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

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<strong>Seed</strong> <strong>and</strong> <strong>Feed</strong> <strong>Stage</strong> Agitations <strong>of</strong> BMA <strong>and</strong> NMA 363<br />

seed stages <strong>and</strong> feed stages (‘‘factor’’) was varied by varying <strong>the</strong> speed <strong>of</strong> <strong>the</strong><br />

agitator at two levels. When <strong>the</strong> values <strong>of</strong> x factors are varied at n levels, a<br />

total <strong>of</strong> n x different experiments can be performed. Thus, <strong>the</strong> latexes were<br />

prepared using all <strong>the</strong> 2 2 possible permutations <strong>of</strong> agitation speeds. No<br />

monomer pooling was observed at any stage <strong>of</strong> <strong>the</strong> reaction, when <strong>the</strong> 8 cm<br />

Rushton turbine was used. After <strong>the</strong>ir syn<strong>the</strong>sis, <strong>the</strong> latexes were characterized<br />

for <strong>the</strong> ‘‘responses’’, viz., <strong>the</strong> amount <strong>of</strong> coagulum, <strong>the</strong> particle<br />

diameter, <strong>the</strong> amount <strong>of</strong> water-soluble polymer, <strong>and</strong> <strong>the</strong> viscosity. The agitation<br />

conditions <strong>and</strong> <strong>the</strong> results are shown in Table 2.<br />

Determination <strong>of</strong> Coagulum Amount<br />

For <strong>the</strong> determination <strong>of</strong> <strong>the</strong> amount <strong>of</strong> coagulum (aggregated polymer<br />

particles), <strong>the</strong> polymer on <strong>the</strong> reactor inserts were carefully scraped,<br />

collected, washed using a sieve with 53 mm pore size, dried in an oven at<br />

75°C, <strong>and</strong> weighed. The latex was also filtered through <strong>the</strong> sieve, but <strong>the</strong><br />

amount <strong>of</strong> coagulum in <strong>the</strong> latex was negligible.<br />

Characterization <strong>of</strong> Serum-Polymer<br />

Ultracentrifugation (Beckman, L8-55M ultracentrifuge) was used to<br />

separate <strong>the</strong> aqueous phase <strong>of</strong> <strong>the</strong> latex, commonly called <strong>the</strong> serum,<br />

from <strong>the</strong> polymer particles. It was found that ultracentrifugation <strong>of</strong> <strong>the</strong><br />

latex diluted with an equal mass <strong>of</strong> water resulted in a good separation<br />

<strong>of</strong> <strong>the</strong> serum <strong>and</strong> <strong>the</strong> particles. Centrifugation was carried out at<br />

37000 rpm <strong>and</strong> 4°C, for 6 h. Let x be <strong>the</strong> mass <strong>of</strong> a sample <strong>of</strong> <strong>the</strong><br />

original latex, w, <strong>the</strong> mass <strong>of</strong> water used for dilution, <strong>and</strong> y, <strong>the</strong> mass<br />

fraction <strong>of</strong> solids in <strong>the</strong> aqueous phase <strong>of</strong> <strong>the</strong> diluted latex. The mass<br />

fraction <strong>of</strong> solids in <strong>the</strong> serum <strong>of</strong> <strong>the</strong> original latex, f ws , was calculated<br />

using Eq. 1:<br />

f ws ¼<br />

<br />

y<br />

1 y<br />

<br />

f w þ w <br />

x<br />

ð1Þ<br />

where f w is <strong>the</strong> mass fraction <strong>of</strong> water in <strong>the</strong> original latex. If f a is<br />

<strong>the</strong> mass-fraction <strong>of</strong> non-polymeric solids in <strong>the</strong> serum (SDS, NaHCO 3 ,<br />

KPS, <strong>and</strong> unreacted NMA), <strong>the</strong> mass <strong>of</strong> water-soluble polymer in <strong>the</strong><br />

serum, M wsp (based on <strong>the</strong> total mass, M tot , <strong>of</strong> <strong>the</strong> recipe) is given by:<br />

M wsp ¼ M tot ðf ws f a Þ ð2Þ

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