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Viscosity and moving dislocations in colloidal crystals
M. Jorand, A.-J. Koch, F. Rothen
To cite this version:
M. Jorand, A.-J. Koch, F. Rothen. Viscosity and moving dislocations in colloidal crystals. Journal de
Physique, 1986, 47 (2), pp.217-227. �10.1051/jphys:01986004702021700�. �jpa-00210198�
Viscosity and moving dislocations in colloidal crystals
M. Jorand, A.-J. Koch and F. Rothen
Institut de Physique Expérimentale, Université de Lausanne, 1015 Lausanne-Dorigny, Switzerland (Reçu le 2 mai 1985, accepté sous forme définitive le 8 octobre 1985)
Résumé.
2014Nous étudions le mouvement d’une dislocation vis dans les cristaux colloidaux et appliquons ce
calcul à un écoulement de Couette. On en déduit une relation analytique pour la viscosité macroscopique ~ en
fonction d’une viscosité intermédiaire ~, de la densité n de dislocation et du cisaillement. Une modification des contraintes internes au voisinage du coeur de la dislocation, lorsque sa vitesse change, entraîne une diminution de ~ lorsque le cisaillement externe augmente.
Abstract.
2014We study the motion of a screw dislocation in colloidal crystals and apply the results to a Couette flow. We get an analytic expression for the macroscopic viscosity n as a function of an intermediate viscosity ~,
of the dislocation density n and of the shear. A modification of internal stress near the dislocation core, when its velocity changes, implies a diminution of ~ when the external shear rises.
Classification Physics Abstracts
47.55K - 82.70
-61.70G
Introduction.
There has been a great deal of interest in the physics
of colloidal suspensions [1] and among them, the colloidal crystals present very peculiar physical pro-
perties such as phase transitions under shear [2].
Colloidal crystals [2] (c.c.) are monodisperse colloids
in which the colloidal particles, through dissociation reaction in water, have strong electric charge. (Ze N
1000 e for a typical diameter ø ~ 0.1 pm). Under
well defined conditions (density of particles, charge,.
electrolyte concentration), the most interesting phe-
nomenon resulting from the Coulomb interaction between particles is their ordering into a crystalline lattice with a typical lattice constant a N 1 J.1m.
As any solid, these c.c. have a finite elastic modulus
(E) whose order of magnitude can be estimated [3]
by multiplying U, the energy of interaction between two particles by n, the density of particles :
For a charge Ze - 10’ e and an interparticle dis-
tance a - 1 pm, the Coulomb interaction
- er gives
U N 10 eV with a dielectric constant c - 100. One finds : E - 1 a3 U - 1 dyn Y cm-’ while in a usual
solid E - 1012 dyn cm- 2.
The above estimate has been confirmed by various experiments [4-6]. Such a low value of the elastic modulus will have very interesting consequences,
especially for the flow and melting of these colloidal
crystals.
In this paper, we consider a model of dislocation motions to calculate the behaviour of the macrosco-
pic viscosity of c.c. flowing under applied shear. In
the first section we review the basic experiments studying the flow properties of c.c. ; in the second sec-
tion the model is presented and discussed and in the
third part, numerical results are compared to the experimental results.
1. Experimental review.
The most appropriate geometry to study flow pro-
perties of c.c. is the Couette flow (Fig. 1) (two coaxial cylinders with different angular velocities). In this geometry, Mitaku et al. [7] have measured the shear
rate Vij as a function of the shear stress Gij for the flow of ordered c.c. Typical curves are given in references
[7] and [8] but the qualitative behaviour is reproduced
here (Fig. 2).
The main result is that, in the ordered state, the c.c.
behave like a non-Newtonian fluid, whose viscosity
diminishes with increasing shear (pseudo-plactic
fluid [9]).
If we consider a stress-strain relation [7] of the form : G r8
=nVre + K, where K is the yield stress, from the measurements of Mitaku et al. we can draw the macroscopic viscosity -q as a function of the angular velocity w of the inner cylinder, the outer being at
rest (this is shown in Fig. 3).
Article published online by EDP Sciences and available at http://dx.doi.org/10.1051/jphys:01986004702021700
Fig. 1.
-Geometry of a Couette flow experiment.
shear stress (dyn.cni 2)
Fig. 3.
-Diagram of the macroscopic viscosity t-I vs.
angular velocity w (w ~ shear rate).
In the experiments [7,8], V,,, > - 6 co (see Eq. (36)).
At low shear rate (cm - 10-3 s-1) this viscosity n is
four orders of magnitude greater than that of water
(17H,O - 10- 2 p) and decreases to - 10 p for m - 10-1 s-1.
For much higher shear rates, Lindsay and Chaikin
[10] observe a shear melting transition between ordered and disordered c.c. For their sample this occurs at a
critical shear rate ( V’,Io > - 60 s- l. The viscosity is
then of the order 5 x 10- 2 p and above this melting
transition the colloid is non-Newtonian with a vis-
cosity ranging (1-10) ’ 10-1 p.
These results are in qualitative agreement with the results obtained on polymeric fluids [11], but from a
theoretical point of view, a statistical approach in
our case is more difficult since we must add a Coulomb interaction between particles.
Another interesting experiment has been perform-
ed by Chaikin et al. [ 12] in a Couette geometry with
a very small gap between the cylinders.
Under low shear rate, the ordered c.c. flow and this flow can be described by dislocation motion.
Indeed, in this experiment the dislocations form walls
(Fig. 4) and these have been observed through the modifying light scattering properties of the sample.
(The existence of these walls is not surprising since they correspond to a stable equilibrium of grain boundaries) (see for instance Ref. [13]).
q Fig 2.
-Qualitative behaviour of shear rate vs. shear stress
(from paper by Mitaku et al. [7] Fig. 5, 130uM in kCl
concentration). Dotted line : Newtonian fluid; continuous
line : ordered colloidal crystals; main characteristics of the
sample : volume fraction - 12 % ; shear modulus
p - 102 dyn cm- 2 ; lattice constant a - 3 x 10- 5 cm.
Fig. 4.
-Periodic stripes of grain boundaries (wall edge dislocations) in Couette flow experiment [12] (a - 100).
Another experiment of shear-induced melting by
Ackerson and Clark [14] has been interpreted as the slipping of two-dimensional hcp layers but in this work we assume that the whole flow is due to disloca- tions. Moreover, we restrict ourselves to very low shear rate regime and from the above two experiments
we calculate I by studying the dislocation motion in this regime.
2. Theoretical approach.
We first present the general idea leading to an esti-
mate of the macroscopic viscosity of these c.c., then
we discuss the motion of a single dislocation through
the theoretical description of the c.c. and results introduce these in the general scheme of the first part in order to calculate this viscosity.
2.1 How To CALCULATE fi. - From now on, we describe our c.c. in the Couette geometry and, as figure 4 suggests, we treat straight dislocations whose
axes are parallel to the z-axis (Fig. 1). So we have a
two-dimensional problem.
There are two ways to discuss the motion of c.c.
under shear flow :
1) The macroscopic point of view treats the c.c.
like a fluid of macroscopic viscosity I without refer-
ring to what happens to the structure inside this fluid. As we saw in section 1, the order of magnitude of i ranges from 103 p to 10-2 p, n being shear depen-
dent
2) The intermediate point of view considers a
scale length on the order of the interdislocation dis- tance. At such a scale, we treat discrete dislocations in
a continuous elastic medium. Submitted to an exter- nal shear, the dislocations move and their displace-
ment fields induce hydrodynamical currents which are
characterized by an intermediate viscosity q.
For an isolated moving dislocation, we have a
small local displacement of the elastic medium and the
viscosity associated with this motion can be compar- ed to the viscosity appearing in shear waves experi-
ments [5]. For a typical sample (u - 102 dyn cm-’,
a - 3 x 10- 5 cm) we get 11 ’" 0.1 p.
One could describe the c.c. in a third way by consi- dering lengths smaller than a and starting from the
fundamental level of a pure liquid with a viscosity
110 ’" 11820 ’" 10-2 p.
Then we have three scale lengths and three kinds of viscosity and we ought to start from 110 to arrive at to have a continuous description of these c.c. But
in this work, we will skip the first step and just find
a relation between n and 11.
For this purpose we evaluate the power dissipated by the Couette flow through the two descriptions
and equal the final results. Let P
=P(w, -j7 be the dissipated power in the macroscopic description and Pi(V’, n) the power dissipated by an individual mov-
ing dislocation (Yo is the dislocation velocity). More-
over, if we assume that there is no hydrodynamic inter-
action between dislocations [15], we can write :
If we still find a relation between the dislocation velo- cities and the shear rate, we will get from (1) a relation
for this macroscopic viscosity :
for a given sample and geometry.
2.2 THEORETICAL DESCRIPTION OF c.c.
-As figure 4
suggests [12], we ought to consider edge dislocations but these are much more difficult to treat than screw
dislocations, since they contain a non-zero displace-
ment divergence which describes compression or
dilatation around them. However, by symmetry, this main difference disappears if we sum the contri- butions of all dislocations in the wall [16], and for
and order of magnitude, the power dissipated by a moving wall of N edge dislocations will be obtained
by summing this power over N uniformly distributed
screw dislocations submitted to the same constraint.
(These screw dislocations do not reproduce the geo- metry of the c.c. but this is not important for evaluating
the power dissipated by their motion).
2.2. 1 Displacement dislocation.
-If we field confine around our c.c. a moving between screw two infinite parallel plates and consider the ideal case of
only one screw dislocation in a perfect surrounding
medium (Fig. 5).
In Cartesian coordinates (x, y, z), we take the Bur- gers vector b
=(0, 0, b) with b - a ; the direction of the dislocation is defined by a unit vector = (0, 0,
-
1) tangent to the dislocation line : then we-consider
a left handed screw dislocation [13] (b · 0).
Fig. 5.
-Moving dislocation between parallel plates 4
=sense of the dislocation
b - 0 : left handed screw
b
=Burgers vector dislocation.
If we move uniformly the upper and lower plates in
-
z and + z directions respectively, the resulting cons-
tant shear induces the motion of the dislocation in the
plane (x, z) at a constant velocity Yo and in the + x
direction [13, § 3, 6].
The problem now is to find the displacement field
around such a dislocation and for this we need the
hydro dynamical equations describing the dynamics
of colloidal crystals.
These have been presented elsewhere [17] and for
an incompressible deformation (as it is for a screw
dislocation) and slow motion, the equation of motion
has the following form :
where U is the local displacement of the continuous elastic medium,
p is the shear modulus [16, 5], and ’1 is an effective
transverse viscosity [18, 5] p being an average density
of the suspension ( N 1 g em - 3).
The velocity V
=au/at describes the hydrodyna-
mical currents induced by the motion of the disloca-
tion, and since these currents are characterized by a viscosity ’1, the power dissipated by them is sim-
ply [18] :
where
For the particular problem we now consider, we look
for a solution of (2) .in the form
where Vo is the dislocation velocity.
Introducing (5) into (2), we have :
or
with
is the velocity of shear waves [16]
For motions such that Vo CS, we have /32 1
and we can neglect the inertia term of (7), which is simply written
Through this simplification, we donnot consider the energy radiated by the dislocation as it moves [19],
but naturally we ought to verify the above assumption
for the experiment we consider.
From the relation V
=aU and equation (5), t ) we can
still write the power dissipated as :
We can now look for a solution of (12) but since U(x’, y) characterized the displacement held around
a dislocation, we must add the boundary condi-
tion [13] :
where the integral is taken over a circle of radius r
around the dislocation axis. (We do not now consider
the exact form of f(r)).
From equation (14), we see that Uz is a multivalued function but for mathematical simplicity, we can also
consider it as a uniform but discontinuous function
[16, § 27].
Suppose there is a discontinuity on the negative
x-axis. The boundary condition will be written [13] :
lim Uz(x’, s) - Uz(x’, - s)
=6Uz = b8( - x’)f(x’)
e-0
with
For a usual crystal [13], f(x’)
=1. But for c.c., the motion of a dislocation is slackened by the visco- sity of the liquid which slows down the displacements
of the elastic medium. One can study this more quanti- tatively by considering the dynamics of the disconti- nuity ðUz appearing behind a moving screw dis-
location. Let us decompose 6 U_, according to figure 5a
Fig. 5a. - Discontinuity ð Uz given by a classical part ð U.’ and an additional effect 6 Uz due to the viscosity.
where 6Ufl is the discontinuity appearing behind a
« classical » screw dislocation : 6 U,,,o
=bO(Vo t
-x), 6U/ is a correction of the discontinuity due to the viscosity, and 6 U,, and 6 U/ should satisfy the following
conditions
a) if the dislocation velocity Vo goes to zero,
ðUz1 should decrease since the viscosity effect decreases;
b) far behind the dislocation (where all relative displacements of the elastic medium have been
damped) one has ðUz1
=0;
c) in front of the dislocation (where x - Vo t > 0) ðUz
=0.
The simplest nontrivial equation one can imagine
to describe the dynamics of ð U zl is :
T is a relaxation time which can be roughly estimated
with the help of the two effects in competition : the elasticity and the viscosity
The solution of (17) which satisfies all the above- mentioned requirements is :
(the singularity b(Yo t
-x) appearing in (17) is not
relevant since it is contained in the dislocation core).
The discontinuity (16) is then given by :
where the length ’1" 0 = a is the interaction range of the liquid on the dislocation. From now on one
writes x for x - Vo t and (20) writes
Then we have to solve equation (12) with boundary
condition (21), this exercice is done in Appendix A, and we get an exact solution :
where E1 z) is the exponential-integral [20] defined by :
with the properties :
and for z large :
(Fig. 6 describes the effects of this motion and the
discontinuity (21) of Uz).
Fig. 6.
-Draft of a moving screw dislocation, showing
a vanishing discontinuity of the displacement field Uz at the origin (dotted discontinuity
=pure elastic case). Two nearly points A(xo, yo + s) and B(xo, Yo - c) after the passing of the dislocation will be at A’(xo, yo + a,
-b/2)
and B’(xo, Yo - B, b/2) with opposite velocities. Summing
this effect over all dislocations reproduces the flow of
c.c. under constant shear.
From (23) we see that, within the limit a - 0, equation (22) gives :
a standard result in the usual elasticity theory [ 13].
From (22) we get an expression for V z as :
with
This velocity describes the hydrodynamic currents
Fig. 6a, b.
-Comparison of the discontinuity of Uz in
usual crystal (a) and colloidal crystal (b) (lattice spacing :
b
=10-4 em).
I
Fig. 6c.
-Draft showing the discontinuity of Yz
=ðtUz
on x 0.
induced by dislocation motion and as figure 6c shows, Vz is discontinuous on y
=0 for x 0.
But this discontinuity is meaningless in a discrete
lattice and we interpret it as a strong change in velocity over a length b.
If we define Vz such that
where m=x+i .b
where ffi = x a + i 2 b oc oc IX
Then we have a continuous velocity giving a
viscous stress
were 110 is the viscosity of the fluid in a band of width b and it is thus equal to 11820 ’" 10-2 p.
Since , b - 110’ we have (11 ’" 62 and for sim p li-
a
city, we then assume
on the whole domain and forget the singularity on a .
2.2.2 Power dissipated by a moving dislocation. -
Introducing (24) into (13), we find the hydrodynamic
power dissipated by a moving screw dislocation :
and L is the dislocation length.
The lower integration bound corresponds to the
extent of the core of the dislocation and we can
determine the curve C(xc, Yc) by assuming that
inside it, the elastic stress Q is greater than a critical
stress a,. We assume this critical stress to correspond
to the « theoretical elastic limit » [21] whose order of magnitude is
Introducing (22) into the expression of the elastic
stress
we get
and from this the curve C(xc, Yc) is given by
with
For a vanishing velocity Yo we find a circular core
whose radius rc ’" b is the admitted classical value for a pure elastic medium. Some curves C(xc, Yc)
have been drawn in figure 7 for various velocities
Fig. 7.
-Core section of a moving dislocation at various velocities [cm S-1].
and we see that above a given value, the core is vanish- ingly small; yet it doesnot make sense to consider
a core with r, b, since we treat the elastic medium
as a continuum. Therefore it seems natural at this
point to add a restriction on C(xc’ Yc) by requiring :
Another contribution to this dissipated power comes from the phonon interaction and periodic structure
of the elastic medium as in any usual crystal. This
contribution has been estimated by Leibfried [22]
and Lothe [23] and an order of magnitude is given
in reference [ 13], § 7 :
where WT is the density of thermal vibrational energy
An estimate of (25) within the limit a -+ 0 gives :
and the ratio
r -of --
r L-
- -105.
and the ratio - 105 .
P’ 4 1t pb x 10-
’~
As a consequence, the power dissipated by a moving
dislocation is essentially given by Phya..
2.3 MACROSCOPIC DESCRIPTION OF c.c.
-As we said in section 2.1, we will consider the c.c. like a fluid of viscosity I submitted to a Couette flow. The
angular velocity of the inner cylinder is w and since
RZ R1 1 (Fig. 1) in the experiment of Mitaku R1
et al. [7, 8] we can suppose a constant shear between
cylinders and thus for a given w, we assume that I is
constant.
We can then solve the Navier-Stokes equations [18]
for such a flow, and assuming cylindrical symmetry and azimuthal flow, we find the well-known solution
2 / n2B
From (32) we get the macroscopic dissipated po-
wer [18]
Before comparing (25) and (33) we must find a rela-
tion between the angular velocity m and dislocation
velocity V o.
In the limit of a plane motion (Ri, R2 -> oo and R2 - R,
=Cte) we find
dislocation density . (
For the cylindrical case with R2 - Ri 1, we can R
write :
where n is the mean dislocation density
As said in section 1, we consider very low shear rates
and consequently we can assume that the density of
dislocations is constant. This is certainly not right
when we approach the critical shear rate of melting
transition [10] but is fairly correct in our case. So equation (36) means that, for a given w, the disloca- tions have the same mean velocity Vo, which is rather
j? 2013 R1
correct since R2 - Ri R 1 1. (W e are near the plane
case.) From this, the result (25) for plane motion will be a good approximation of the cylindrical problem.
2.4 DETERMINATION OF THE MACROSCOPIC VISCOSITY.
-
From the above discussion, we introduce (25)
and (33) into equation (1) and write :
or
with
If we introduce x’ = x and y’ - y , we get
a a
From (39) we see that the inferior integration bound
determines the behaviour of ti. Within the limit of small velocities such as b > a 1, and for the limiting plane case, we find
in perfect agreement with our previous result [24].
With in this limit, the viscosity I does not depend
on the shear rate m but decreases as the dislocation
density increases, since the flow is facilitated.
2. 5 DISCUSSION.
-We can understand the behaviour
of I qualitatively by observing from (37)
For small velocities Vo with a b, the characteristic
length is b and we have
So in this domain ?-I - - 172and nb we find the result (40).
But for velocities such that ex >> b(VO >> 10 -2 cm s- 1) the characteristic length is ex and we have
which implies
giving a decreasing of I for increasing shear, since - Vol
In order to compare our result quantitatively with
the experimental one, we performed the integral (39) numerically. The result is presented in the third
section.
3. Numerical results.
Our purpose is not to fit the experimental results with
our calculation, since we do not exactly know the
values of the physical parameters (appearing in
Eq. (39)) characterizing a given sample. We have
nevertheless considered Mitaku’s experiments [7, 8],
to fix these values; this provides an order of magnitude.
If we consider Chaikin’s experiment [12], the density
of dislocations is given by the minimum value neces-
sary to reproduce the geometry of the sample. We
then get [13] :
With this value of n, we can estimate the dislocation
velocity through equation (35) with Vr8 )max ~ 10-1 s-1 and find Võax ’" 10-1 cm s-1.
This is much smaller than the sound velocity
and vindicates the simplification of equation (7).
We have plotted the theoretical (continuous line)
and experimental (dotted line) values of I as a func-
tion of w, this is shown in figure 8.
As in the experiment, we observe a continuous
decrease of In for increasing co. For m 10-3 s-1,
the viscosity is close to a constant value given by equation (40) (t-l - 250 p) and it decreases to tj - 3 p for w - 10-1 S-1.
As said above, the difference in magnitude is not significant. It is more instructive to consider the shear dependence of the viscosity and we easily see
a disagreement on this point.
For the experimental curve, we have a power law in the form :
with d - 0.75 for the reported experiment, while for
Fig. 8.
-Comparison of experimental (dotted line) and
theoretical (continuous line) results of 1-7 vs. co. Experimental
value of the parameters [8] :
n 11
the theoretical curve, we have a logarithmic depen-
dence :
for
and
This main difference between experimental and theo-
retical results may be explained by dimensionality
effects. By computer simulation [11] of non-Newto- nian simple fluids undergoing planar Couette flow,
it appears that in 2-dim. the viscosity of these fluids
is given by q(y)
= -A log (By) where y is the shear rate, while the result in 3-dim. is
But our theoretical approach of the problem is 2-
dimensional since we considered straight parallel
dislocations and we must not be surprised by this logarithmic dependence.
4. Concluding remarks.
If the quantitative disagreement between experiment
and theory is really due to dimensional effects, our
task is quite hopeless, due to the great mathematical difficulties to treat 3-dimensional dislocations. To
improve our results the first thing we could do is to
consider straight edge dislocations (as they are really)
but we are convinced that the order of magnitude will
not change. In the same way the assumption of the
dislocations independence seems to be correct for
such a density (in a wall of edge dislocations [12],
their separation is
-10 b [15]), but if we decrease
the radius of cylinders, the density rises and the hydro- dynamic interaction between dislocations would have
important effects.
Another way to improve our results would be to
consider a varying density of dislocations but, as said
in section 2. 3, this does not seem to be right for such
a low shear rate. Whatever the detail of the model
developed here, the flow of ordered suspensions in
terms of the dislocation motion gives interesting
results.
The main point in this work is related to this length
a = ’1 V 0 which for a > b implies a deep change in
JL
the velocity dependence y of the viscous strain - yo a
around the dislocation axis by reference to the quasi-
static case - b V0. As a direct consequence, q
’we observe a decrease of the macroscopic viscosity as the
shear raises. It would be interesting to consider the behaviour of c.c. near shear melting by extending this
model to the consideration of higher shear rates, with a varying density of dislocations.
Acknowledgments.
We are indebted to W. Benoit for a fruitful discussion
on the dislocation theory and we thank B. Pansu, E. Dubois-Violette and P. Pieranski for their helpful
comments.
We thank the referees for their instructive remarks.
Appendix A.
We have to solve equation (12)
where Uz is a uniform but discontinuous function on the negative x-axis. It must then satisfy the boundary
condition (21) :
with
Following Landau’s method (16, § 27), since Uz is discontinuous, its derivatives and then the stress aij
are singular. But physically, it is meaningless to have
such singularities of Uij and in order to cancel them,
we add a fictitious force f(sing.) such as
From (A. 1) we have
with
where
6 (y) is the Dirac distribution . The singular part of a,j is then given by
with a singular force
We now introduce (A. 7) in (A. 3) to get with (A. 4)
We can solve (A. 8) by introducing Green’s function
G(x, y) satisfying
.