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Relative Importance of the Effects of Seed and Feed Stage ...

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376 Krishnan et al.<br />

CONCLUSIONS<br />

Agitation has a strong effect on <strong>the</strong> properties <strong>of</strong> <strong>the</strong> latex prepared by<br />

emulsion polymerization. More particles are nucleated under a higher<br />

agitation speed. This observation is consistent with <strong>the</strong> mechanism <strong>of</strong><br />

interfacial particle nucleation (Varela de la Rosa, 1991), wherein <strong>the</strong> shear<br />

stress generated by <strong>the</strong> agitation results in <strong>the</strong> formation <strong>of</strong> minidroplets<br />

near <strong>the</strong> surface <strong>of</strong> <strong>the</strong> monomer droplets, <strong>and</strong> polymer particles are formed<br />

by <strong>the</strong> nucleation <strong>of</strong> <strong>the</strong>se minidroplets. Although <strong>the</strong> reactions were carried<br />

out under a constant flow <strong>of</strong> nitrogen through <strong>the</strong> reactor, trace amounts <strong>of</strong><br />

oxygen impurity in <strong>the</strong> reactor headspace can also result in a higher particle<br />

concentration at a higher agitation speed (Krishnan, 2002).<br />

The main factor influencing <strong>the</strong> amount <strong>of</strong> water-soluble solids in<br />

<strong>the</strong> latex serum is <strong>the</strong> number <strong>of</strong> particles produced at <strong>the</strong> end <strong>of</strong> <strong>the</strong> seeding<br />

stage. The greater <strong>the</strong> number <strong>of</strong> particles, <strong>the</strong> lower was <strong>the</strong> amount <strong>of</strong> watersoluble<br />

polymer. More NMA monomer copolymerizes with BMA in <strong>the</strong><br />

polymer particles when <strong>the</strong> number <strong>of</strong> particles is higher. The agitation<br />

during <strong>the</strong> feed stage did not have a significant effect unless <strong>the</strong><br />

emulsification <strong>of</strong> <strong>the</strong> added BMA monomer was poor <strong>and</strong> pooling occurred<br />

(as with <strong>the</strong> 4 cm Rushton turbine). The low viscosity <strong>of</strong> <strong>the</strong> latex, <strong>and</strong> <strong>the</strong><br />

good mixing with <strong>the</strong> 8 cm agitator even at 150 rpm, were <strong>the</strong> reasons for no<br />

effect <strong>of</strong> <strong>the</strong> feed stage agitation on <strong>the</strong> water-soluble polymer formation.<br />

As expected, <strong>the</strong> amount <strong>of</strong> coagulum increased with <strong>the</strong> agitation<br />

intensity. Almost all coagulum formed during <strong>the</strong> reaction was on <strong>the</strong><br />

agitator blades, baffle, etc. If <strong>the</strong> trailing vortices behind <strong>the</strong> agitator blades<br />

are <strong>the</strong> sites <strong>of</strong> coagulum formation, <strong>the</strong>n <strong>the</strong> amount <strong>of</strong> coagulum is<br />

expected to scale with <strong>the</strong> Reynolds number.<br />

The viscosity <strong>of</strong> <strong>the</strong> final latex was more sensitive to <strong>the</strong> number <strong>of</strong><br />

polymer particles than <strong>the</strong> amount <strong>of</strong> water-soluble polymer. The latex<br />

viscosity was higher when <strong>the</strong> latexes were prepared using a higher agitation<br />

speed during <strong>the</strong> seed stage <strong>and</strong> <strong>the</strong>reby contained more polymer particles.<br />

ACKNOWLEDGMENTS<br />

The help <strong>of</strong> Mr. William Anderson with NMR data acquisition <strong>and</strong><br />

interpretation, <strong>and</strong> <strong>the</strong> financial support from <strong>the</strong> Emulsion Polymers<br />

Liaison Program is greatly appreciated.<br />

REFERENCES<br />

Ali, S. I., Zollars, R. L. (1987). Changes in coagulum configuration resulting<br />

from shear-induced coagulation. J. Colloid Interface Sci. 117(2):425–430.

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