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Vinyl chloride polymerization in microdroplet reactor - Les thèses en ...

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Chapter I : Bibliographic review<br />

2 hours at 80° C > t 1/2 > 2/3 hour at 40° C.<br />

Organic peroxides are unstable chemical compounds, decompos<strong>in</strong>g at relatively low temperatures.<br />

They can, however, be handled and stored safely if proper precautions are followed. They can be solid<br />

long-cha<strong>in</strong> alkyl peroxydicarbonates, available <strong>in</strong> differ<strong>en</strong>t formulations. Among the latter, the water<br />

based peroxide susp<strong>en</strong>sions and emulsions are much safer than the usual solid, liquid or solv<strong>en</strong>t based<br />

peroxides.<br />

The conc<strong>en</strong>tration and type of <strong>in</strong>itiator dep<strong>en</strong>ds on the <strong>polymerization</strong> temperature and the required<br />

<strong>polymerization</strong> rate. It is common to use differ<strong>en</strong>t types and oft<strong>en</strong> comb<strong>in</strong>ations of two or more<br />

<strong>in</strong>itiators <strong>in</strong> order to optimize the reaction. For <strong>in</strong>stance, at low temperatures, a fast <strong>in</strong>itiator may be<br />

employed <strong>in</strong> comb<strong>in</strong>ation with a slower one. The fast <strong>in</strong>itiator ma<strong>in</strong>ly steps <strong>in</strong> at the very beg<strong>in</strong>n<strong>in</strong>g of<br />

the reaction <strong>in</strong> order to boost the slow <strong>in</strong>itial rate while the slow one <strong>en</strong>ables a constant reaction rate<br />

until the limit<strong>in</strong>g conversion is reached. (P<strong>in</strong>to et al., 2001).<br />

Dur<strong>in</strong>g the first stages of the reaction, the small droplets of <strong>in</strong>itiator rapidly diffuse <strong>in</strong>to the VCM. The<br />

break-up and coalesc<strong>en</strong>ce processes of the VCM droplets at the beg<strong>in</strong>n<strong>in</strong>g of the reaction positively<br />

contribute to the <strong>in</strong>itiator distribution. This distribution over the VCM droplets was found to <strong>in</strong>flu<strong>en</strong>ce<br />

the morphology of the f<strong>in</strong>al PVC particles. If the <strong>in</strong>itiator is not equally partitioned <strong>in</strong> each VCM<br />

droplet, particles without any porosity can be formed, which are therefore called clear particles. These<br />

non-porous particles have a glassy character, a high d<strong>en</strong>sity and they are very difficult to process. The<br />

pres<strong>en</strong>ce of these particles causes the appearance of visible imperfections, the so-called fish-eyes, on<br />

the surface of f<strong>in</strong>ished PVC products.<br />

The distribution of <strong>in</strong>itiator over VCM droplets can be homog<strong>en</strong>ized <strong>in</strong> a very short period of time (5<br />

m<strong>in</strong>utes) by dos<strong>in</strong>g the <strong>in</strong>itiator <strong>in</strong> solution <strong>in</strong> an <strong>in</strong>ert solv<strong>en</strong>t or as a susp<strong>en</strong>sion <strong>in</strong>stead of a dosage as<br />

a solid material with non-uniform particle sizes (PVC Symposium 1990a, PVC Symposium 1990b).<br />

The <strong>polymerization</strong> k<strong>in</strong>etics is <strong>in</strong>flu<strong>en</strong>ced by the type of <strong>in</strong>itiator, <strong>in</strong> particular by its decomposition<br />

rate or by the rate of distribution betwe<strong>en</strong> monomer and polymer phases as highlighted by Titova et al.<br />

(1982).<br />

30

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