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Handbook of Size Exclusion Chromatography and Related ...

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Scheme 1<br />

Usually, a nitroxide acts as the counter-radical X*. TEMPO (2,2,6,6tetramethylpiperidine<br />

nitroxide) <strong>and</strong> SG1 (N-tertiobutyl-1-diethylphosphono-2,<br />

2-dimethylpropyl nitroxide) are among the agents commonly used in CRP.<br />

An extensive literature exists on the theoretical (35) <strong>and</strong> applied aspects <strong>of</strong> CRP<br />

(36–39).<br />

ACOMP was adapted to CRP monitoring for the SG1 controlled, bulk<br />

polymerization <strong>of</strong> butyl acrylate (40). A high-pressure mixing scheme was used to<br />

deal with the high reactor viscosities. The monomer conversion kinetics closely<br />

resembled a first-order process, <strong>and</strong> Mw increased linearly with f , although the initial<br />

Mw is finite, not zero, as <strong>of</strong>ten reported. GPC sampling during the reactions showed<br />

that, as in anionic polymerization, the polydispersity decreases during the CRP.<br />

2.1.5 Copolymerization<br />

There are many ways <strong>of</strong> producing copolymers, including free <strong>and</strong> controlled<br />

radical copolymerization (41). Average sequence lengths <strong>of</strong> a comonomer can run<br />

from one, for a strictly alternating copolymer, to very large numbers for block<br />

copolymers. Additionally, copolymers can have widely varying architectures, such<br />

as combs, stars, dendrimers, <strong>and</strong> others.<br />

As an initial entry into the field <strong>of</strong> copolymerization, ACOMP was recently<br />

applied to free radical copolymerization (42). The classical system <strong>of</strong> polystyrene/<br />

methyl methacrylate was chosen. Exploiting the differences in refractive index<br />

increment <strong>and</strong> UV absorption between each comonomer <strong>and</strong> the polymers, it was<br />

possible to obtain a continuous, on-line record <strong>of</strong> the conversion <strong>of</strong> each comonomer.<br />

This means that at every instant the remaining concentration <strong>of</strong> each comonomer is<br />

known, <strong>and</strong>, from the derivative <strong>of</strong> these concentrations, the instantaneous rate <strong>of</strong><br />

comonomer incorporation into polymer is known. This immediately provides a<br />

record <strong>of</strong> the average copolymer composition at every instant, so that the entire<br />

average compositional distribution <strong>of</strong> the copolymer is obtained during the reaction.<br />

Furthermore, by running two or more experiments at different initial relative<br />

comonomer concentrations it is possible to obtain the reactivity ratios <strong>of</strong> the<br />

comonomers without the need for the many approximations that have <strong>of</strong>ten been<br />

made in order to use single point techniques (43,44). Knowledge <strong>of</strong> the reactivity<br />

ratios, together with the instantaneous comonomer concentrations allows the average<br />

sequence length <strong>of</strong> the copolymer population also to be followed.<br />

© 2004 by Marcel Dekker, Inc.

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