody immobilization. Conclusions are drawn inthe light of the potential generic implementation of these strategies as an initial step in theestablishment of bioprocesses for the purification of stem cells.

Keywords

Affinity partitioning, ATPS, CD133þ cells,scale-up, stem/progenitor cells isolation,purification

History

Received 17 July 2012Revised 14 March 2013Accepted 3 April 2013Published online 16 May 2013

Introduction

Stem cells are distinguished for their unique characteristics of

self-renewal, proliferation and differentiation capacities.

These properties have attracted the attention of researchers

due to the potential results that can be achieved with stem cell

transplantation. In this sense, purified stem cells have been

used as a therapeutic alternative for several incurable, chronic

and degenerative diseases, including critical limb ischemia

(Burt et al., 2010), chronic ischemic heart disease (Stamm

et al., 2007), amyotrophic lateral sclerosis (ALS) (Martinez

et al., 2009) and chronic lymphocytic leukemia (Isidori et al.,

2007). However, to apply these treatments, special attention

must be given to the recovery and purification stages to

guarantee the purity and number of stem cells required for a

successful transplantation procedure. Isolation of highly

purified stem cells is essential for the development of cell-

based therapeutics to guarantee removal of undifferentiated

and other unwanted cells that could be tumor forming.

A desirable recovery method for stem cells has to assure high

purity and should be sensitive, rapid, quantitative, scalable,

non- or minimally invasive to preserve viability and bio-

logical functions (e.g. differentiation capacity) of the purified

cells (Gonzalez-Gonzalez et al., 2012a; Pethig et al., 2010).

Currently, there is a wide range of methodologies available for

stem cells isolation. These techniques can be classified into

three categories: (1) isopycnic centrifugation, including

density gradient and cell culture; (2) immunochemical,

employing immune labeling; and (3) novel, tagless procedures

(Gonzalez-Gonzalez et al., 2012a). Table 1 highlights the

advantages, limitations and performance parameters of some

of the current methods employed for stem cell separation that

require immuno-tags. In this context, the major constraints of

employing immune-affinity separation methodologies are

the availability of suitable antibodies and possible elimination

of important primitive cell subsets that have not expressed

the selection marker (Wognum et al., 2003). Another possible

drawback is the need of removing the antibody from the

isolated cells, particularly when the antibody alters the

surface characteristic of the cells and affects its subsequent

use (Tsukamoto et al., 2009).

In this context, immunochemical affinity techniques

including MACS (Magnetic Activated Cell Sorting) and

FACS (Fluorescence Activated Cell Sorting) have become

one of the most exploited methods for stem cells purification.

This is due to the high specificity conferred by the cell surface

marker (cluster of differentiation, CD) that they employ as

molecular tagging. For example, one of the most recently

used CD for identification of stem cells is the novel CD133.

CD133, a five-transmembrane stem cell glycoprotein

Address for correspondence: Marco Rito-Palomares, Centro de Biotec-nologıa-FEMSA, Tecnologico de Monterrey. Campus Monterrey, Ave.Eugenio Garza Sada 2501 Sur, Monterrey, NL 64849, Mexico. Tel: (52)81 8328-4132. Fax: (52) 81 8328-4136. E-mail: [email protected]

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

Tab

le1

.A

dvan

tages

,li

mit

atio

ns

and

per

form

ance

par

amet

ers

of

curr

ent

met

ho

ds

emp

loyed

for

stem

cell

sse

par

atio

n.

Ad

apte

dfr

om

Go

nza

lez-

Go

nza

lez

etal

.(2

01

2b

).

Met

ho

dS

epar

atio

ncr

iter

iaA

dvan

tages

Lim

itat

ion

sS

tem

cell

sou

rce

Pu

rity

(%)

Yie

ld(%

)V

iab

ilit

y(%

)R

efer

ence

Mag

net

icA

ctiv

ated

Cel

lS

ort

er(M

AC

S)

Aff

init

y,m

agn

etis

mH

igh

pu

rity

,lo

wer

cost

vs.

FA

CS

,h

igh

yie

ld,

easy

tou

se,

com

mer

cial

lyav

aila

ble

ind

iffe

ren

tca

pac

itie

s,al

low

sp

osi

tive

and

neg

ativ

ese

lect

ion

Req

uir

esm

agn

etic

bea

ds

wit

han

tib

od

yan

dm

agn

etic

fiel

d,

lon

gp

roce

ssti

me,

sam

ple

pre

par

atio

nre

qu

ired

,n

eed

lab

elre

moval

,al

ters

cell

via

bil

ity,

no

n-m

ult

ipar

a-m

etri

c,lo

wce

llre

cover

y,m

igh

tco

ntr

ibu

teto

cell

dif

-fe

ren

tiat

ion

,o

pti

miz

edp

roto

cols

are

mu

ltis

tep

s

CD

13

leu

kap

her

esis

pro

du

ct9

38

14

95

Lan

get

al.

(20

04

)5

0%

SS

EA

-1þ

mE

SC

cell

mix

ture

(CD

34þ

)9

58

57

0–

80

Sch

rieb

let

al.

(20

10

)

Qu

adru

po

leM

agn

etic

Cel

lS

ort

er(Q

MS

)

Aff

init

y,m

agn

etis

mS

teri

led

isp

osa

ble

flow

chan

-n

el,

con

tin

uo

us,

hig

hes

tth

rou

gh

pu

t,sc

alab

le,

hig

hle

vel

of

T-c

ell

log

dep

leti

on

No

nli

nea

rp

erfo

rman

ce,

cell

loss

du

eto

mag

net

icd

epo

siti

on

CD

34þ

cry

op

rese

rved

leu

ka-

ph

eres

isp

rod

uct

85

84

NR

Jin

get

al.

(20

07

a)

CD

34þ

KG

-1a

and

leu

kap

her

-es

isp

rod

uct

96

60

NR

Jin

get

al.

(20

07

b)

Pan

nin

gA

ffin

ity

Co

mm

erci

ally

avai

lab

le,

sho

rtp

roce

ssti

me,

scal

able

Req

uir

esw

ash

ing

step

,lo

wy

ield

,u

nsp

ecif

icad

hes

ion

,lo

wre

solu

tio

n

CD

34þ

bo

ne

mar

row

70

–9

0N

R8

5L

ebkow

ski

etal

.(1

99

2)

CD

34þ

bo

ne

mar

row

94

74

NR

Car

do

soet

al.

(19

95

)

Aqu

eou

stw

op

has

esy

stem

s(A

TP

S)

Hy

dro

ph

ob

icit

y,si

ze,

net

char

ge

Bio

com

pat

ibil

ity,

lab

elfr

ee,

scal

able

,lo

wen

erg

yin

pu

t,co

nti

nu

ou

s,sh

ort

pro

cess

tim

e,re

cycl

ing

of

cost

lyaf

fin

ity

ligan

ds,

sele

ctiv

ep

arti

tio

n,

sin

gle

step

,h

igh

cell

via

bil

ity,

low

vis

cosi

ty

Low

spec

ific

ity,

inst

abil

ity

of

inte

rph

ase,

lab

scal

e,re

cov-

ery

of

sep

arat

edce

lls,

op

ti-

miz

atio

nre

qu

ires

rep

etit

ive

extr

acti

on

step

s

KG

1b

on

em

arro

w(C

D3

)8

07

5–

80

95

Ku

mar

etal

.(2

00

1)

CD

34þ

wh

ole

um

bil

ical

cord

blo

od

24

59

5N

RS

ou

saet

al.

(20

11

)

NR

,n

ot

rep

ort

ed

2 M. Gonzalez-Gonzalez and M. Rito-Palomares Crit Rev Biotechnol, Early Online: 1–10

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

(Miraglia et al., 1997), that appears to be a reliable marker

for the isolation of neural stem cells (Wu and Wu, 2009)

and has the ability to promote neural growth (Martinez et al.,

2009). Particularly, researchers from Hospital San Jose Tec de

Monterrey (Mexico) have isolated CD133þ stem cells and

transplanted them into the frontal motor cortex in ALS

patients (Martinez et al., 2009). ALS is a neurodegenerative

disease characterized by the rapid weakening and selective

death of neurons. Unfortunately, current purification tech-

niques employed for stem cells treatments are limited by their

potential scale-up feasibility, high costs and complex infra-

structure (specialized instrument, reagents, facilities, main-

tenance and expertise personnel), resulting in a non-generic

process application.

Aqueous two-phase systems (ATPS) represent an attractive

alternative for the recovery of stem cells. ATPS are a liquid-

liquid extraction technique (polymer-polymer, polymer-salt

or novel components) that exhibits several advantages

including biocompatibility, economically attractive, scalable

and low processing time (Benavides & Rito-Palomares, 2008;

Benavides et al., 2011; Hatti-Kaul, 2001; Sinha et al., 2000).

Moreover, if this methodology is complemented with the

use of antibodies (known as immunoaffinity ATPS), a novel

strategy with improved selectivity for the purification of stem

cells that satisfies the requirements previously mentioned

could be achieved.

Even though the method reported by Martinez and

collaborators (2009) obtained successful clinical results, a

latent niche exists for the development of a faster, scalable

and cost-effective procedure that guarantees purity, yield and

the biological activity required for the final application of the

process. This article focuses on presenting a strategic review,

based on our working experience, that provides general rules

and pre-establish the bases for the development of a novel,

faster and scalable procedure with lower downstream costs

for the selective recovery and purification of stem cells

employing immunoaffinity aqueous two-phase systems.

The proposed bioengineering strategies include the potential

implementation of immunoaffinity ATPS in three major

variants: (i) antibody-polymer conjugation, (ii) antibody

addition and (iii) antibody immobilization. In this sense,

immunoaffinity ATPS represent an alternative technique to

establish a potential bioprocess viable for clinical use, thus

promoting the widespread application of stem cells therapy.

Application of ATPS for stem cells recovery andpurification

Stem cells are mostly present in a limited amount in adult

tissues and organs. Moreover, if a rare population of stem

cells is the target object (e.g. CD133þ cells), an efficient

purification method is required. This procedure is hindered by

the considerations of employing a simplified, mild, fast,

reproducible, cost-effective and scalable procedure to obtain

the purity and amount of cells required for clinical settings.

An aqueous two-phase system is a liquid-liquid fraction-

ation technique first employed in the 1950s by Albertsson

that has demonstrated to be a gentle procedure for the

recovery and primary purification of viable and fully

functional high-value biological products, including proteins

Table 2. Advantages and limitations of the immunoaffinity ATPS strategies proposed for stem cells separation.

Immunoaffinity ATPS strategy Advantages Limitations

Antibody-polymer conjugation Most employed Conjugation stepPossible modified phase recycling Detaching stepSmart polymer can be employed Long reaction timesDifferent conjugation reactions available More reagentsPEGs simple modification LaboriousMay apply to various ATPSHigher affinity interactionPositive selection strategy

Antibody additiona) Free antibody Faster Antibody recycling challenging

Simple cell recoveryNo extra stepsLess reagentsLess time-consumingNo polymer forming phase activationPositive selection strategy

b) PEGylated antibody Benefits of PEGylation Conjugation stepBiotin-streptavidin fast conjugation More reagentsCommercially available modified PEGs LaboriousNo polymer forming phase activationMay apply to various ATPSHighly effective reactionSite-specific reaction conserves antibody’s affinityPositive selection strategy

Antibody immobilization Possible phase recycling Immobilization stepNontoxic, biodegradable matrix Detaching step with glass bead matrixDifferent immobilization approaches More processing time prior ATPS stepNo polymer activation More reagentsGreater surface area for selective binding Applied to selective types of ATPSPositive selection strategy Laborious

DOI: 10.3109/07388551.2013.794125 Aqueous two-phase systems strategies for stem cells recovery 3

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

(Albertsson, 1958; Albertsson et al., 1987; Johansson 1985),

cells (Walter et al., 1968; Walter et al., 1969a,b) and

organelles (Albertsson, 1974; Albertsson, 1988; Morre &

Morre, 2000; Morre et al., 1998). The biphasic system

contains more than 80% water as it is composed of two

hydrophilic aqueous solutions. When mixing these two liquids

above certain critical concentrations, immiscible phase

formation is induced. ATPS can be classified depending on

their composition in (i) polymer-polymer, (ii) polymer-salt

and (iii) novel systems including ionic liquids, tree gum,

starch, copolymers and alcohol, among others. The two

structurally distinct hydrophilic and high molecular weight

polymer forming phases could be polyethylene glycol (PEG),

dextran and ficoll, while the salts could be phosphates,

sulfates or citrates. The reader is referred to the volumes by

Walter et al. (1985), Albertsson (1986), Walter & Johansson

(1994), Zaslavsky (1995), and Hatti Kaul (2000) for a broader

explanation of ATPS.

For cell separation, ATPS exploit the affinity of the cells

for the components of either the top, bottom phase or the

interface between phases in one or multiple steps (Kumar &

Bhardwaj, 2008) positioning the cell in the most energetically

favorable location within the system (SooHoo & Walker,

2009). The separation is based on the physicochemical

properties of the cell such as hydrophobicity, size, net surface

charge and membrane properties (Gossett et al., 2010;

Kamihira & Kumar, 2007). As well as the polymeric and

ionic composition of the phases (Malmstrom et al., 1978) and

the selected systems parameters of volume ratio (VR), tie line

length (TLL), pH and temperature (Benavides & Rito-

Palomares, 2008). Moreover, ATPS are advantageous for

cell separation as they are safe, suitable for large-scale

separation, noninvasive, nondestructive, inexpensive, techno-

logically simple and biocompatible to preserve cell viability

and biological functions. Other advantages of the ATPS

separation method is that the cell fractions are not exposed to

differences in pH, osmolarity or ion concentration during the

separation procedure (Malmstrom et al., 1978). Furthermore,

if the technology of ATPS is combined with affinity ligands

(e.g. dyes, metal ions, enzyme inhibitors or antibodies) a

powerful and versatile separation method known as affinity

ATPS is developed (Delgado et al., 1991, 1992; Johansson,

1984; Karr et al., 1988; Kopperschlager & Birkenmeier,

1990) to achieve specific partitioning through cell surface

receptors. This technology has the advantage of exploiting the

highly specific interaction between an antigen and an

antibody raised against it, known as immunoaffinity ATPS.

Thus, is capable of separating the product of interest from the

contaminants even though only small differences in physical

properties such as charge, size and hydrophobicity exist.

Immunoaffinity ATPS can be constructed mainly in three

different ways: (i) antibody-polymer conjugation, (ii) anti-

body addition or (iii) antibody immobilization. In most cases,

the upper phase (frequently PEG) is the polymer that suffers

the chemical modification or where the added antibody must

partition, because the target cell and contaminants have

preference to the bottom phase. In this way, the antibody will

bind the specific target antigen on the cell surface and will

promote the cell’s partition to the phase to which the affinity

ligand is partitioned, enabling them to be easily isolated.

Potential immunoaffinity ATPS bioengineeringstrategies for stem cells recovery and purification

Before discussing the proposed bioengineering ATPS strate-

gies, special attention must be placed when working on the

purification of stem cells. Considerations derived from our

experience are presented with the aim of providing a complete

scenario that could facilitate the understanding and charac-

terization of the partitioning of stem cells in ATPS. First, the

most recommended types of ATPS in the case of stem cell

separation are the polymer-polymer systems. This is empha-

sized, as careful handling is important to allow the preser-

vation of the integrity of the cells. In this respect, the most

adequate solvent is phosphate buffered saline (PBS, pH 7.4,

150 mM NaCl), providing suitable media for the separation of

viable cells. It is not advised to use PEG/salt ATPS due to the

fact that biospecific interactions are usually obstructed by

high salt concentration (Cabral, 2007) and because of the

hypertonicity of the salt component. Even though traditional

polymer-polymer systems are more expensive than polymer-

salts, it is anticipated that the investment and operational costs

of immunoaffinity ATPS represent a lower budget compared

to the MACS and FACS technologies. Moreover, the invest-

ment in polymer-polymer ATPS for the purification of

specific stem cells with potential medical applications

appears highly justified.

The speed of the operation is another important logistical

factor, but thanks to the simplicity of ATPS technology this

does not represent an obstacle. The process requires a few

minutes for the mixing step, after the sample and antibodies

(in the case of immunoaffinity ATPS) have been added.

Afterwards, phase separation is achieved and this could

usually be performed by low-speed centrifugation.

Affinity ATPS is exploited with the introduction of

ligands, for which receptors exist on the material of interest.

The most selective type of affinity ATPS is the antibody-

antigen interaction or so-called immunoaffinity ATPS.

Ideally, the product of interest would be recovered in the

upper phase, leaving the contaminants in the bottom phase.

In such scenario, the recommended ATPS for affinity

approaches are the ones that conserve the top phase clean,

meaning that the target cells and contaminants partition

naturally to the bottom phase (e.g. PEG 10 000-dextran 10 000

and PEG 8000-dextran 500 000). The affinity ligand must

partition into the upper phase and this can be achieved with

two of the previously mentioned immunoaffinity strategies:

(i) antibody-polymer conjugation and (ii) antibody addition.

The first strategy implies that the chemical modification of

one of the phase forming polymers (i.e. PEGylation).

PEGylation is the process of attaching PEG to a molecule

and when performed to an antibody it confers the advantages

of increase circulating half-lives; reduce antigenicity,

immunogenicity and toxicity; improve solubility and bio-

availability; and enhance proteolytic resistance (Chapman,

2002). On the other hand, the antibody addition method

consists of loading free ligands or modified antibodies (e.g.

PEGylated antibody) to the ATPS. The three proposed

strategies imply positive selection, in which the antibody

would be used against a specific surface marker to label the

desired cells.

4 M. Gonzalez-Gonzalez and M. Rito-Palomares Crit Rev Biotechnol, Early Online: 1–10

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

The final objective of immunoaffinity ATPS is to concen-

trate the contaminants and the stem cells of interest in

opposite phases. In this context, the next subsection will focus

on providing a deeper description and the schematic repre-

sentation of each immunoaffinity ATPS strategy, derived

from our work experience, for the particular case scenario of

CD133þ cells purification. Before entering to the immunoaf-

finity strategies, description of a brief explanation concerning

the experimental sample matrix and sample preparation is

addressed.

Sample preparation

Hematopoietic stem cells CD133þ, our product of interest, is

present at very low concentrations in bone marrow, mobilized

peripheral blood or human umbilical cord blood (HUCB),

thus the isolation for further analysis is a complex challenge.

HUCB is selected as the experimental matrix based upon

abundance, simplicity of collection and as the recovery of

suitable samples is a noninvasive and painless procedure. A

pre-enrichment step employing Lymphoprep (Axis-Shield,

Norway) is performed to eliminate water and other contam-

inants. Hence, the mononuclears are separated from platelets

and red blood cells. Additionally, the volume of the sample is

drastically reduced (from 100 mL obtained during a typical

HUCB collection to a concentrated pellet).

Antibody-polymer conjugation

In this approach (Figure 1), the antibody that recognizes the

stem cells of interest would be conjugated to one of the phase

forming polymers through a covalent or noncovalent reaction.

The PEG is commonly selected as the modified phase as most

products partition preferentially to the dextran-rich phase

(Azevedo et al., 2009), leaving the PEG-rich top phase clean

and available to capture the stem cell of interest. Furthermore,

PEG is easily derivatized due to its terminal hydroxyl groups.

For this various reactions have been reported (Azevedo et al.,

2009; Ruiz-Ruiz et al., 2012). Another possibility is to

employ commercially available derivatized PEGs. Likewise,

dextran or other phase-forming polymers could be chemically

modified, in cases where the samples added concentrate in the

opposite polymer phase.

The fundamentals behind this strategy are the positive

selection performed by the antibody coupled to one of the

phase-forming polymers during the mixing step. After phase

formation, the stem cells of interest would be isolated in the

modified phase, leaving contaminants in the opposite phase.

Even though antibody-polymer conjugation has the advan-

tages of exploiting a higher affinity interaction by allowing

the homogenous distribution of the antibody in one of the

phases, it requires additional time and costs for the

derivatization. One alternative to overcome these limitations

is to recycle the modified polymer after detaching the stem

cells of interest.

Another variant of the antibody-polymer conjugation

methodology is to bind the antibody of interest into a third

ligand carrier polymer, which concentrates mainly in one of

the ATPS phases. The advantage of the ligand carriers is that

smart polymers (SP) (sensitive to temperature, pressure, pH or

light) can be employed to facilitate the detaching step.

Examples of this type of SP are presented in various reports

(Kumar et al., 2007; Liu, 2011).

This strategy is the most common way of purifying

products within the affinity strategies, and for stem cells, it is

Figure 1. Schematic representation of the first proposed immunoaffinity ATPS: antibody-polymer conjugation.

DOI: 10.3109/07388551.2013.794125 Aqueous two-phase systems strategies for stem cells recovery 5

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

not the exception. The conjugation of the CD34 antibody

with the temperature-sensitive polymer polyNIPAM (poly-N-

isopropylacrylamide) in an ATPS composed of 4% PEG

8000–5% dextran T500 to isolate CD34þ human acute

myeloid leukemia cells (KG-1) from human T lymphoma

cells (Jurkat) has been reported (Kumar et al., 2001).

Antibody addition

This immunoaffinity ATPS strategy implies the addition of

CD133 antibodies into traditional polymer-polymer systems.

Its advantages are the elimination of the pre-treatment step

required for the chemical activation of the polymer, which

increases the time and cost of the process. The main

difference with the previous strategy is the addition of

antibodies after ATPS construction, instead of being intro-

duced within one of the polymers.

The incorporation of antibodies into ATPS can be achieved

by adding them freely into the solution (Figure 2A).

Alternatively, the antibodies could first be modified to

increase their partition to the desired phase. An easy and

fast approach to perform this improvement is through

PEGylation (Figure 2B). The PEGylation of the CD133-

Biotin antibody has been recently reported through a site-

specific PEGylation reaction via streptavidin-biotin conjuga-

tion (Gonzalez-Gonzalez et al., 2012b). The molecular weight

and charge of the PEG used in the reaction are factors that

could help in achieving a better partition of the antibodies to

the desired phase.

Sousa and coworkers implemented an immunoaffinity

ATPS strategy to recover CD34þ from whole umbilical cord

blood (Sousa et al., 2011). Traditional 5.6% PEG 8000–7.5%

dextran 500 000 ATPS was added with a pretreated sample

with the monoclonal antibody produced against the CD34

antigen. It was reported an enrichment of CD34þ cells at the

interface, reaching purification factors up to 245 with a

recovery yield of 95%. The addition of PEGylated antibodies

to the polymer-polymer ATPS has not been extensively

addressed. Hence, more investigation should be conducted

to exploit this immunoaffinity ATPS for the purification of

stem cells. The potential of phase recycling to reduce the

operational costs, especially for a scale-up process, is also

interesting.

Antibody immobilization

The last proposed strategy involved the immobilization of

antibodies on a solid matrix. It is anticipated that the cells of

interest will be coupled to the immobilized matrix. This

strategy considers the use of ficoll-dextran ATPS added with

microbeads containing anti-CD133 (Figure 3A). The immo-

bilized micro-beads have the advantage of possessing a

greater surface area for selective cell binding. In this type of

ATPS, both the product of interest and contaminants partition

to the ficoll rich top phase. However, it is expected that the

CD133þ stem cells would bind the immobilized antibody on

the microbeads. As a result, the product of interest would be

recovered from the bottom phase. Further removing of the

cell from the separating agent via trypsinization, can be

implemented, to obtain a product suitable for further purifi-

cation. Alternatively, a nontoxic and biodegradable matrix (as

in the case of MACS technology) can be used with the final

aim of eliminating the need of removing the cells after the

separation process. In comparison to the MACS technology,

Figure 2. Schematic representation of the second proposed immunoaffinity ATPS: antibody addition. (A) Free antibody strategy and (B) PEGylatedantibody approach.

6 M. Gonzalez-Gonzalez and M. Rito-Palomares Crit Rev Biotechnol, Early Online: 1–10

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

this proposed protocol does not require the usage of magnetic

particles. The main limitation of this strategy is the need of an

immobilization step, which consumes time and reagents.

Another approach for this strategy is to immobilize the

antibody of interest on the wall of the tubes that will be in

touch with the clean bottom phase (Figure 3B). In this way,

the cells of interest will be in contact with the immobilized

antibodies during the mixing step and will be retained on the

tube. A mild detaching step will be necessary to recover the

product of interest. Other creative ways could be developed to

introduce the solid phase into the two polymer phases and

exploit the already mentioned advantages of ATPS.

This proposed technology fuses the benefits of several

existing purification technologies, including ATPS, MACS

and panning, but should be further investigated to fully

develop its potential. In this context, the herein proposed

strategies have the objective to serve as an inspirational

strategy to unlock other possible isolation mechanisms that

may gather the advantages of existing methods and comple-

ment them with novel approaches.

In an attempt to increase the recovery and purity of the

target cells, counter current distribution (CCD, a multiple-step

extraction procedure) could be implemented. This technology

enhances the high selectivity of the affinity step and the

aforementioned advantages of ATPS. Briefly, immunoaffinity

ATPS-CCD implies the use of the immunoaffinity rich top

phase of the selected system and transferring it to a fresh

bottom phase. Likewise, the bottom phase of the original

ATPS is mixed with fresh immunoaffinity-rich top phase

(Figure 4). This approach can be repeated consecutively.

Hence, a number of immunoaffinity-rich top phases are

sequentially moved over a set of fresh bottom phases, and vice

versa. The required time and effort involved in this strategy

needs to be analyzed.

As general considerations for all the proposed strategies

(Figure 5), special attention must be given to the operational

conditions to preserve cell viability and function. Thus, after

the estimation of the recovery yield and purification factor

obtained from each of the isolation procedure proposed, the

purified stem cells must be cultured to monitor their viability,

differentiation and propagation capacities.

Conclusions

Today, stem cell researchers are focused on the discovery of

interesting functional phenotypes or are directing their efforts

toward the application of stem cells to try to cure several

diseases. In this sense, stem cells have the potential to

revolutionize tissue regeneration and cell-based treatments by

providing a therapy for incurable diseases in the near future.

However, it is important to realize that there will be a need to

develop novel isolation protocols. In the coming years, stem

cell purification, to some degree now neglected, will play a

crucial role once effective cell-based clinical protocols have

been tested and approved. Hence, it is important for stem cells

to be efficiently and accurately isolated from their original

matrix. Currently, there are numerous challenges regarding

the purification and isolation of stem cells that must be

addressed before therapeutic stem cell transplantations can be

widely applied. Moreover, it is well known that a key problem

for the recovery of stem cells is the high cost and scale-up

limitations of the existing methods.

Figure 3. Schematic representation of the third proposed immunoaffinity ATPS: antibody immobilization. (A) Immobilized micro-beads and(B) immobilized bottom phase walls.

DOI: 10.3109/07388551.2013.794125 Aqueous two-phase systems strategies for stem cells recovery 7

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

Even though ATPS have been mainly used for the recovery

and purification of proteins, immunoaffinity ATPS represent

a promising and suitable option to develop a selective

purification system capable of processing large quantities of

cell mixtures. ATPS are able to isolate a specific target stem

cell population without the requirement of specialized and

expensive instruments or of highly trained personnel. This

article proposes potential ATPS bioengineering strategies that

can be effectively followed in order to obtain the desired

purity and recovery required for further studies. Thus, these

Figure 4. Scheme of the immunoaffinity ATPS counter current distribution (CCD) process.

Figure 5. Summary of the proposed immunoaffinity ATPS bioengineering strategies.

8 M. Gonzalez-Gonzalez and M. Rito-Palomares Crit Rev Biotechnol, Early Online: 1–10

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

strategies may be used as a starting point for the development

of novel and more ambitious stem cell purification processes.

Additionally, the aim of this work is to present immunoaffi-

nity ATPS as a relatively inexpensive approach compared to

currently existing affinity-based purification technologies.

In this sense, immunoaffinity ATPS represent a viable

technique that can meet the future necessities, thus promoting

the acceleration of the widespread application of stem cells

therapy.

Declaration of interest

The authors report no declarations of interest and wish to

acknowledge the financial support of Tecnologico

de Monterrey, Bioprocess research chair (Grant CAT161),

of the Zambrano-Hellion Foundation and of the CONACyT

for the fellowship of M. Gonzalez-Gonzalez No. 223963.

References

Albertsson PA. (1958). Partition of proteins in liquid polymer-polymertwo-phase systems. Nature, 182, 709–11.

Albertsson PA. (1974). Countercurrent distribution of cells and cellorganelles. In: Fleisher S, Packer L, eds. Methods in Enzymology.Vow. 31. San Diego: Academic Press, 761–9.

Albertsson PA. (1986). Partition of cell particles and macromolecules.New York: Wiley.

Albertsson PA. (1988). Separation of cell organelles and membranevesicles by phase partition. Prog Clin Biol Res, 270, 227–35.

Albertsson PA, Cajarville A, Brooks DE, Tjerneld F. (1987). Partitionof proteins in aqueous polymer two-phase systems and the effect ofmolecular weight of the polymer. BBA-Gen Subjects, 926, 87–93.

Azevedo AM, Rosa PAJ, Ferreira IF, et al. (2009). Affinity-enhancedpurification of human antibodies by aqueous two-phase extraction.Sep Purif Technol, 65, 31–9.

Benavides J, Rito-Palomares M. (2008). Practical experiences from thedevelopment of aqueous two-phase processes for the recovery of highvalue biological products. J Chem Technol Biotechnol, 83, 133–42.

Benavides J, Rito-Palomares M, Asenjo JA. (2011). Downstreamprocessing and product recovery j Aqueous two-phase systems.In: Murray MY, ed. Comprehensive Biotechnology. 2nd ed., Vol. 2.Burlington: Elsevier, 697–713.

Burt RK, Testori A, Oyama Y, et al. (2010). Autologous peripheral bloodCD133þ cell implantation for limb salvage in patients with criticallimb ischemia. Bone Marrow Transpl, 45, 111–6.

Cabral JMS. (2007). Cell partitioning in aqueous two-phase polymersystems. Adv Biochem Eng Biotechnol, 106, 151–71.

Cardoso AA, Watt SM, Batard P, et al. (1995). An improved panningtechnique for the selection of CD34(þ) human bone-marrowhematopoietic-cells with high recovery of early progenitors.Exp Hematol, 23, 407–12.

Chapman AP. (2002). PEGylated antibodies and antibody fragments forimproved therapy: a review. Adv Drug Deliver Rev, 54, 531–45.

Delgado C, Anderson RJ, Francis GE, Fisher D. (1991). Separation ofcell mixtures by immunoaffinity cell partitioning: strategies for lowabundance cells. Anal Biochem, 192, 322–8.

Delgado C, Sancho P, Medieta J, Luque J. (1992). Ligand-receptorinteractions in affinity cell partitioning: studies with transferrincovalently linked to monomethoxypoly(ethylene glycol) and ratreticulocytes. J Chromatogr A, 594, 97–103.

Gonzalez-Gonzalez M, Vazquez-Villegas P, Garcıa-Salinas C, Rito-Palomares M. (2012a). Current strategies and challenges for thepurification of stem cells. J Chem Technol Biot, 87, 2–10.

Gonzalez-Gonzalez M, Mayolo-Deloisa K, Rito-Palomares M. (2012b).PEGylation, detection and chromatographic purification of site-specific PEGylated CD133-Biotin antibody in route to stem cellseparation. J Chromatogr B, 893–4, 182–6.

Gossett DR, Weaver WM, Mach AJ, et al. (2010). Label-free cellseparation and sorting in microfluidic systems. Anal Bioanal Chem,397, 3249–67.

Hatti-Kaul R. (2000). Aqueous two-phase systems: methods andprotocols. New Jersey: Humana Press.

Hatti-Kaul R. (2001). Aqueous two-phase systems - a general overview.Mol Biotechnol, 19, 269–77.

Isidori A, Motta MR, Tani M, et al. (2007). Positive selection andtransplantation of autologous highly purified CD133þ stem cells inresistant/relapsed chronic lymphocytic leukemia patients results inrapid hematopoietic reconstitution without an adequate leukemic cellpurging. Biol Blood Marrow Tr, 13, 1224–32.

Jing Y, Moore LR, Schneider T, et al. (2007a). Negative selectionof hematopoietic progenitor cells by continuous magnetophoresis.Exp Hematol, 35, 662–72.

Jing Y, Moore LR, Williams PS, et al. (2007b). Blood progenitor cellseparation from clinical leukapheresis product by magnetic nanopar-ticle binding and magnetophoresis. Biotechnol Bioeng, 96, 1139–54.

Johansson G. (1984). Affinity partitioning. In: Jakoby WB, ed. Methodsin Enzymology. Vol. 104. San Diego: Academic Press, 356–64.

Johansson G. (1985). Aqueous two-phase systems in protein purification.J Biotechnol, 3, 11–8.

Kamihira M, Kumar A. (2007). Development of separation technique forstem cells. Adv Biochem Eng Biotechnol, 106, 173–93.

Karr LJ, Van Alstine JM, Snyder RS, et al. (1988). Cell separation byimmunoaffinity partitioning with polyethylene glycol-modified pro-tein A in aqueous polymer two-phase systems. J Chromatogr A, 442,219–27.

Kopperschlager G, Birkenmeier G. (1990). Affinity partitioning andextraction of proteins. Bioseparation, 1, 235–54.

Kumar A, Bhardwaj A. (2008). Methods in cell separation forbiomedical application: cryogels as a new tool. Biomed Mater, 3,1–11.

Kumar A, Kamihira M, Galaev IY, et al. (2001). Type-specificseparation of animal cells in aqueous two-phase systems usingantibody conjugates with temperature-sensitive polymers. BiotechnolBioeng, 75, 570–80.

Kumar A, Srivastava A, Galaev IY, Mattiasson B. (2007). Smartpolymers: physical forms and bioengineering applications. ProgPolym Sci, 32, 1205–37.

Lang P, Bader P, Schumm M, et al. (2004). Transplantation of acombination of CD133(þ) and CD34(þ) selected progenitor cellsfrom alternative donors. Brit J Haematol,, 124, 72–9.

Lebkowski JS, Schain LR, Okrongly D, et al. (1992). Rapid isolation ofhuman CD34 hematopoietic stem cells-purging of human tumor cells.Transplantation, 53, 1011–9.

Liu Y, Yu YL, Chen MZ, Xiao X. (2011). Advances in aqueous two-phase systems and applications in protein separation and purification.Can J Chem Eng Technol, 2, 1–7.

Malmstrom P, Nelson K, Jonsson A, et al. (1978). Separation of ratleukocytes by countercurrent distribution in aqueous two phasesystems. I. Characterization of subpopulations of cells. Cell Immunol,37, 409–21.

Martinez HR, Gonzalez-Garza MT, Moreno-Cuevas JE, et al. (2009).Stem-cell transplantation into the frontal motor cortex in amyotrophiclateral sclerosis patients. Cytotherapy, 11, 26–34.

Miraglia S, Godfrey W, Yin AH, et al. (1997). A novel five-transmembrane hematopoietic stem cell antigen: isolation, character-ization, and molecular cloning. Blood, 90, 5013–21.

Morre DJ, Morre DM, Van Alstine JM. (1998). Separation of endosomesby aqueous two-phase partition and free-flow electrophoresis.J Chromatogr B, 711, 203–15.

Morre DM, Morre DJ. (2000). Aqueous two-phase partition applied tothe isolation of plasma membranes and Golgi apparatus from culturedmammalian cells. J Chromatogr B, 743, 377–87.

Pethig R, Menachery A, Pells S, De Sousa P. (2010). Dielectrophoresis: areview of applications for stem cell research. J Biomed Biotechnol,2010, 1–7.

Ruiz-Ruiz F, Benavides J, Aguilar O, Rito-Palomares M. (2012).Aqueous two-phase affinity partitioning systems: current applicationsand trends. J Chromatogr A, 1244, 1–13.

Schriebl K, Lim S, Choo A, et al. (2010). Stem cell separation: abottleneck in stem cell therapy. Biotechnol J, 5, 50–61.

Sinha J, Dey PK, Panda T. (2000). Aqueous two-phase: the system ofchoice for extractive fermentation. Appl Microbiol Biot, 54, 476–86.

SooHoo JR, Walker GM. (2009). Microfluidic aqueous two phase systemfor leukocyte concentration from whole blood. Biomed Microdevices,11, 323–9.

Sousa AF, Andrade PZ, Pirzgalska RM, et al. (2011). A novel method forhuman hematopoietic stem/progenitor cell isolation from umbilical

DOI: 10.3109/07388551.2013.794125 Aqueous two-phase systems strategies for stem cells recovery 9

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.

cord blood based on immunoaffinity aqueous two-phase partitioning.Biotechnol Lett, 33, 2373–7.

Stamm C, Kleine H-D, Choi Y-H, et al. (2007). Intramyocardial deliveryof CD133þ bone marrow cells and coronary artery bypass grafting forchronic ischemic heart disease: safety and efficacy studies. J ThoracCardiov Sur, 133, 717–25.

Tsukamoto M, Taira S, Yamamura S, et al. (2009). Cell separation by anaqueous two-phase system in a microfluidic device. Analyst, 134,1994–8.

Walter H, Brooks DE, Fisher D. (1985). Partitioning in aqueous two-phase systems: theory, methods, uses, and applications to biotechnol-ogy. Orlando: Academic Press.

Walter H, Krob EJ, Ascher GS. (1969a). Separation of lymphocytesand polymorphonuclear leukocytes by countercurrent distribution inaqueous two-polymer phase systems. Exp Cell Res, 55, 279–83.

Walter H, Johansson G, eds. (1994). Aqueous two-phase systems.Methods in enzymology. Vol. 228. San Diego: Academic Press, 3–725.

Walter H, Krob EJ, Garza R. (1968). Factors in the partition of red bloodcells in aqueous dextran-polyethylene glycol two-phase systems.BBA-Gen Subjects, 165, 507–14.

Walter H, Krob EJ, Garza R, Ascher GS. (1969b). Partition andcountercurrent distribution of erythrocytes and leukocytes fromdifferent species. Exp Cell Res, 55, 57–64.

Wognum AW, Eaves AC, Thomas TE. (2003). Identification andisolation of hematopoietic stem cells. Arch Med Res, 34, 461–475.

Wu Y, Wu PY. (2009). CD133 as a marker for cancer stem cells:progresses and concerns. Stem Cells Dev, 18, 1127–34.

Zaslavsky BY. (1995). Aqueous two-phase partitioning – physicalchemistry and bioanalytical applications. New York: MarcelDekker, Inc.

10 M. Gonzalez-Gonzalez and M. Rito-Palomares Crit Rev Biotechnol, Early Online: 1–10

Cri

tical

Rev

iew

s in

Bio

tech

nolo

gy D

ownl

oade

d fr

om in

form

ahea

lthca

re.c

om b

y 20

1.10

0.25

.11

on 0

5/21

/13

For

pers

onal

use

onl

y.