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* Chemical Engineering Department, Ben-Gurion University, Beer-Sheva, Israel; and
Laboratoire Physicochimie "Curie", UMR 168, Institut Curie/Centre National de la Recherche Scientifique, Paris, France
Correspondence: Address reprint requests to Cécile Sykes, Tel.: 33-1-423-46790; E-mail: cecile.sykes{at}curie.fr.
| ABSTRACT |
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| INTRODUCTION |
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The challenge in understanding the physical mechanism of force generation by actin assembly has given rise to various theoretical descriptions (7
12
). For many years Listeria monocytogenes was used as a model system for studying the biochemistry of actin-based movement (3
) and the effect of external influences on its movement (13
). Listeria move at a velocity of a few µm/min, either smoothly or in a periodic fashion, as observed sometimes for wild-type bacteria (14
) or genetically modified bacteria (15
). However, the use of Listeria for testing theoretical models suffers from the drawback that geometrical parameters such as its size and shape are predetermined, and that the surface density of the Arp2/3 complex bacterial activator (ActA) is unknown. Biophysical studies on movement induced by actin polymerization were greatly facilitated by the development of in vitro systems that explore actin-driven motility of nonbiological cargos such as protein-coated beads (16
) and lipid vesicles (17
,18
) placed in cell extracts. The discovery of the minimal set of proteins needed for reconstituting the movement of Listeria (19
) opened the way for a controlled study of the physical parameters involved in actin-based motility (20
). Such a system enables a detailed analysis of the physical parameters that govern actin-based movement. It was already experimentally demonstrated that at a fixed surface density of the actin polymerization activator, the type of movement is dramatically affected by changing the microsphere diameter, shifting it from a continuous to a jerky movement which resembles that of the mutated hopping Listeria (15
).
In the work presented here, we investigate experimentally the bead diameter-protein surface density parameter space. Previously, only the influence of bead diameter was investigated in detail (20
). We show that the transition from continuous to periodic regimes of motion can be induced simply by increasing the activating protein surface density as well as increasing the bead diameter. We further provide a scaling analysis of the transition from continuous to periodic regimes, and of the characteristics of this periodic regime. This analysis extends previous published works (10
,21
) that only provided numerical results relevant to the Listeria geometry. Here, we provide scaling guidelines for locating the transition from continuous to periodic behaviors and for characterizing the periodic regime. We finally compare these expectations to experimental results.
| MATERIALS AND METHODS |
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Protein coating of polystyrene beads
Polystyrene beads of diameter ranging from 1 to 9.1 µm were purchased from Polyscience (Niles, IL). The error bars in bead diameter were given by the manufacturer (see Table 1). We varied the protein concentration on the surface by changing the protein concentration in the incubating solution. The beads were incubated in the protein solution at concentrations in the range of 0.011 mg/ml for 1 h at room temperature. We used an initial volume of beads that was proportional to the diameter, i.e., volumes of 1 µl and 10 µl for beads of 1 µm and 10 µm diameters, respectively, given that the volume fraction of the beads in the stock solution was constant, equal to 2.5%. The beads were finally resuspended in a constant total volume of 20 µl to ensure a constant total surface area independently of the bead diameter. The beads were stored at 4°C in a storage buffer (20 mM phosphate buffer pH = 7.4, 150 mM NaCl, 1.5 mM NaN3, 10 mg/ml BSA, 5% glycerol) for up to 1 week.
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Motility assay
The motility medium contained 8.5 mM HEPES, pH = 7.7, 1.7 mM Mg-ATP, 5.5 mM DTT, 0.12 mM Dabco, 0.1 M KCl, 1 mM MgCl2, 6.5 µM F-actin, 0.1 µM Arp2/3 complex, 0.046 µM capping proteins, 2.5 µM ADF, 2.5 µM profilin, 0.54 µM
-actinin, 0.31% methyl-cellulose, 0.75% BSA, and 1.1 µM actin-rhodamin as optimized for Listeria movement (19
). No vasodilator-stimulated phosphoprotein (VASP) was needed. A 0.3-µl volume of bead suspension was added to 20 µl of motility medium. The small volume of the beads ensured that the composition of the motility medium remained unchanged. The sample was placed immediately between a glass slide and an 18-mm-square glass coverslip sealed with vaseline/lanolin/paraffin (at weight ratio of 1:1:1). To prevent squeezing of the objects, the distance between slide and coverslip was controlled using an inert polyethylene-glycol spacer (Goodfellow, Berwyn, PA) to obtain a ratio between sample height and bead diameter of 5:6. This ratio was found to ensure that the beads with their comets do not stick to the coverslip walls. In all experiments, symmetry breaking occurs spontaneously and 100% of the beads generate a comet.
Tracking and imaging of bead movement
The characterization of the bead movement, polymerization dynamics, and comet structure were performed by means of phase contrast and fluorescence microscopy techniques (Olympus IX51 microscope, Melville, NY). Each data point was obtained by averaging experimental data from a minimum of 10 beads. The movement of the microspheres was tracked during 1.5 h by timelapse optical video-microscopy. Measurement of the beads velocity was performed as in Bernheim-Groswasser et al. (20
). The thickness of the actin gel in the comet of saltatory moving beads was determined as the distance between the inflection points in the gray-level intensity curve obtained as a linescan of the middle of the comet.
| RESULTS |
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2.1 µm) always move continuously regardless of the surface concentration value Cs, whereas larger beads (2.1 < D < 9.14 µm diameter) exhibit transitions from saltatory to continuous motion by decreasing Cs. The largest beads in this study, 9.1 µm in diameter, always moved in a saltatory manner in the experimentally investigated domain, Cs
Css = (6 ± 1) x 102 molecules/nm2, with Css corresponding to the saturating conditions. The dashed-dot line in Fig. 1 marks the approximate boundary between the two regimes. The critical surface concentration at which the regime changes from continuous to saltatory is a strongly decreasing function of the bead diameter. In addition to the continuous and saltatory regimes, an intermittent regime is identified at a saturating protein surface concentration (Css) and for an intermediate bead diameter of 2.8 µm (open triangle in Fig. 1).
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(time derivative of X(t)) was then calculated. The velocity of a 6.3-µm-diameter bead moving in a periodic motion is plotted in Fig. 3. The saltatory motion is characterized by a velocity cycle that starts at a maximal velocity Vmax, passes through a minimal velocity Vmin, and ends at Vmax. A careful look at a typical velocity cycle starting from Vmax reveals three phases. The first two phases correspond to a steep decrease of the velocity to Vmin, followed by a slow increase of the velocity. These two phases are achieved in a total characteristic time
' (Fig. 3), which is also the time needed for growing a gel of thickness e*. The third phase is a steep increase of the velocity to Vmax and corresponds to the expulsion of the bead from the actin shell of thickness e*. This expulsion phase is achieved in a characteristic time
(Fig. 3). For different bead sizes, we measured experimentally the characteristic time
' required for growing a gel of thickness e* (see Table 1). We found that for beads of large diameter (D > 2.8 µm), the time
' is always smaller than the time of symmetry breaking (ts), which is the time necessary to built the first layer. Note that this layer is always larger than e*. In the case of 2.8-µm-diameter beads, ts equals
' within experimental error and the thickness of the first layer equals the thickness of the other layers (see also Fig. 2). Additionally, we define as
rep the time that corresponds to the first phase (steep decrease of the velocity from Vmax to Vmin). All times
',
, and
rep are defined in Fig. 3 and their experimental values are given in Table 1.
To analyze the transition from continuous to saltatory movement, we define the velocity amplitude (Vmax Vmin). The transition from steady to periodic movement is determined by plotting the normalized velocity amplitude
as a function of the two control parameters of the system, D or Cs. A typical first-order (discontinuous) transition appears in Fig. 4, where
is plotted as function of the bead diameter D for a saturating activator surface density Css. Small beads (D
2.1 µm) move smoothly, thus
Increasing the bead diameter (D
2.8 µm) induces a transition to a motion type for which
: for intermediate bead diameters (D = 2.8 µm) we observe the coexistence of two regimes of motion (solid dash-dot double arrow in Fig. 4)a steady one, where (Vmax Vmin) = 0 and a saltatory one, with (Vmax Vmin)
0. In that case, the bead movement is intermittent, and shifts randomly from one velocity regime to the other. For larger bead diameters (D > 2.8 µm) the movement is always periodic,
and the velocity amplitude decreases with D (Fig. 4).
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| DISCUSSION |
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rr depends on the square of the gel thickness e and on the bead diameter
where Y is the elastic modulus of the gel. This formula, used in the case of a nonmoving spherical bead in Noireaux et al. (14
L of the gel relative to the bead is thus
As a result, the total elastic force scales like the cube of e (21
![]() | (1) |
Introducing the elastic force per activator, fe, we get
![]() | (2) |
A complete analysis of the bead movement must include a description of the polymerization dynamics during a complete velocity cycle. From Eq. 2 one finds that the propulsion force increases with the gel thickness e. Since the maximal value of e is found experimentally to be independent of the bead size e = e* = 1.5 ± 0.2 µm (Fig. 2), the maximal value of the elastic force reads
![]() | (3) |
The friction force
There are two contributions to the friction between the bead and the gel: one is the standard contact surface friction, which is simply proportional to the bead-gel relative velocity and the contact area. It is described by a constant surface friction coefficient,
s. Such a term always exists: it results either from the direct friction of the filaments on the solid surface, or from the indirect friction transmitted by the fluid to the solid surface. The second term is more subtle, and results from the existence of a finite average time over which an actin filament is bound to an activator, or, in other terms, to transient attachments to the surface of the bead (8
,9
). It is proportional to the friction area, the protein surface density Cs, and the average force between an actin filament and an actin polymerization activator,
Hence the total friction force, Ff can be written as (9
,10
)
![]() | (4) |
Per actin polymerization activator, the friction force can be expressed as
![]() | (5) |
and thus ff, depend on V in a nontrivial way (9
is proportional to V with a coefficient that we denote
(
; and a large friction coefficient per nucleator,
can be defined (ff =
V) (equivalently, if we note ß the friction coefficient, the friction force per unit surface reads Cs
V = ßV).
is inversely proportional to the bead velocity:
Thus at large velocities,
vanishes and the only contribution to the friction force comes from the standard friction
s.
Cs >
s), due to the fact that fewer bonds are present between the bead and the actin gel in the second branch.
|
. If
is long compared to the time
' required for growing a gel layer around the bead, this gel layer is maintained, the system is at steady state and the bead motion is continuous at a constant velocity Vcont (Fig. 7). In the continuous regime, it is difficult to obtain an exact experimental estimate of the gel thickness around the bead. However, we observe that this thickness is not larger than the 1.5-µm thickness that corresponds to e* (see, for example, the continuous regime bead of Fig. 1). If
is short compared to
', the consequence will be the appearance of a saltatory motion where fe
fth (see ff(V) and fe(D2) in Fig. 6 and ff(Cs1) and fe(Cs1) in Fig. 7). For saltatory motion, a velocity cycle that starts at a maximal velocity Vmax passes through a minimal velocity Vmin, and ends at Vmax. Rough estimates of the times
and
' gives
and
(where
p is the velocity of polymerization on the bead surface). The condition for obtaining a saltatory motion is thus
Given that D > e* (see Fig. 2), the maximal velocity is always greater than the polymerization velocity. This is in agreement with our experiments since the maximal velocity is of the order of 1 µm/min (20
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1 µm/min) is in agreement with the theoretical analysis of the force-velocity curve depicted in Fig. 6. One can see that the intersection of the elastic force fe(D1) with the fast branch of the friction force ff(V) (c-d segment) results in a high and constant velocity. The increase of D reduces the propulsion force and drives the system toward the saltatory regime (ff(V) and fe(D2) curves, Fig. 6) as observed experimentally (Figs. 1 and 4).
Conversely, varying the surface nucleator concentration at constant bead diameter also allows exploring the system state diagram. At a given velocity, the friction force per nucleator decreases when the nucleator density is increased:
is independent of Cs, whereas the second term of Eq. 5 is inversely proportional to Cs. As a consequence, the slope of the c-d part is a decreasing function of Cs, as shown in Fig. 7.
The Cs dependence of the propulsion force is difficult to assess. A naive analysis would predict an increase of the elastic modulus with Cs. However, under strong branching conditions controlled by the Arp2/3 complex, the elastic modulus Y should become essentially independent of Cs. Thus the propulsion force per activator should increase upon decreasing Cs. Thus, starting from a saltatory regime and decreasing Cs at constant D should lead the system to a continuous regime according to Fig. 7. Note that the stationary velocity Vcont in the continuous regime is smaller than the maximal velocity Vmax in the saltatory regime in a suitable parameter range. This corresponds to our experimental observations, since
is 2.6 and 4.3 for 6.3-µm-diameter beads coated with 0.37 x Css and 0.02 x Css proteins, respectively, and 1.8 for 4.5-µm-diameter beads coated with 0.195 x Css proteins.
Analysis of the saltatory regime and numerical estimates
In a velocity cycle, the maximal velocity is obtained for the smallest friction force. Considering the simple argument that the new actin gel is in a triangle defined by
and e*, where the gel moves parallel to the bead surface (see Fig. 8), we find that
equals
Under these conditions the total friction force applies on a surface of the order of D x l, hence
![]() | (6) |
s is the constant surface friction coefficient corresponding to the fast branch of the friction force curve (c-d segment of ff(V), Fig. 6). The maximal velocity Vmax can now be deduced by equating Ff to the total propulsion force
(see Eq. 1):
![]() | (7) |
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Cs is the friction coefficient and D2 is the bead-gel friction area. The minimal velocity Vmin results from the balance between the total friction force ßD2Vmin and the total elastic propulsion force
where
is the gel thickness around the bead when it is propelled at the velocity Vmin. The value of
is not accessible directly from our experiments. However, we can measure the time
rep necessary to repolymerize a gel of thickness
at a polymerization rate
p after the bead was expelled from its surrounding gel, and
The time
rep corresponds also to the time necessary for the velocity to drop from its maximal value Vmax to its minimum value Vmin (see Figs. 3 and 7). The minimal velocity Vmin is thus given as a function of
rep by equating the friction and propulsion forces:
![]() | (8) |
We can use the expression for
', the time required to develop a gel of thickness
to express the minimal velocity in terms of the measurable parameters e*, D,
rep, and
':
![]() | (9) |
In practice we find that
<<
rep <
' (see Table 1) and since the ratio of
for all bead diameters studied, then
Taking all these parameters into account, we evaluate Vmin to be almost zero, again in agreement with our experimental results. The ratio
in Eq. 9 represents a characteristic velocity: under stretching conditions, if the bead velocity is greater than
the elastic force is dominant, whereas for velocities smaller than
the friction dominates (25
). The value of
can be estimated from our experimental data as follows: the minimal velocity for a bead of diameter D = 2.8 µm is Vmin = 0.082 µm/min, where
(see Fig. 2) and
(Table 1); therefore
0.015 µm/min. With Y of the order of 103104 Pa (25
,26
), the friction coefficient ß is equal to 4 x 1013 Pa s/m, or 4 pN/nm. Since the surface concentration of activating proteins is of the order of 102 mol/nm2 (see Materials and Methods, above), the value of ß is of 4 pN x s x nm1. Thus, in the slow regime motion, the tangential force exerted on average per filament on the bead is of the order of a few pN, which is quite reasonable.
| CONCLUSION |
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| ACKNOWLEDGEMENTS |
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Submitted on November 5, 2004; accepted for publication May 17, 2005.
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