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A Practical Approach to Rheology and Rheometry

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Shear stress τ<br />

<strong>Rheology</strong><br />

Flow curve Viscosity curve<br />

� �<br />

0<br />

8<br />

Shear rate<br />

Log shear rate<br />

I: First New<strong>to</strong>nian range → viscosity η0 not<br />

yet dependent on shear rate.<br />

II: In this range viscosity drops as a result<br />

of molecular or particle orientation.<br />

III: Second New<strong>to</strong>nian range → viscosity η∞<br />

stays constant, independent of further increases<br />

of shear rate.<br />

Fig. 8 The shear rate dependence of pseudoplastic liquids<br />

24<br />

Log Viscosityη<br />

η 0<br />

η<br />

8<br />

I II<br />

III<br />

B. Liquids which show a dilatant flow behaviour – (Curves 3 in Fig. 6)<br />

There is one other type of a material characterized by a shear rate dependent<br />

viscosity: “dilatant” substances – or liquids which under certain conditions of<br />

stress or shear rate show a dilatant flow behaviour – increase their viscosity<br />

whenever shear rates increase. In other words, the more one tries <strong>to</strong> increase<br />

the coating speed for some PVC-plastisols <strong>to</strong> coat a fabric substrate, the stiffer<br />

the coating material becomes. The resistance <strong>to</strong> flow may become so high that<br />

the fabric is <strong>to</strong>rn or even the rolls of the coating calender are broken.<br />

Dilatant flow behavior is found for example in highly concentrated suspensions<br />

in which solid particles such as emulsion-PVC are mixed with liquids such as<br />

plasticizers <strong>to</strong> form plastisols. The particles are densely packed <strong>and</strong> the<br />

amount of plasticizer added is just sufficient <strong>to</strong> fill the void between the particles.<br />

At rest or at low coating speeds the plasticizer fully lubricates the particle<br />

surfaces <strong>and</strong> thus allows an easy positional change of particles when forces<br />

are applied: this suspension behaves as a liquid at low shear rates. At higher<br />

shear rates, particles will wedge others apart causing general volume increases.<br />

At this stage the plasticizer’s share of the <strong>to</strong>tal plastisol volume decreases.<br />

Since the plasticizer is no longer sufficient <strong>to</strong> fill all voids <strong>and</strong> <strong>to</strong> keep<br />

the PVC-particle surfaces fully lubricated, the plastisol becomes more viscous.<br />

Dilatancy in liquids is rare. Inasmuch as this flow behavior most likely complicates<br />

production conditions, it is often wise <strong>to</strong> reformulate the recipe in order<br />

<strong>to</strong> reduce dilatancy.<br />

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