review of shear flow affecting proteins
-
Upload
aditya-raghunandan -
Category
Documents
-
view
16 -
download
1
description
Transcript of review of shear flow affecting proteins
-
ReviewThe Effects of Shear Flow on Protein Structure and Function
Innocent B. Bekard,1 Peter Asimakis,1 Joseph Bertolini,2 Dave E. Dunstan11 Department of Chemical and Biomolecular Engineering, University of Melbourne, Parkville, VIC 3010, Australia
2 Research and Development Department, CSL Biotherapies, 189-209 Camp Rd, Broadmeadows, VIC 3047, Australia
Received 14 February 2011; revised 20 April 2011; accepted 26 April 2011
Published online 4 May 2011 in Wiley Online Library (wileyonlinelibrary.com). DOI 10.1002/bip.21646
This article was originally published online as an accepted
preprint. The Published Online date corresponds to the
preprint version. You can request a copy of the preprint by
emailing the Biopolymers editorial office at biopolymers@wiley.
com
INTRODUCTION
Proteins are linear polymer chains of combinations of
the 20 amino acid residues. These complex macro-
molecules form an essential part of an array of bio-
logical processes in living systems, such as structural
components of cells, biological catalysts (enzymes),
and chemical messengers (hormones). The functional prop-
erties of proteins depend on their unique three-dimensional
structure which is determined primarily by the amino acid
sequence of individual chains. The energy threshold between
the native and denatured state of a protein is low, thus the
physicochemical environment is a critical determinant of
protein structure and function.1 Perturbation of the native
protein conformation results in loss of catalytic activity or
biological function,2,3 and in many cases aggregation and
amyloid bril formation.46
Structural perturbation of protein molecules occurs as a
result of conditions of temperature, pH, and ionic strength
as well as through the presence of denaturants (e.g., urea,
guanidine), organic solvents, and surfactants.7 In addition,
structural destabilization can result from exposure to hydro-
dynamic shear forces810 originating from shaking, sonica-
tion, mixing, vortexing, and ow through conduits.7,11,12
The effect of uid shear stress on protein structure is a
subject of practical interest because it is a common pheno-
menon in bioprocessing.13 Proteins have been shown to
exhibit conformational dynamics in shear ow.1417 Protein
solutions are exposed to shear stresses during bioprocessing
steps as a result of centrifugation, fractionation, pumping,
and ultraltration.13,18,19 Similarly, the shipping and
handling of biotherapeutics and protein based bioprocessing
reagents such as monoclonal antibodies, hormones, cyto-
kines, and enzymes can result in signicant agitation. For
these reasons, an understanding of the effects of shear ow
on protein stability, and a means of testing and measuring
this effect, would allow the appropriate design and selection
of manufacturing processes, conditions, and formulations
which would ensure maximum yield and stability.
It has been known for some time that considerable shear
stress is generated by blood ow in the circulatory system.20
However the pathophysiological implications of this have not
been explored. Thus, this review will also examine relevant
papers in this area and highlight implications to the patho-
genesis of some diseases.
ReviewThe Effects of Shear Flow on Protein Structure and Function
Correspondence to: Dave E. Dunstan; e-mail: [email protected]
Innocent B. Bekard and Peter Asimakis contributed equally to this work.
ABSTRACT:
Protein molecules are subjected to potentially denaturing
uid shear forces during processing and in circulation in
the body. These complex molecules, involved in numerous
biological functions and reactions, can be signicantly
impaired by molecular damage. There have been many
studies on the effects of hydrodynamic shear forces on
protein structure and function. These studies are
reviewed and the implications to bioprocessing and
pathophysiology of certain diseases are discussed. # 2011
Wiley Periodicals, Inc. Biopolymers 95: 733745, 2011.
Keywords: shear ow; protein; unfolding; aggregation;
amyloid bril; physiology; bioprocessing
VVC 2011 Wiley Periodicals, Inc.
Biopolymers Volume 95 / Number 11 733
p4notewifiHighlight
p4notewifiHighlight
-
Studying the Effect of Shear Flow on ProteinsExtensional Flow vs. Simple Shear Flow. The common ow
elds applied in shear studies are extensional ow and simple
shear ow. A homogeneous extensional ow, also called
elongational ow or stretching ow, is characterized by a lin-
ear velocity gradient of the form vy _cy along the directionof ow (Figure 1).21 The strain rate, _c @xy@y , is constant. Anexample is the ow of a polymer solution through a con-
verging channel with hyperbolically-shaped walls. This
should not be confused with well developed ow of an
incompressible uid through a circular pipe of innite
length, which is characterized by inhomogeneous shear.
Here, the ow pattern is of the Poiseulle type, showing a
parabolic velocity prole where both the shear rate and
uid velocity varies as a function of the distance from the
vessel boundary (Figure 1). The strain rate is given as
_c 2y0a where y0 is the distance between the center of thepolymer and the ow axis and a is a measure of the curvatureof the ow prole.22
Simple shear ow on the other hand describes uid ow
characterized by a velocity gradient perpendicular to the ow
eld (Figure 1). It is modeled as a linear superposition of
rotational ow with vorticity x, and elongational ow with
strain rate _c @vx@y .16 In the rotational component of the oweld, protein molecules experience whole body rotation
with no hydrodynamic shear strain, hence maintain their
structural integrity. However, protein molecules are sub-
jected to stretching events when oriented in the extensional
ow eld. The hydrodynamic shear stress resulting from
these events is thought to destabilize the native protein
structure, leading to aggregate formation.17 For Newtonian
uids, the mathematical relationship between shear stress
(s) and velocity gradient ( _c) in a given ow eld is expressedas s g _c.23 A tangential stress of this type is called shearing,where innitesimally thin layers of uid slide over each other
in laminar ow. Shear stress has units of force per unit area
(N/m2), and is a measure of the actual hydrodynamic drag
forces acting on the protein solution under ow. The velocity
gradient, also referred to as the shear rate, has units of inverse
time (s21).
It is noteworthy that the magnitudes of rotational and
elongational components of simple shear ow are equal (|x|5 | _c|). This implies that the conformational dynamics ofprotein molecules in the ow eld are dictated by the ran-
dom occurrence of both events. In practice, the rotational
and elongational components of ow differ in magnitude.
FIGURE 1 Schematics of the common velocity proles in ow. (A) Homogeneous extensional
ow typically associated with cross-slot geometries. The shear rate is constant. (B) Well developed
ow in a conduit. The velocity prole is parabolic, typical of Poiseuille ow. In addition, the uid
velocity is maximal at the center of the tube, approaching zero at the boundaries. The converse is
true for the uid shear rate. (C) Simple shear ow, showing a velocity gradient perpendicular to
the direction of ow. In all cases (AC), the arrows show both the direction of ow as well as the
velocity prole.
734 Bekard et al.
Biopolymers
-
Devices for Generating Shear Flow
In many protein studies, shear ow is generated by subjecting
protein solutions to ow patterns characterized by uniform or
heterogeneous velocity gradients.18 Shear devices that create a
near uniform velocity gradient through protein solutions pro-
vide a well controlled and quantiable shear stress. Hence,
such devices are ideal for studying the effects of shear forces on
protein molecules. Conversely, heterogeneous velocity gra-
dients, for example, resulting from stirring or shaking, provide
poorly controlled shear conditions that are difcult to quantify.
It is worth noting that the differences in experimental devices
applied in shear studies, and the associated data interpretation,
could be a major contributory factor to the inconsistent exper-
imental results reported throughout the literature.
Several studies that show the effect of shear ow on a number
of proteins, along with the shear devices employed, are summar-
ized in Table I. By virtue of the differences in experimental design,
the shear (strain history) as well as the shear stress values, which
are not given here, varies signicantly among the different experi-
ments. The experimental ow devices used for protein studies
fall into two main categories: capillary and rotational devices.
Capillary/Microuidic Flow Devices
Capillary ow is where a uid is forced through a conduit of
known dimensions, by applying a given pressure difference
between the inlet and outlet of the conduit.43 Here, the uid
velocity prole is of the Poiseuille type (non-homogeneous
shear ow) with the maximum shear rate at the uid-vessel
boundary, reducing gradually towards the vessel center
(Figure 1B). Very high shear rates, up to 105 s21, can be
achieved but over short residence times on the order of
milliseconds.41,44 A schematic of a typical capillary ow tube
is shown in Figure 2. It has been reported that the short resi-
dence time spent in the ow eld could contribute to
incomplete protein stretching (unfolding).45 However, recir-
culation of protein solutions through conduits have been
successfully applied to increase residence times,32 offering a
good model system for uid shear stress in ultraltration
units and membranes.
Rotational Flow Devices
Cone and plate, parallel plate and concentric cylinder visc-
ometers are three types of rotational ow devices commonly
Table I Studies of the Shear-Stability of Protein Systems Using a Variety of Shear Devices
Device Geometry Protein Shear Rate/Rotational Speed Result References
Couette Insulin 200 s21 Unfolding and aggregation 14
Poly-L-lysine [333 s21 Unfolding 24b-lactoglobulin 25 s21, 150 s21 Fibril formation 25, 26von Willebrand factor \3.0 3 103 s21 Unfolding 27Amyloid-b 50 s21 Fibril formation 28
Taylor-Couette Lysozyme 750 rpm,[14 s21 Unfolding 29, 30Cytochrome-c 750 rpm No change 29
Cone and plate a-amylase 120 s21 Loss of activity 31Fibrinogen 290 s21 Degradation 32
Catalase 91.5 s21 Loss of activity 33
Rennet 9.15 s21 Loss of activity 33
Glycoprotein Ib and IIb-IIIa 8.23 103 s21 Unfolding 34von Willebrand factor 6.7 3 103 s21 Aggregation 35
Concentric cylinder Urease 683 s21 Particle formation 36
Catalase 683 s21 Particle formation 36
Alcohol dehydrogenase 683 s21 Particle formation 37
Deoxyribonuclease 1.5 3 103 rpm No change 38Growth hormone 1.5 3 103 rpm Unfolding and fragmentation 38Urease 48 s21 Loss of activity 39
Capillary Catalase 67 s21 Loss of activity 40
Catalase 4.6 3 104 s21 Minor loss of activity 36Cytochrome-c 2.0 3 105 s21 No change 41
Microuidic cell von Willebrand factor [13 103 s21 Unfolding 42
FIGURE 2 Schematic of a simple extrusion glass capillary vis-
cometer. The arrows show the direction of ow.
Effects of Shear Flow on Protein Structure and Function 735
Biopolymers
-
used to impart shear stress on protein systems across a nar-
row gap (Figure 3). All models consist of two parts where
one rotates with the other being stationary. In the case of the
concentric cylinder, also known as Couette or coaxial cylin-
der ow-cell, there are several sorts that differ in basic design
but operate on the same principles.46 However, a through-
cell Couette arrangement is ideal for generating a simple
shear ow, as the design minimizes any end effects.47 This
type of device also curtails particle settling or migration away
from the solid boundaries, thereby limiting variations of
uid properties across the gap.48 In addition, a nominal
shear rate can be calculated for each rotational speed. At high
rotational speeds, large deviations from the ideal ow may
occur due to the formation of vortices. It is recognized that
vortices occur in extensional ow regions in uids, and
should therefore be avoided if a simple shear ow is
desired.49 The main advantage of rotational shear devices
over that of the capillary design is that the entire test solution
is sheared at a near constant rate. This permits the study of
any time-dependent behavior of protein samples over an
extended period of time. In the through-cell Couette
arrangement, the shear rate can be regarded as constant only
if the gap width is much less than the radius of the inner cyl-
inder.50 In the cone-and-plate design, the solution is con-
tained in the space between a cone of large apex angle and a
plate with a at surface normal to the axis. For small angles
between the cone and plate, the shear rate is considered con-
stant for all radial positions.
The Effects of Shear Flow on Protein SolutionsProtein Function. Preliminary studies on the relationship
between shear ow and protein structure exploited the cata-
lytic activity of enzyme solutions as a means of measuring
protein integrity. Thus, a decrease in enzyme activity implied
a structural deformation of the native enzyme molecules.
These early studies were critical in dening the appropriate,
and operation of, devices to allow the study of the behavior
of proteins in shear ow, allowing the estimation of shear
forces required to perturb protein function with insight into
possible resulting structural changes.
Studies on catalase, rennet, and carboxypeptidase solu-
tions sheared in a narrow gap coaxial viscometer40 at shear
rates between 9.15 and 1155 s21 for 90 min, showed a strong
correlation between decrease in enzyme activity and shear
(shear rate 3 time). A loss of enzyme activity occurred for
shear greater than 104 although the rennet solutions partially
regained activity upon the cessation of shearing. The
observed enzyme inactivation was attributed to the breaking
of the molecules tertiary structure when oriented appropri-
ately in the shear eld. The authors discounted any signi-
cant contribution from the airliquid interface in the
viscometer, where protein molecules, by virtue of their
amphipathic nature, may aggregate (causing inactivity). It is
also possible that the loss in enzyme activity was due to a
ow-induced limited residence time for enzyme-substrate
interaction. A similar shear-effect was observed upon expo-
sure of catalase and rennet solutions to shear rates in the
region of 104 s21 in model ultraltration systems.33 Whereas
the catalase solutions lost some activity during ultraltration,
the rennet solutions did not suffer inactivation in the circula-
tion lter systems. Further studies on plasma brinogen,
sheared in a Weissenberg rheogoniometer (shear rates 290
1155 s21) with a Couette attachment, revealed a tempera-
ture-independent loss in its clottability.32
Studies on the shear-stability of urease, using a coaxial cyl-
inder viscometer, which allowed direct monitoring of urease
catalyzed hydrolysis of urea during shear exposure, showed
continuous decrease in the rate of urease activity with
increasing shear rate (48, 288, 741, and 1717 s21).39 The par-
tial deactivation of urease revealed both reversible and irre-
versible elements. The reversible inactivation was ascribed to
hydrodynamic distortion of the enzymes structure in ow,
whereas permanent inactivation was attributed to the break-
ing of the enzymes tertiary structure. The permanent loss in
urease activity correlated with shear strain, with a critical
shear value of 105, similar to that previously reported.40 A
comparison of catalase degradation in streamline and turbu-
lent ow regimes, upon mixing in a cylindrical container,
showed a signicant inactivation in the latter where a vortex
and air bubbles had formed in the solution.51 This suggested
that the airliquid interface may have contributed signi-
cantly to catalase degradation. It was also shown that shear
stress in selected microltration membranes caused a signi-
cant decrease in the catalytic activity of yeast alcohol dehy-
drogenase (ADH), under solution conditions where the
FIGURE 3 Schematics of the common rotational ow devices:
(A) concentric cylinder, (B) cone and plate, and (C) parallel plate
rheometers.
736 Bekard et al.
Biopolymers
-
enzyme was slightly unstable.52 This observation was attrib-
uted to membrane-enzyme interactions resulting from a
shear-induced deformation of the enzyme structure.
In studies of the shear-stability of ADH solutions using a
high shear concentric viscometer, a rotating disk reactor and
several pumps, it was found that fully active tetrameric mole-
cules of ADH showed negligible change in activity even for
strain rates as high as 26, 000 s21 over 1 h in the high shear
device.53 Turbulent regimes in the rotating-disk reactor
(3600 rpm for 5 h) and up to about 1500 passes in the
various pumps likewise had little effect on ADH activity.
However, the introduction of a gas-liquid interface in the
rotating-disk reactor resulted in a 40% decrease in the initial
ADH activity after 5 h. Similarly, a signicant decrease in
ADH activity was observed in both a gear and a Jabsco pump
after 2000 passes.53 This report suggested that interfacial
denaturation, and not shear per se, accounts for the defor-
mation of proteins in solutions exposed to shear ow, and
that the native conformation of globular proteins, when in a
chemically stable environment, are stable in shear ows usu-
ally encountered in practice.
The importance of an airliquid interface in promoting
shear-induced protein denaturation was shown in a study
with progesterone 11a-hydroxylase complex, using anopen concentric cylinder viscometer and a horizontal vis-
cometer closed at both ends.54 It was observed that the
gas-liquid interface, in concert with high shear regimes,
which replenished the protein at the interface, promoted
rapid protein denaturation as previously reported.53 In
addition, a wall surface effect on the enzyme complex was
observed as the gap width of the viscometer was reduced
from 0.475 to 0.15 mm. Furthermore, it was observed
that viscous enzyme solutions showed a marked decrease
in activity as a function of shear stress.54 These observa-
tions lead the authors to propose that the applied shear
stress resulted in enzyme denaturation via either the rup-
ture of the enzyme membrane or the enhanced solubiliza-
tion of component(s) of the enzyme complex by the ve-
locity gradient in the agitated solution.
The above studies clearly showed that shear could have a
profound effect on the activity of enzymes, and by inference
on protein structure. The shear-effect was more pronounced
in the presence of an airliquid interface. A key limitation of
the above studies was that any deduction of structural change
was based on indirect evidence derived from enzyme activity.
Indeed, whereas shear may not have caused signicant struc-
tural damage, a decrease in enzyme activity could result from
minor modications to an enzymes active site. In many of
the experiments, the enzymes were subjected to intermittent
shearing force to allow sampling. Therefore, signicant time
would have elapsed between sampling of solutions and test-
ing for enzyme activity. This would have allowed reversible
structural changes to revert and thus go undetected. The
advent of new experimental techniques, allowing real-time
measurements of the solution conformation of proteins, is
providing new insight into the shear-stability of proteins
with respect to variations in the sensitivity of different pro-
teins to shear, and the specic molecular changes occurring
in response to shear exposure.14,55
Protein Structure
Human von Willebrand Factor (vWF), a blood plasma pro-
tein with important functions in coagulation, was amongst
the rst of protein systems, besides enzymes, to be studied
for shear induced structural changes. vWF molecules, which
are initially secreted by the endothelial cells as large, hyper-
active multimers, with relative molecular mass up to 50 3106, circulate as a series of smaller, less active proteolytic frag-
ments in the plasma as a result of the action of the metallo-
protease ADAMTS-13.56,57 Interestingly, the proteolysis of
large vWF multimers is not observed when normal plasma is
incubated in vitro.58 This lead to the conclusion that the gen-
eration of proteolytic fragments of vWF in circulation
depends on haemodynamic shear stress.57 The size distribu-
tion of vWF multimers in microcirculation is critical to its
haemostatic potential.
Tsai et al. investigated this theory by perfusing normal
plasma through long capillary tubes (190 or 354 cm in
length), at shear rates between 1508 and 4761 s21, followed
by an examination of the size distribution of vWF using a
combination of SDS agarose gel electrophoresis and densito-
metric scanning analysis of autoradiographs.59 Relative to
unsheared plasma, an increase in smaller vWF multimers was
observed in the sheared samples at the expense of the larger
multimers, especially in high shear regimes. These observa-
tions lead to the conclusion that shear stress might be
involved in the modulation of the size distribution of vWF in
circulation by enhancing the proteolytic cleavage of large
vWF multimers.59
In a subsequent study by Siedlecki et al., using a combina-
tion of atomic force microscopy and a rotating disk system,
vWF molecules were observed (visually) to undergo a shear-
induced conformational transition from a globular state to
an extended chain conformation at a critical shear stress
value[31.5 dyn/cm2 ( _c 4618.8 s21).60 The result was theexposure of intra-molecular domains of vWF. It was sug-
gested that shear-induced structural changes in vWF may
have an important role in platelet adhesion and thrombus
formation in regions of high shear stress, as would develop at
the site of a bleeding injury.60
Effects of Shear Flow on Protein Structure and Function 737
Biopolymers
p4notewifiImage
p4notewifiHighlight
p4notewifiHighlight
p4notewifiLine
-
To this point, it had been considered that clot formation
was initiated through direct shear activation of platelets.58
This was substantiated in a later study,61 which investigated
the mechanics involved in the formation of reversible tether
bonds between the platelet glycoprotein receptor Iba and theA1 domain of surface-immobilized vWF under hydro-
dynamic shear ow. Puried platelets were perfused over
plasma vWF-A1 coated surfaces in a parallel-plate ow
chamber at shear stresses between 0.2 and 8 dyn/cm2. Platelet
tethering was visualized using a Nikon microscope equipped
with a high speed video camera, and the motion of the teth-
ered platelets calculated using an analytical two-dimensional
model. The results showed that hydrodynamic compressive
forces inuence tether bond formation between platelets and
vWF.61
Recently, uorescence microscopy has been used to
directly visualize individual uorescently labeled vWF multi-
mers under hydrodynamic stress in a microuidic device.42
vWF was uorescently labeled with Alexa uor 488, which
was attached to the primary amines of the glycoprotein using
tetrauorophenyl ester. It was found that shear rates greater
than 1000 s21 triggered a reversible stretching of vWF in so-
lution. Furthermore, real-time measurements of the confor-
mational dynamics of vWF in response to laminar shear ow
in a Couette ow-cell, using a combination of small angle
neutron scattering (SANS) spectroscopy and quantitative
modeling, showed an irreversible conformational change in
vWF, under hydrodynamic shear stress, at shear rates 3000s21.27 The observed conformational change was found to
involve the exposure of hydrophobic domains at shear rates
[2300 s21, as indicated by an increase in the binding afnityof the hydrophobic dye 1,10-bis(anilino)-4-,40-bis(naphta-
lene)-8,80-disulfonate (bis-ANS).27 The shear-effect was
more pronounced with increasing shear rate.
A more recent single-molecule investigation of the shear-
stability of vWF has provided more insight into the relevance
of shear stress in the homeostatic regulation of the size of cir-
culating vWF multimers as well as the potentiation of vWF-
mediated platelet aggregation.62 Specically, the study exam-
ined the folded and unfolded states of a single A2 domain of
vWF, which contains the site of cleavage for ADAMST-13, in
the presence and absence of the metalloprotease. The A2
domain of vWF was unfolded by directly applying force with
laser tweezers. The results showed that only the unfolded A2
domain is cleaved by ADAMST-13.62 These observations cor-
roborated previous studies which found that shear-induced
stretching of large vWF multimers results in the exposure of
the scissile Tyr1605-Met1606 bond within the A2 domain, faci-
litating cleavage by ADAMST-13 in normal plasma.56,57
Smaller vWF multimers in microcirculation equally undergo
stretching in regions of high shear, such as a bleeding arte-
riole, which expose bonding sites in the A1 domain of vWF
for complexation with platelets during haemostasis.57,60,63
While studies of vWF provided clear evidence that shear
ow can alter protein structure, it may be argued that differ-
ent proteins experience different shear since the strain rates
required to trigger structural alterations decreases with
increasing molecular weight and solvent viscosity. For exam-
ple, studies on the effect of high shear rates on ferric equine
cytochrome c, a small globular protein of molecular weight
12,384 Da, showed no signicant structural alterations when
exposed to shear rates as high as 105 s21 in a capillary ow
device.41 By applying a simple model, the authors suggested
that a shear rate of 107 s21 would be required to denaturea small globular protein in water.41 However, the transient
residence time associated with capillary ow devices may
explain the hysteresis observed in such systems.45 More
importantly, the results41 contradict the observed abrupt
stretching of vWF ([20,000 kDa) in a microuidic device ata threshold shear rate of 103 s21.42 Clearly, the larger, more
complex vWF would be expected to be more susceptible to
shear stress relative to cytochrome c. However, it is notew-
orthy that specic conformational characteristics such as
a-helix and b-sheet composition, and intra-molecularinteractions (e.g., hydrophobic, electrostatic) and covalent
bonds (e.g., disulde), would be an important determinant
of protein stability.
Thus, protein systems with comparable molecular weights
may differ in their shear-stability due to differences in their
solution properties. For example, previous studies on
the effects of both high shear ([107) and high shear rate([105 s21), using concentric cylinder-based systems, onrecombinant human growth hormone (rhGH) (22 kDa)and recombinant human deoxyribonuclease (rhDNase)
(31 kDa) showed that rhDNase was more resistant toshear-effects.38 For instance, whereas scanning microcalorim-
etry and SDS-PAGE analysis of extensively sheared solutions
showed changes in the melting temperature of rhGH and the
presence of low molecular weight fragments, respectively, no
such changes were observed for rhDNase. Interestingly, the
observed structural changes in rhGH were not detected in
both the near and the far-UV circular dichroism spectral pro-
le of the sample.38 Further studies on both samples showed
that rhGH denatured upon exposure to high shear in the
presence of an airliquid interface whereas rhDNase
remained relatively stable.64 The stability of rhDNase was
attributed to its comparatively high surface tension and low
foaming tendency in solution.
Intriguingly, it has been shown that human and bovine
albumin samples, which differ in only two amino acids,
738 Bekard et al.
Biopolymers
-
show different aggregation kinetics upon shaking at high
shear rates ([8000 rpm).65 Multi-angle laser light-scatter-ing measurements showed that in addition to the mono-
mer-dimer transition observed in both albumin samples
upon shearing, human serum albumin also formed trimers
especially at high shear rates. Since the protein concentra-
tion and solventair interfaces were considered as xed
factors, the observed differences in the degree of albumin
aggregation was attributed to the minor variation in their
primary structure.
Protein Aggregation
As has been discussed above, shear can result in protein
denaturation and compromised function. It is also well
established that denaturation of proteins can lead to aggrega-
tion.66 Hence, the use of agitation (uncontrolled shear stress)
to both induce and accelerate protein aggregation and amy-
loid bril formation is common practice throughout the lit-
erature.66 For example, under favorable solution conditions,
various forms of agitation including shaking, sonication and
stirring have been successfully applied to accelerate the aggre-
gation of insulin,6771 amyloid-b,28,72 b2-microglobulin,73,74
b-lactoglobulin,25 albumin,65 and the PDZ domain frommurine Protein Tyrosine Phosphatase Bas-like (PDZ2)75
among others. In one particular study, a range of structurally
diverse protein systems including BSA, myoglobin, lysozyme,
Tm0979, SOD and hisactophin were shown to generate amy-
loid like structures following sonication.76
Shear effects on protein aggregation have also been stud-
ied in uniform ow elds. For example, a shear-induced
nucleation, without ow enhanced aggregation, of preheated
b-lactoglobulin solutions (0.5 wt%) at low pH has beenreported.77 b-lactoglobulin solutions were exposed to Cou-ette ow in a rheometer, at a moderate shear rate of 200 s21
over 5 h, while measuring the ow-induced birefringence.
Thermal treatment of the b-lactoglobulin samples triggeredthe formation of metastable pre-brillar aggregates, without
which bril formation was absent in the sheared samples.
Shearing of b-lactoglobulin samples was done either continu-ously or in short pulses, both producing a similar degree of
bril formation. These observations lead to the conclusion
that brief mechanical perturbation of an aggregation prone
protein solution was enough to enhance bril formation.77
That is, shear ow only triggered the nucleation of bril for-
mation but did not inuence the polymerization of preaggre-
gates into mature brils, discounting orthokinetic coagula-
tion under the experimental conditions. However, the brils
formed from the continuous shear treatment showed a
smaller variance in Gaussian length distribution relative to
those from the pulse shear treatments, indicating a homoge-
nizing effect of the continuous shear treatment. Evidently, a
synergy of heat and agitation triggered rapid bril formation.
Another study showed that the aggregation of preheated
b-lactoglobulin solutions in Couette ow was shear rate de-pendent.25 In addition, if shearing was performed prior to
thermal treatment, a rapid enhancement of brillar species
still occurred, suggesting a shear-induced formation of the
precursor nuclei required for bril development as previously
reported.77 Interestingly, at shear rates[500 s21, bril degra-dation, possibly arising from the persistent stretching (exten-
sional ow) events in the ow eld, was observed. A further
study78 revealed that a sufciently high b-lactoglobulin con-centration ([3 wt%) was required to initiate bril formationwhen samples were heated and sheared simultaneously. In
addition, the amount of brils formed increased as a function
of shear rate up to 337 s21 beyond which an opposing shear
effect, similar to that reported earlier,25 was observed. The
paradoxical shear-effect was explained by a ow enhanced
polymerization of the bril nucleus in low shear regimes,
whereas in high shear regimes, the extensional component of
the ow eld overwhelmed the nascent inter-b-strand hydro-gen bonds stabilizing the aggregating brils. Furthermore, the
authors observed that the shear applied produced shorter
brils and also enhanced, below a critical bril concentration,
the viscosity of the resulting bril solutions.78
More recently, a similar ow enhanced bril formation
has been observed in aqueous solutions of bovine insulin,14
thermally treated amyloid-b28 and b-lactoglobulin.26 Theshear-stability of bovine insulin in Couette ow was probed
directly via novel circular dichroism and tyrosine autouor-
escence measurements, in situ and in real time. For a given
shear rate, helical segments of native insulin were observed to
unfold as a function of time. Atomic force microscopy
images of the sheared samples revealed the presence of bril-
lar forms in relatively strong shear regimes (600 s21).14 The
shear-effect on preheated amyloid-b samples28 exposed toCouette ow showed similar trends to that reported earlier.25
For the b-lactoglobulin studies,26 the authors compared themorphology and mechanical properties of brils formed
under heterogeneous (stirred) and uniform (Couette) ow
conditions using atomic force microscopy. They found that
b-lactoglobulin brils resulting from heterogeneous ow hadtwisted ribbon-like morphologies and higher mechanical
strength relative to the beaded brils formed in Couette ow.
Evidently, the intertwining of brils produced in the variable
shear regime imparted additional mechanical stability to the
overall bril structure. It was hypothesized that polymeriza-
tion of bril seeds occurs in the ow eld, and in the case of
stirred samples, mature brils anneal into twisted ribbons
possibly via orthokinetic coagulation. Taking together, even
Effects of Shear Flow on Protein Structure and Function 739
Biopolymers
-
if in some cases the initial structural destabilization required
for protein aggregation is not triggered by shear, its ability to
accelerate the polymerization of metastable prebrillar aggre-
gates into mature brils still has grave implications in bio-
processing and physiology.
Regarding the mechanism of shear-induced protein
aggregation, there is a general consensus that mechanical
perturbation of a protein molecule often results in a struc-
tural destabilization of the native conformation, leading to
the exposure of sequestered hydrophobic residues to the
surrounding medium. Solvent-exposed hydrophobic groups
nucleate via hydrophobic interactions and subsequently ag-
gregate. Several studies show that the initial destabilization
of the protein structure occurs at the solventair or sol-
ventsolid interface, where surface tension forces unfold
the native protein.36,37,64,79 The airwater interfacial force
is estimated to be 140 pN,80 taking the airwater interface
to be 2 nm in depth with a 0.07 N/m surface tension.81
This value is comparable to the 150 pN observed to
unfold globular proteins in atomic force microscopy stud-
ies.82 In addition, as agitation increases the turnover of
the airliquid interface, and thus the number of protein
molecules interacting with this interface, the nucleation of
solvent-exposed hydrophobic species via hydrophobic
interactions, and hence the aggregation of the bulk protein
solution, increases dramatically.72 In fact, the inuence of
agitation can be so profound that, in the case of insulin,
it was found to attenuate the effects of other parameters,
such as protein concentration and ionic strength, that
inuence the kinetics of amyloid bril assembly.68
Molecular Models and Theoretical Aspects
The complexity of protein molecules with respect to confor-
mational heterogeneity as well as intra- and intermolecular
interactions between amino acid residues, with the consequent
differences in the exibility of secondary conformations and
tertiary congurations between proteins, results in variations
in their solution properties in shear ow. Indeed, differences in
the levels of association in diverse protein systems dictate the
different degrees of shielding, especially of hydrophobic resi-
dues concealed in the protein matrix, from hydrodynamic drag
during shear ow.83,84 Hence, it is difcult to obtain uniform
data to allow the formulation of a theoretical model relating
protein conformation to shear. For these reasons, dilute solu-
tions of homopolymers, especially unbranched polymer
chains, have been used as model systems for shear studies
because of their inherent structural uniformity.
By virtue of its conformational plasticity in response to
temperature, pH, salt concentration and alcohol content in
solution,24 poly-L-lysine is commonly used as a model system
in protein studies.85 The homopolypeptide exists as a
random coil at neutral pH, a-helix at high alkaline pH andb-sheet at temperatures[308C.86 For these reasons, poly-L-lysine is the ideal choice in probing the initial conformational
transitions, under denaturing conditions, between the three
basic protein secondary conformations namely: random coil,
a-helix, and b-sheet.Experimental studies on the shear-stability of poly-L-ly-
sine solutions (437 kDa), in an initial a-helical conformation,showed an increase in solution viscosity and turbidity with
shearing time.87 A combination of Raman spectroscopy (col-
lected in situ) and circular dichroism were employed for data
acquisition in a Couette ow cell at 150 s21. In addition, a
ow induced-gelation and an increase in the b-sheet contentof the samples was observed in solution concentrations[0.3g/dL. However, the circular dichroism data further revealed a
reversal of the a-helix to b-sheet conformational transitionafter prolonged shearing ([50 min). The observed confor-mational change and subsequent aggregation of the sheared
samples was thought to involve ow-enhanced hydrophobic
interactions between individual poly-L-lysine molecules in
solution.87 Further studies, via real-time circular birefrin-
gence measurements, showed a reversible, shear-induced, he-
lix-to-coil transition of poly-L-lysine in simple shear ow.24
The conformational transition was observed at a critical
strain rate of 300 s21, and the change was attributed to a
shear-induced breakage of intramolecular hydrogen bonds in
a-helical poly-L-lysine.More recently, the molecular-weight-dependence of the
shear-induced unfolding of a-helical poly-L-lysine in Couetteow has been measured in real-time using circular dichroism
spectroscopy.55 The authors observed that the shear-stability of
the helices increased as a function of molecular weight. The hys-
teresis observed in the heavy chains was attributed to the large
network of hydrogen bonds (cohesive force) stabilizing the helix
structure, and the associated hydrodynamic screening of helical
segments from the drag in the ow eld. Interestingly, irrespec-
tive of the molecular weight of poly-L-lysine, unfolding of the
helical segments was found to occur at a critical strain ( _ctc)value of 105 (Figure 4), similar to that observed in globularproteins.39,40 For this reason, the authors proposed that the
shear rate is not as critical as the duration of its application,
which makes the idea of a critical shear rate arbitrary. In
addition, the helix content, a, was found to show a powerlaw dependence with strain: a _ct1=2.
The inherent monodispersity associated with lamda bacte-
riophage DNA made it another ideal model for studies of
polymer dynamics in hydrodynamic ows. For example, a
novel real-time uorescence videomicrocopy of uorescently
labeled single DNA molecules was developed to visualize the
740 Bekard et al.
Biopolymers
-
conformational dynamics of DNA chains in both elongation21
and shear16 ows. The elongation and shear ow experiments
were performed in a microfabricated ow cell and between
two parallel glass plates (50 lm gap), respectively, at verylow shear rates ranging from 0.05 to 4.0 s21. It was found that,
at relatively high shear rates, the sharp coil-stretch transitions
of DNA chains observed in pure elongation ow was absent in
shear ow.16,21 Individual chains in steady shear ow rather
showed large, aperiodic temporal uctuations in conforma-
tion, consistent with what had been predicted in theory.84 In
addition, stretching of DNA chains in shear ow occurred at a
strain value\50 (101),16 which is several orders of magni-tude lower than the 105 critical strain value observed forpoly-L-lysine55 as well as folded proteins.39,40
Jaspe and Hagen41 suggests that coil-stretch transitions
readily occur in homopolymer systems because the free
energy cost of unfolding is negligible compared to that of a
native protein, and this was purported to explain why an ex-
traordinarily high shear rate (107 s21) is required to destabi-
lize the latter. Another study88 estimated a destabilizing
strain rate in the region of 108 s21 for collapsed polymers in
planar shear ow.
Classical theories on the shear-stability of polymer chains
predict that a polymer chain would remain in a coil state in
shear ow until a critical velocity gradient, which triggers an
abrupt unwinding of the coil, is reached.86 In addition,
abrupt conformational transitions are not expected in simple
shear ow since the occurrence of extensional strain, hence
polymer stretching, is random. It is hypothesized that at very
high strain rates, where polymer chains spend a relative short
time (residence time) in an extensional ow eld, no unfold-
ing or incomplete chain extensions may occur.45 These pre-
dictions were substantiated in later studies that simulated
polymer dynamics in shear ow. For example, in molecular
dynamics (MD) simulations of a grafted collapsed macro-
molecule in strong uniform ow, it was observed that a exi-
ble macromolecule remains compact below a critical shear
value but shows a globule-stretch transition above this criti-
cal shear value.89 The transition was reported to be more
pronounced in strong extensional ow.
Lemak et al.90 later compared the conformational instabil-
ities of a minimalist b-barrel protein in both uniform andelongational ow elds using MD simulations. It was
reported that whereas unfolding was abrupt in elongational
ow, the uniform ow elds presented a multi-step unfold-
ing process, with several intermediates, depending on the
tethered terminus of the protein. In explaining this observa-
tion, it was proposed that whereas every monomer (i.e.,
amino acid residues) experienced a destabilizing hydrody-
namic drag in elongational ow, only the terminal monomer
experiences this force in uniform ow. Hence, in uniform
ow, deformation of the protein follows an unzipping mech-
anism where the b-strands are unfolded one at a time, lead-ing to the evolution of intermediate states. More importantly,
it was evident that the nature of the applied external force
dictated the preferred mechanism for protein unfolding.
Szymczak and others observed similar ow effects on
employing Brownian dynamics simulations to examine ow-
induced stretching of integrin and ubiquitin.91,92 They noted
that the hydrodynamic drag on a grafted protein chain in
extensional ow increases along the chain length as the poly-
mer unfolds. Therefore, the initiation of unfolding triggers a
positive feedback mechanism which leads to the rapid unravel-
ing of the entire chain to the exclusion of intermediate states.
Indeed, it had previously been predicted that the uid drag
acting on an initially coiled polymer increases as the molecule
unfolds due to the decreased hydrodynamic interactions
between its constituent monomers.84,93 In addition, the
authors observed that whereas the grafted protein chains
unfold through a series of intermediate states in uniform ow,
consistent with that reported earlier,90 synthetic helices unrav-
eled smoothly with no detectable intermediate states.91 This
highlights the fact that proteins and homopolymers do indeed
differ in their hydrodynamic properties in shear ow. Further-
more, it was also noted that the array of metastable conforma-
tions observed during protein unfolding in uniform ow was
absent in mechanical pulling measurements in a force clamp
apparatus such as the atomic force microscope.
FIGURE 4 Change in the helix content of PLL as a function of
shear strain. The gure shows that the a-helix-PLL structure (68.3kDa) is stable below a strain value of 105. For clarity, the shear rates
plotted are: (&) 74 s21, (^) 302 s21, (*) 518 s21, and (l) 715s21. For clarity, error bars representing 6 standard deviation areshown only for the sample sheared at 518 s21.55
Effects of Shear Flow on Protein Structure and Function 741
Biopolymers
-
A subsequent study examined the inuence of hydrody-
namic interactions, which facilitate the folding of protein
molecules into compact native structures, on the mechani-
cal stretching of proteins using ubiquitin as a model sys-
tem.94 Mechanical stretching at constant speed, at constant
force, and through uid ow was examined. It was found
that hydrodynamic interactions (cohesive forces) between
amino acid residues facilitated unfolding (stretching)
when a constant speed or force was applied to grafted
ubiquitin. This observation was explained on the basis
that an amino acid residue, which is pulled away from
the bulk protein, creates a ow which drags other residues
with it. In contrast, these cohesive forces were found to
counter uid forces by screening monomers concealed in
the protein matrix from the drag in the ow eld, thereby
hindering ubiquitin unfolding in both uniform and elon-
gational ow elds.94 It has been reported that hydrody-
namic interactions increase with increasing protein size
and hence inuence the critical shear rate required to
unfold a protein of radius R.88 However, the authors note
that this prediction pertains to solutions with high solvent
viscosity and low interfacial tension.
Recently, Sulkowska and Cieplak applied the coarse-
grained MD model to investigate the resistance of 7510 pro-
teins to mechanical stretching at a constant speed.95 Pulling
was done by the termini to determine the maximum force
of resistance, Fmax, of the protein chains. They restricted
their study to non-fragmented protein chains deposited in
the Protein Data Bank by August, 2005 and between 40 and
150 amino acid residues long. For specic sequential lengths
of proteins, the average Fmax increased with increasing chain
length. That is, longer protein chains showed better resist-
ance relative to shorter chains. In relation to conforma-
tional classes, a-proteins were found to be weak and gener-ated small Fmax values relative to b- and ab-proteins. Specif-ically, immunoglobulins and transport protein homologies
were shown to yield larger Fmax values. However, the
authors acknowledged that proteins with multi-a-domainsmay show a signicantly high resistance to mechanical
stretching. In total, 134 proteins were considered to be
strong with a threshold force of 170 pN. The authors pro-
posed that the mechanical strength of the strongest proteins
arises from a clamp consisting of long parallel b-strandswhich are stabilized by a network of intra- and intermolecu-
lar interactions.
Implications in Physiology and Bioprocessing
Proteins are known to show a strong conformation-function
relationship. Destabilization of the native protein structure
can potentially lead to the evolution of dysfunctional, aggre-
gation-prone species with undesirable effects.4 Reports in the
literature demonstrate that shear, which is a common stress
in both physiology20,58,96 and bioprocessing,13,18 can induce
protein deformation.97 Therefore, it is important to analyze
the relevance of shear stress to protein molecules under phys-
iological ow and in bioprocessing.
Pulsatile blood ow generates non-uniform shear stress
throughout the arterial system during circulation.96 Arterial
shear rates peak at 1640 s21, 96 reaching 104 s21, 58 in partly
clogged coronary arterioles. The literature contains a signi-
cant number of reports98107 (and references therein) linking
the haemodynamic stress generated on arterial walls during
microcirculation, specically in regions of relatively low
shear stress, to the pathogenesis of atherosclerosis through
the modulation of endothelial function.108 A characteristic
hallmark of this disease state is the deposition of amyloid-
like protein aggregates as plaque on arterial walls. Arterial
amyloid-plaques may trigger vascular inammation, weaken
the elasticity of blood vessels, and alter biochemical reactions
such as lipid metabolism.109 Interestingly, it has been shown
that molecular connement enhances the deformation of
entangled polymers under squeeze ow,110 a condition which
models pulsatile blood ow. Similarly, there are a consider-
ably number of reports27,34,35,42,59,60,111113 citing haemody-
namic shear stress as the primary facilitator of the proteolytic
cleavage of large vWF multimers freshly released from endo-
thelial cells as well as vWF-mediated platelet adhesion during
haemostasis. The accumulation of large vWF multimers in
the plasma may lead to disease states including thrombotic
thrombocytopenic purpura, microvascular occlusion and
atherosclerosis, due to the development of microvascular
thrombi resulting from the complexation of the hyperactive
vWF multimers and platelets at regions of low physiological
shear.63,114 On the other hand, the smaller size of circulating
vWF multimers, resulting from proteolysis, enhance their
haemostatic potential in high shear regimes as occurs during
arteriolar bleeding.62 The inuence of shear stress on the
activity of platelets and vWF has been discussed in other
review articles.57,58,63,115
Others have linked the deterioration in cerebral microcir-
culation (cerebral hypoperfusion) to the onset of protein
conformational disorders such as Alzheimers disease.116118
It is suggested that reduced cerebral blood ow may replace
old age as a risk factor for Alzheimers disease.118 It also pro-
posed that haemodynamic shear stress regulates insulin-like
growth factor-I activity indirectly, and possibly its effect on
vascular pathologies.119
It is noteworthy that although protein conformational
diseases and vascular disorders have received considerable
attention in research, the role of physiological shear stress in
742 Bekard et al.
Biopolymers
-
the initiation and/or progression of these debilitating diseases
remain to be fully understood.
In the case of bioprocessing, shear stresses are present dur-
ing the separation, purication, shipping, and handling of
protein based products.13 For example, processing steps
involving ultraltration reactors,120,121 stirred tanks,122,123
homogenizers,124 and pumps53,125 induce high shear stresses.
Simulated lobe pump studies have shown that high shear
stress in these processing steps is sufcient to cause minor
changes to protein structure.125 These structural changes
may trigger the exposure of hitherto buried hydrophobic
regions to the aqueous environment, initiating intra/inter-
molecular hydrophobic interactions leading to aggregation.
The simulation further suggests that shear stresses may have
played a crucial role in the protein aggregation behavior
observed in a previous lobe pump study.126 Indeed, protein
aggregation and particle formation during processing can
affect the efciency of protein recovery, efcacy, safety, and
product shelf-life.11 Furthermore, therapeutic protein aggre-
gates are associated with a range of clinical side effects
including non-specic anti-complementary activity leading
to anaphylactic shock.127,128 In addition, insoluble aggregates
can cause immune responses, lodge in the lung capillary bed,
and block blood vessels.129131
The design of experiments to establish the effect of uid
shear stress alone on protein structure and function has
proved difcult. Existing shear devices generate other stresses
including surface interactions and enhanced proteinair con-
tacts, which complicates data interpretation.121,132,133 How-
ever, it has been established that the shear-stability of a pro-
tein molecule depends on: (i) its primary structure and mo-
lecular weight (ii) the magnitude of shear strain and the
duration of its application, and (iii) the viscosity of its sur-
rounding medium.31,64,65 Therefore, these factors must be
taken in consideration for a complete understanding of the
shear-stability of protein systems. Advancing knowledge in
this eld will be crucial for the design of processes, especially
in the bioprocessing industry, to ensure protein stability,
maintain functionality, and promote process yield.
Future development of protein based products will
increasingly require several areas of improvement, especially
in-process-monitoring of the stability of protein solutions.
This will require the development of experimental techniques
to allow the measurement of shear stress on proteins of inter-
est. This is imperative as several studies show that individual
protein systems demonstrate unique ow properties in a
given ow eld. Additionally, it will be essential to appreciate
the shear ( _ct) thresholds beyond which particular proteinsystems destabilize in solution. This will inform the develop-
ment of new processing equipment to improve efciency
during production. It is noteworthy that knowledge from
such studies could contribute to our understanding of the
purported shear-induced pathogenesis of vascular and pro-
tein conformational disorders in vivo.
CONCLUSIONProtein unfolding and aggregation is an issue of concern
both in vitro and in vivo, specically in bioprocessing and in
the pathogenesis of disease. Shear rates less than 103 s21 have
been found to signicantly alter the three-dimensional struc-
ture of globular proteins, leading to aggregation and amyloid
bril formation. The strain history ( _ct) is found to be an im-portant parameter in the shear-effect. Therefore, even in
environments where ostensibly low shear is generated can
lead to shear-induced protein structural change. Given the
diversity of protein species, and the diversity of molecular
sizes, conformations and nature of intramolecular interac-
tions, the susceptibility of proteins to shear can vary. It is
clear that high shear generating processes should be avoided
in bioprocessing. Shear also exists in the circulatory system
and could be a signicant contributor to the pathogenesis of
certain diseases by facilitating the aggregation of aberrantly
folded proteins.
REFERENCES1. Petsko, G. A.; Ringe, D. Protein Structure and Function; New
Science Press: London, 2004.
2. Dobson, C. M. Trends in Biochemical Science 1999, 24,
329332.
3. Stefani, M.; Dobson, C. M. J Mol Med 2003, 81, 678699.
4. Dobson, C. M. Nature 2003, 426, 884890.
5. Chiti, F.; Dobson, C. M. Annu Rev Biochem 2006, 75,
333366.
6. Calamai, M.; Chiti, F.; Dobson, C. M. Biophys J 2005, 89,
42014210.
7. Wang, W. Int J Pharm 1999, 185, 129188.
8. Bryant, Z.; Pande, V. S.; Rokhsar, D. S. Biophys J 2000, 78,
584589.
9. Li, P.-C.; Makarov, D. E. J Chem Phys 2003, 119, 92609268.
10. Rohs, R.; Etchebest, C.; Lavery, R. Biophys J 1999, 76,
27602768.
11. Wang, W. Int J Pharm 2005, 289, 130.
12. Morel, M.-H.; Redl, A.; Guilbert, S. Biomacromolecules 2002,
3, 488497.
13. Thomas, C. R. In Chemical Engineering Problems in Biotech-
nology; Winkler, M. A., Ed.; Elsevier Applied Science: London,
1991, pp 2393.
14. Bekard, I.; Dunstan, D. E. J Phys Chem B Lett 2009, 113,
84538457.
15. Dunstan, D. E.; Hill, E. K.; Wei, Y. Macromolecules 2004, 37,
16631665.
16. Smith, D. E.; Babcock, H. P.; Chu, S. Science 1999, 283,
17241727.
Effects of Shear Flow on Protein Structure and Function 743
Biopolymers
-
17. Elias, C. B.; Joshi, J. B. Adv Biochem Eng Biotechnol 1997, 59,
4772.
18. Yim, S. S.; Shamlou, P. A. Adv Biochem Eng Biotechnol 2000,
67, 83122.
19. Lin, J.; Meyer, J. D.; Carpenter, J. F.; Manning, M. C. Pharm
Res 2000, 17, 391396.
20. Tangelder, G. J.; Slaaf, D. W.; Arts, T.; Reneman, R. S. Am J
Physiol 1988, 254, H1059H1064.
21. Perkins, T. T.; Smith, D. E.; Chu, S. Science 1997, 276,
20162021.
22. Danker, G.; Vlahovska, P. M.; Misbah, C. Phys Rev Lett 2009,
102, 148102.
23. Munson, B. R.; Young, D. F.; Okiishi, T. H.; Huebsch, W. W.
Fundamentals of Fluid Mechanics; Wiley: Hoboken, New
Jersey, 2009.
24. Lee, A. T.; McHugh, A. J. Biopolymers 1999, 50, 589594.
25. Hill, E. K.; Krebs, B.; Goodall, D. G.; Howlett, G. J.; Dunstan,
D. E. Biomacromolecules 2006, 7, 1013.
26. Dunstan, D. E.; Hamilton-Brown, P.; Asimakis, P.; Ducker, W.;
Bertolini, J. Soft Matter 2009, 5, 50205028.
27. Singh, I.; Themistou, E.; Porcar, L.; Neelamegham, S. Biophys J
2009, 96, 23132320.
28. Dunstan, D. E.; Hamilton-Brown, P.; Asimakis, P.; Ducker, W.
A.; Bertolini, J. Protein Eng Des Sel 2009, 22, 741746.
29. Imomoh, E.; Dusting, J.; Ashton, L.; Blanch, E.; Balabani, S.
14th International Symposium on Applications of Laser Tech-
niques to Fluid Mechanics, Lisbon, Portugal, 2008.
30. Ashton, L.; Dusting, J.; Imomoh, E.; Balabani, S.; Blanch, E. W.
Biophys J 2009, 96, 42314236.
31. van der Veen, M. E.; van Iersel, D. G.; van der Goot, A. J.;
Boom, R. M. Biotechnol Progr 2004, 20, 11401145.
32. Charm, S. E.; Wong, B. L. Science 1970, 170, 466468.
33. Charm, S. E.; Lai, C. J. Biotechnol Bioeng 1971, 13, 185202.
34. Peterson, D. M.; Stathopulos, N. A.; Giorgio, T. D.; Hellums, J.
D.; Moake, J. L. Blood 1987, 69, 625628.
35. Ikeda, Y.; Handa, M.; Kawano, K.; Kamata, T.; Murata, M.;
Araki, Y.; Anbo, H.; Kawai, Y.; Watanabe, K.; Itagaki, I.; Sakai,
K.; Ruggeri, Z. M. J Clin Investig 1991, 87, 12341240.
36. Thomas, C. R.; Dunnill, P. Biotechnol Bioeng 1979, 21, 2279
2302.
37. Thomas, C. R.; Nienow, A. W.; Dunnill, P. Biotechnol Bioeng
1979, 21, 22632279.
38. Maa, Y.; Hsu, C. C. Biotechnol Bioeng 1996, 51, 458465.
39. Tirrell, M.; Middleman, S. Biotechnol Bioeng 1975, 17, 299303.
40. Charm, S. E.; Wong, B. L. Biotechnol Bioeng 1970, 12,
11031109.
41. Jaspe, J.; Hagen, S. J. Biophys J 2006, 91, 34153424.
42. Schneider, S. W.; Nuschele, S.; Wixforth, A.; Gorzelanny, C.;
Alexander-Katz, A.; Netz, R. R.; Schneider, M. F. Proc Natl
Acad Sci 2007, 104, 78997903.
43. Chien, S.; Skalak, R. Biorheology 1981, 18, 307330.
44. Bell, D. J.; Dunnill, P. Biotechnol Bioeng 1982, 24, 12711285.
45. Cathey, C. A.; Fuller, G. G. J Non-Newtonian Fluid Mechanics
1990, 34, 6388.
46. Rodel, W. In Instrumentation and Sensors for the Food Indus-
try; Kress-Rogers, E., Ed.; Butterworth-Heinemann: Oxford,
1993, pp 375415.
47. Hill, E. K.; Watson, R. L.; Dunstan, D. E. J Fluorescence 2005,
15, 255266.
48. Guyon, E.; Hulin, J. P.; Petit, L.; Mitescu, C. D. Physical Hydro-
dynamics; Oxford University Press: New York, 2001.
49. Taylor, G. I. Philosophical Transactions Royal Society London
Series A 1923, 223, 289343.
50. van Wazer, J. R.; Lyon, J. W.; Kim, K. Y.; Colwell, R. E. Viscosity
and Flow Measurement; Interscience Publishers: New York,
1963.
51. Charm, S. E.; Wong, B. L. Biotechnol Bioeng 1978, 20,
451453.
52. Bowen, W. R.; Gan, Q. Biotechnol Bioeng 1992, 40, 491497.
53. Virkar, P. D.; Narendranathan, T. J.; Hoare, M.; Dunnill, P.
Biotechnol Bioeng 1981, 23, 425429.
54. Talboys, B. L.; Dunnill, P. Biotechnol Bioeng 1985, 27,
17301734.
55. Bekard, I. B.; Barnham, K. J.; White, L. R.; Dunstan, D. E. Soft
Matter 2011, 7, 203210.
56. Dong, J.; Moake, J. L.; Nolasco, L.; Bernardo, A.; Arceneaux,
W.; Shrimpton, C. N.; Schade, A. J.; McIntire, L. V.; Fujikawa,
K.; Lopez, J. A. Blood 2002, 100, 4033.
57. Sadler, J. E. Annu Rev Biochem 1998, 67, 395424.
58. Kroll, M. H.; Hellums, J. D.; McIntire, L. V.; Schafer, A. I.;
Moake, J. L. Blood 1996, 88, 15251541.
59. Tsai, H. M.; Sussman, I. I.; Nagel, R. L. Blood 1994, 83,
2171.
60. Siedlecki, C. A.; Lestini, B. J.; Kottke-Marchant, K.; Eppell, S.
J.; Wilson, D. L.; Marchant, R. E. Blood 1996, 88, 29392950.
61. Mody, N. A.; Lomakin, O.; Doggett, T. A.; Diacovo, T. G.;
King, M. R. Biophys J 2005, 88, 14321443.
62. Zhang, X.; Halvorsen, K.; Zhang, C. Z.; Wong, W. P.; Springer,
T. A. Science 2009, 324, 1330.
63. Sadler, J. E. Annu Rev Med 2005, 56, 173191.
64. Maa, Y.; Hsu, C. C. Biotechnol Bioeng 1997, 54, 503512.
65. Oliva, A.; Santovena, A.; Farina, J.; Llabres, M. J Pharm
Biomed Anal 2003, 33, 145155.
66. Ramirez-Alvarado, M.; Merkel, J. S.; Regan, L. Proc Natl Acad
Sci 2000, 97, 89798984.
67. Ahmad, A.; Uversky, V. N.; Hong, D.; Fink, A. L. J Biol Chem
2005, 280, 42669.
68. Nielsen, L.; Khurana, R.; Coats, A.; Frokjaer, S.; Brange, J.;
Vyas, S.; Uversky, V. N.; Fink, A. L. Biochemistry 2001, 40,
60366046.
69. Grainger, R. J.; Ko, S.; Koslov, E.; Prokop, A.; Tanner, R. D.;
Loha, V. Appl Biochem Biotechnol 2000, 84, 761768.
70. Sluzky, V.; Tamada, J. A.; Klibanov, A. M.; Langer, R. Proc Natl
Acad Sci USA 1991, 88, 93779381.
71. Sluzky, V.; Klibanov, A. M.; Langer, R. Biotechnol Bioeng 1992,
40, 895903.
72. Hamilton-Brown, P.; Bekard, I.; Ducker, W. A.; Dunstan, D. E.
J Phys Chem B 2008, 112, 1624916252.
73. Sasahara, K.; Yagi, H.; Sakai, M.; Naiki, H.; Goto, Y. Biochemis-
try 2008, 47, 26502660.
74. Ohhashi, Y.; Kihara, M.; Naiki, H.; Goto, Y. J Biol Chem 2005,
280, 32843.
75. Sicorello, A.; Torrassa, S.; Soldi, G.; Gianni, S.; Travaglini-Allo-
catelli, C.; Taddei, N.; Relini, A.; Chiti, F. Biophys J 2009, 96,
22892298.
76. Stathopulos, P. B.; Scholz, G. A.; Hwang, Y. M.; Rumfeldt,
J. A. O.; Lepock, J. R.; Meiering, E. M. Protein Sci 2004, 13,
30173027.
744 Bekard et al.
Biopolymers
-
77. Akkermans, C.; Venema, P.; Rogers, S. S.; van der Goot, A.
J.; Boom, R. M.; van der Linden, E. Food Biophys 2006, 1,
144150.
78. Akkermans, C.; van der Goot, A. J.; Venema, P.; van der
Linden, E.; Boom, R. M. Food Hydrocolloids 2008, 22, 1315
1325.
79. Alexander-Katz, A.; Netz, R. R. Europhys Lett (EPL) 2007, 80,
18001.
80. Bee, J. S.; Stevenson, J. L.; Mehta, B.; Svitel, J.; Pollastrini, J.;
Platz, R.; Freund, E.; Carpenter, J. F.; Randolph, T. W. Biotech-
nol Bioeng 2009, 103, 936.
81. Adamson, A. W.; Gast, A. P.; NetLibrary, I. Physical Chemistry
of Surfaces; Wiley: New York, 1997.
82. Best, R. B.; Brockwell, D. J.; Toca-Herrera, J. L.; Blake, A. W.;
Smith, D. A.; Radford, S. E.; Clarke, J. Anal Chim Acta 2003,
479, 87105.
83. Agarwal, U. S.; Mashelkar, R. A. J Chem Phys 1994, 100,
60556061.
84. De Gennes, P. G. J Chem Phys 1974, 60, 50305042.
85. Greeneld, N. J.; Fasman, G. D. Biochemistry 1969, 8, 4108
4116.
86. JiJi, R. D.; Balakrishnan, G.; Hu, Y.; Spiro, T. G. Biochemistry
2006, 45, 3441.
87. Immaneni, A.; McHugh, A. J. Biopolymers 1998, 45, 239
246.
88. Alexander-Katz, A.; Netz, R. R. Macromolecules 2008, 41,
33633374.
89. Buguin, A.; Brochard-Wyart, F. Macromolecules 1996, 29,
49374943.
90. Lemak, A. S.; Lepock, J. R.; Chen, J. Z. Y. Proteins Struct Funct
Genet 2003, 51, 224235.
91. Szymczak, P.; Marek, C. J Chem Phys 2006, 125, 164903.
92. Szymczak, P.; Cieplak, M. J Chem Phys 2007, 127, 155106.
93. Agarwal, U. S.; Rohit, B.; Mashelkar, R. A. J Chem Phys 1998,
108, 16101617.
94. Szymczak, P.; Cieplak, M. J Phys Condensed Matter 2007, 19,
285224285235.
95. Sulkowska, J. I.; Cieplak, M. Biophys J 2008, 94, 613.
96. Stroev, P. V.; Hoskins, P. R.; Easson, W. J. Atherosclerosis 2007,
191, 276280.
97. McNally, E.; Lockwod, C. In Protein Formulation and
Delivery; McNally, E., Ed.; Marcel Dekker: New York, 2000,
pp 111138.
98. Ge, J.; Erbel, R.; Gorge, G.; Haude, M.; Meyer, J. Br Heart J
1995, 73, 462465.
99. Ku, D. N.; Giddens, D. P.; Zarins, C. K.; Glagov, S. Arterioscler
Thromb Vasc Biol 1985, 5, 293302.
100. Malek, A. M.; Alper, S. L.; Izumo, S. JAMA 1999, 282,
20352042.
101. Cunningham, K. S.; Gotlieb, A. I. Lab Invest 2004, 85, 9
23.
102. Krams, R.; Wentzel, J. J.; Oomen, J. A. F.; Vinke, R.; Schuurb-
iers, J. C. H.; De Feyter, P. J.; Serruys, P. W.; Slager, C. J. Arte-
rioscler Thromb Vasc Biol 1997, 17, 2061.
103. Gibson, C. M.; Diaz, L.; Kandarpa, K.; Sacks, F. M.; Pasternak,
R. C.; Sandor, T.; Feldman, C.; Stone, P. H. Arterioscler
Thromb Vasc Biol 1993, 13, 310.
104. Shaaban, A. M.; Duerinckx, A. J. Am J Roentgenol 2000, 174,
1657.
105. Vita, J. A.; Treasure, C. B.; Ganz, P.; Cox, D. A.; David Fish, R.;
Selwyn, A. P. J Am Coll Cardiol 1989, 14, 11931199.
106. Davies, P. F.; Remuzzi, A.; Gordon, E. J.; Dewey, C. F.;
Gimbrone, M. A. Proc Natl Acad Sci USA 1986, 83, 2114.
107. Irace, C.; Cortese, C.; Fiaschi, E.; Carallo, C.; Farinaro, E.;
Gnasso, A. Stroke 2004, 35, 464.
108. Jiang, Y.; Kohara, K.; Hiwada, K. Stroke 2000, 31, 23192324.
109. Howlett, G. J.; Moore, K. J. Curr Opin Lipidol 2006, 17, 541.
110. Rowland, H. D.; King, W. P.; Cross, G. L. W.; Pethica, J. B. ACS
Nano 2008, 2, 419428.
111. Alevriadou, B. R.; Moake, J. L.; Turner, N. A.; Ruggeri, Z. M.;
Folie, B. J.; Phillips, M. D.; Schreiber, A. B.; Hrinda, M. E.;
McIntire, L. V. Blood 1993, 81, 1263.
112. Goto, S.; Salomon, D. R.; Ikeda, Y.; Ruggeri, Z. M. J Biol Chem
1995, 270, 23352.
113. Chow, T. W.; Hellums, J. D.; Moake, J. L.; Kroll, M. H. Blood
1992, 80, 113.
114. Tsai, H. M. Semin Thromb Hemost 2003, 29, 479488.
115. Reininger, A. J. Haemophilia 2008, 14, 1126.
116. de la Torre, J. C. Lancet Neurol 2004, 3, 184190.
117. de La Torre, J. C. Neurol Res 2004, 26, 517524.
118. Crawford, J. G. Med Hypotheses 1998, 50, 2536.
119. Elhadj, S.; Akers, R. M.; Forsten-Williams, K. Ann Biomed Eng
2003, 31, 163170.
120. Ahrer, K.; Buchacher, A.; Iberer, G.; Jungbauer, A. J Membr Sci
2006, 274, 108115.
121. Kim, K. J.; Chen, V.; Fane, A. G. Biotechnol Bioeng 1993, 42,
260265.
122. Cutter, L. A. AIChE J 1966, 12, 3545.
123. Kresta, S. M.; Wood, P. E. AIChE J 1991, 37, 448460.
124. Floury, J.; Bellettre, J.; Legrand, J.; Desrumaux, A. Chem Eng
Sci 2004, 59, 843853.
125. Gomme, P. T.; Prakash, M.; Hunt, B.; Stokes, N.; Cleary, P.;
Tatford, O. C.; Bertolini, J. Biotechnol Appl Biochem 2006, 43,
113120.
126. Gomme, P. T.; Hunt, B.; Tatford, O. C.; Johnston, A.; Bertolini,
J. Biotechnol Appl Biochem 2006, 43, 103111.
127. Thornton, C. A.; Ballow, M. Arch Neurol 1993, 50, 135136.
128. Wang, Y.-C. J.; Hanson, M. A. J Parenteral Sci Technol 1988,
42, S3S26.
129. Katakam, M.; Banga, A. K. J Pharm Pharmacol 1995, 47,
103107.
130. Cleland, J. L.; Powell, M. F.; Shire, S. J. Crit Rev Ther Drug
Carrier Syst 1993, 10, 307377.
131. Dorris, G. G.; Bivins, B. A.; Rapp, R. P.; Weiss, D. L.; DeLuca,
P. P.; Ravin, M. B. Anesth Analg 1977, 56, 422427.
132. Meireles, M.; Aimar, P.; Sanchez, V. Biotechnol Bioeng 1991,
38, 528534.
133. Narendranathan, T. J.; Dunnill, P. Biotechnol Bioeng 1982, 24,
21032107.
Reviewing Editor: Stephen Blacklow
Effects of Shear Flow on Protein Structure and Function 745
Biopolymers