142 Advances in Polymer Science Editorial Board: A. Abe. A.-C ...
142 Advances in Polymer Science Editorial Board: A. Abe. A.-C ...
142 Advances in Polymer Science Editorial Board: A. Abe. A.-C ...
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164 K. Ito, S. Kawaguchi<br />
solvent. (2) Accompanied by the decomposition of the <strong>in</strong>itiator, l<strong>in</strong>ear oligomers,<br />
polymers, and graft copolymers are all produced by polymerization <strong>in</strong> the<br />
cont<strong>in</strong>uous phase. The solubility of these polymers is a function of their MW<br />
and the composition of the graft copolymer. <strong>Polymer</strong>s with a MW larger than a<br />
certa<strong>in</strong> critical value precipitate and beg<strong>in</strong> to coagulate to form unstable particles.<br />
(3) These particles coagulate on contact, and the coagulation among them<br />
cont<strong>in</strong>ues until sterically stabilized particles form. (4) This po<strong>in</strong>t is referred to<br />
as the critical po<strong>in</strong>t, and it occurs when all of the particles of <strong>in</strong>terest conta<strong>in</strong> sufficient<br />
stabilizer polymer cha<strong>in</strong>s on the surface to provide colloidal stability<br />
[112–114].<br />
After this po<strong>in</strong>t, particles grow both by diffusive capture of oligomers and coagulation<br />
of very small yet unstable particles (nuclei, precursors) produced <strong>in</strong><br />
the cont<strong>in</strong>uous phase and by polymerization of the monomer occluded with<strong>in</strong><br />
the particle. The total number of such sterically-stabilized particles rema<strong>in</strong>s<br />
constant so that their size is only a function of amount of polymers produced.<br />
The particle size is determ<strong>in</strong>ed at the critical po<strong>in</strong>t by the amount of polymers<br />
produced at that po<strong>in</strong>t. In the discussion that follows, one uses the term q to describe<br />
the fractional conversion of monomer to polymer (0�q�1), and q D to describe<br />
the correspond<strong>in</strong>g conversion of macromonomer. The weight (W M <strong>in</strong> g/l)<br />
of the monomer polymerized at any po<strong>in</strong>t <strong>in</strong> the reaction is def<strong>in</strong>ed as<br />
(19)<br />
Here, W Mo is the weight of monomer <strong>in</strong> the reactants; R is the radius (cm) of<br />
the particle occupied by the polymer cha<strong>in</strong>s only, N is the total number of particles<br />
per liter, and r is their density.<br />
The surface area per sterically-stabilized particle is determ<strong>in</strong>ed by the surface<br />
area (S) occupied by a macromonomer cha<strong>in</strong> times the number (n') of these<br />
cha<strong>in</strong>s grafted onto the surface.<br />
(20)<br />
(21)<br />
W Do is the weight (<strong>in</strong> g/l) of macromonomer <strong>in</strong> the reactants, N A is<br />
Avogadro's number, and M D is the molecular weight of the macromonomer.<br />
From Eqs. (19)–(21), one can obta<strong>in</strong> a universal relationship between the particle<br />
radius and the extent of polymerization for sterically stabilized particles:<br />
(22)<br />
At the critical po<strong>in</strong>t, sterically stabilized particles are formed, and coalescence<br />
between similar-sized particles is term<strong>in</strong>ated. At this po<strong>in</strong>t one has R=