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Using Polymer Modified Asphalt Emulsions in Surface Treatments A ...

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the materials handl<strong>in</strong>g and placement practicalities for modified AC-10 and A-30 asphalt<br />

b<strong>in</strong>ders.<br />

8000<br />

Viscosity (cP)<br />

6000<br />

4000<br />

2000<br />

AC-30 Base<br />

AC-10 Base<br />

0<br />

0 2 4 6 8 10<br />

SBS Weight Concentration (%)<br />

Figure 17: Viscosity as a Function of SBS Concentration (12)<br />

Serfass et al (1992) report that adequate SBS concentrations are required to ensure<br />

proper formation of a cont<strong>in</strong>uous polymer network, and that it is this network which<br />

imparts the most desirable viscoelastic properties to modified asphalt b<strong>in</strong>ders. With<strong>in</strong><br />

this context, the authors note that “adequate” is highly dependent upon asphalt<br />

compatibility, but is generally with<strong>in</strong> the range of 3% to 5% by weight of residual asphalt<br />

(18).<br />

2.3.3 Storage and Handl<strong>in</strong>g Considerations<br />

Proper storage conditions represent one of the most common problems associated with<br />

the use of PME. The mix<strong>in</strong>g processes used are complex and often proprietary, and as<br />

such, modified b<strong>in</strong>ders are generally acquired <strong>in</strong> an already-blended form from the<br />

supplier. Once batched, the mixture must be placed <strong>in</strong> a special hold<strong>in</strong>g tank that can<br />

be cont<strong>in</strong>uously agitated to prevent the phase separation problems which were noted<br />

previously and described <strong>in</strong> some detail. Temperatures dur<strong>in</strong>g storage must also be<br />

strictly controlled to prevent sett<strong>in</strong>g, premature break<strong>in</strong>g (emulsions), and/or thermal<br />

39

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