Difference between revisions of "Spatial cooperativity in soft glassy flows"

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The authors test flow in two main geometries: shear planar flow in a wide gap Couette cell, and pressure driven planar flow in a narrow microchannel (tens of hundreds micrometers in width).  The substance tested was an emulsion of silicone droplets (6.5um in diameter) in a glycerine-water mixture.  The local flow curves, which relate the local shear stress <math>\sigma</math> to the local shear rate <math>\dot{\gamma}</math>, are obtained from the measured velocity profiles of both geometries.  Figure 1 shows the results for the wide-gap Couette cell, and Figure 2 shows the results for the narrow microchannel.  Evidently, the flow curve is highly dependent on the geometry.  In the wide-gap case, the curve follows the Herschel-Bulkley model.  However, in the microchannel setup, the data does not follow a single rheological curve.  The finite-size effect in the microchannel setup which did not appear in the wide-gap setup suggests that there are extended spatial correlations in the system.
 
The authors test flow in two main geometries: shear planar flow in a wide gap Couette cell, and pressure driven planar flow in a narrow microchannel (tens of hundreds micrometers in width).  The substance tested was an emulsion of silicone droplets (6.5um in diameter) in a glycerine-water mixture.  The local flow curves, which relate the local shear stress <math>\sigma</math> to the local shear rate <math>\dot{\gamma}</math>, are obtained from the measured velocity profiles of both geometries.  Figure 1 shows the results for the wide-gap Couette cell, and Figure 2 shows the results for the narrow microchannel.  Evidently, the flow curve is highly dependent on the geometry.  In the wide-gap case, the curve follows the Herschel-Bulkley model.  However, in the microchannel setup, the data does not follow a single rheological curve.  The finite-size effect in the microchannel setup which did not appear in the wide-gap setup suggests that there are extended spatial correlations in the system.
  
The authors checked that the change in rheology is not caused by a structural change in the emulsion, nor a change in density, nor boundary effects.  In order to explain this finite-size effect, they developed a model considering the plastic rearrangements that occur in concentrated emulsions.  Localized plastic events induce a non-local, long-range elastic relaxation of the stress over the system.
+
The authors checked that the change in rheology is not caused by a structural change in the emulsion, nor a change in density, nor boundary effects.  In order to explain this finite-size effect, they developed a model considering the plastic rearrangements that occur in concentrated emulsions.  In Conceptually, localized plastic events induce a non-local, long-range elastic relaxation of the stress over the system. The rate of plastic rearrangements <math>v</math> is equivalent to a fluidity <math>f</math> defined as <math>\sigma = (1/f)\dot{\gamma}</math>.  In the absence of non-local effects, the fluidity reduces to the bulk fluidity <math>f_bulk = \dot{\gamma}/\sigma_bulk</math>, but to take into account the non-local effects, the fluidity is assumed to be of the form
 +
 
 +
<math>f(z)=f_bulk+\xi^2 \frac{\partial^2f(z), \partial^2 z</math>.
 +
 
 +
In the above, <math>\xi</math> denotes a "flow cooperativity length."  This equation was solved numerically using appropriate boundary conditions.  Surprisingly,

Revision as of 07:47, 6 December 2009

Reference

Goyon, J., Colin, A., Ovarlez, G., Ajdari, A., Bocquet, L., Nature 454 (2008).

Keywords

spatial cooperativity, glass, velocity profile, shear stress, shear strain, Couette cell, Herschel-Bulkley model

Summary

Figure 1.
Figure 2.

A general feature of glassy materials is a strong nonlinear flow rule relating stress and strain. This feature is no well-documented and poorly understood. Many have tried to understand the glass transition by studying the dynamical heterogeneities in glass-forming materials, but how these heterogeneities affect flow remains unclear. Using a local velocity measurement technique, the authors study the local flow of a film of confined glassy material.

The authors test flow in two main geometries: shear planar flow in a wide gap Couette cell, and pressure driven planar flow in a narrow microchannel (tens of hundreds micrometers in width). The substance tested was an emulsion of silicone droplets (6.5um in diameter) in a glycerine-water mixture. The local flow curves, which relate the local shear stress <math>\sigma</math> to the local shear rate <math>\dot{\gamma}</math>, are obtained from the measured velocity profiles of both geometries. Figure 1 shows the results for the wide-gap Couette cell, and Figure 2 shows the results for the narrow microchannel. Evidently, the flow curve is highly dependent on the geometry. In the wide-gap case, the curve follows the Herschel-Bulkley model. However, in the microchannel setup, the data does not follow a single rheological curve. The finite-size effect in the microchannel setup which did not appear in the wide-gap setup suggests that there are extended spatial correlations in the system.

The authors checked that the change in rheology is not caused by a structural change in the emulsion, nor a change in density, nor boundary effects. In order to explain this finite-size effect, they developed a model considering the plastic rearrangements that occur in concentrated emulsions. In Conceptually, localized plastic events induce a non-local, long-range elastic relaxation of the stress over the system. The rate of plastic rearrangements <math>v</math> is equivalent to a fluidity <math>f</math> defined as <math>\sigma = (1/f)\dot{\gamma}</math>. In the absence of non-local effects, the fluidity reduces to the bulk fluidity <math>f_bulk = \dot{\gamma}/\sigma_bulk</math>, but to take into account the non-local effects, the fluidity is assumed to be of the form

<math>f(z)=f_bulk+\xi^2 \frac{\partial^2f(z), \partial^2 z</math>.

In the above, <math>\xi</math> denotes a "flow cooperativity length." This equation was solved numerically using appropriate boundary conditions. Surprisingly,