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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Poly(macromonomers), Homo- and Copolymerization 145<br />
Conventional radical polymerization usually produces polymers with a broad<br />
distribution <strong>in</strong> DP. The polymers are mixtures of the <strong>in</strong>stantaneous polymers<br />
with DP w /DP n of at least 1.5 for the term<strong>in</strong>ation by recomb<strong>in</strong>ation or 2.0 either<br />
for the term<strong>in</strong>ation by disproportionation or for the cha<strong>in</strong> transfer to small molecules.<br />
In this respect, any liv<strong>in</strong>g polymerization with rapid <strong>in</strong>itiation will afford<br />
polymers with a narrow DP distribution of the Poisson type. R<strong>in</strong>g-open<strong>in</strong>g methathesis<br />
polymerization of norbornenyl-term<strong>in</strong>ated macromonomers, 8, 15,<br />
and 16, appears promis<strong>in</strong>g <strong>in</strong> this regard [22, 23].<br />
4.2<br />
Copolymerization<br />
A number of copolymerizations <strong>in</strong>volv<strong>in</strong>g macromonomer(s) have been studied<br />
and almost <strong>in</strong>variably treated accord<strong>in</strong>g to the term<strong>in</strong>al model, Mayo-Lewis<br />
equation, or its simplified model [39]. The Mayo-Lewis equation relates the <strong>in</strong>stantaneous<br />
compositions of the monomer mixture to the copolymer composition:<br />
where d[A]/d[B] is the molar ratio of the monomers A to B <strong>in</strong>corporated <strong>in</strong>to the<br />
copolymers <strong>in</strong>stantaneously formed from the monomer mixture with the molar<br />
ratio [A]/[B], and r A and r B are the respective monomer reactivity ratios.<br />
Copolymerization between a conventional comonomer (A) and a macromonomer<br />
(B) affords a so-called graft copolymer with A as a backbone and B as statistically<br />
distributed branches, as <strong>in</strong> Fig. 1b,d. S<strong>in</strong>ce usually [A]/[B]>>1 <strong>in</strong> order<br />
to obta<strong>in</strong> a balanced composition (<strong>in</strong> weight) of backbone and branches, Eq. (3)<br />
is approximated to a simplified form:<br />
Therefore, the copolymer composition or the frequency of the branches is essentially<br />
determ<strong>in</strong>ed by the monomer composition and the monomer reactivity<br />
ratio of the comonomer.<br />
The relative reactivity of the macromonomer <strong>in</strong> copolymerization with a<br />
common comonomer, A, can be assessed by 1/r A =k AB /k AA , i.e., the rate constant<br />
of propagation of macromonomer B relative to that of the monomer A toward a<br />
common poly-A radical. In summariz<strong>in</strong>g a number of monomer reactivity ratios<br />
<strong>in</strong> solution copolymerization systems reported so far [3, 31, 40], it appears<br />
reasonable to say that the reactivities of macromonomers are similar to those of<br />
the correspond<strong>in</strong>g small monomers, i.e., they are largely determ<strong>in</strong>ed by the nature<br />
of their polymeriz<strong>in</strong>g end-group, i.e., essentially by their chemical reactivity.<br />
(3)<br />
(4)