Vinyl chloride polymerization in microdroplet reactor - Les thèses en ...
Vinyl chloride polymerization in microdroplet reactor - Les thèses en ...
Vinyl chloride polymerization in microdroplet reactor - Les thèses en ...
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Chapter I : Bibliographic review<br />
Emulsion<br />
Latex may be directly usable<br />
High <strong>polymerization</strong> rates<br />
possible<br />
Usable, small-particle size<br />
possible<br />
Usable <strong>in</strong> produc<strong>in</strong>g soft and<br />
solid particles<br />
Polymer may require additional cleanup and<br />
purification<br />
Difficult to elim<strong>in</strong>ate <strong>en</strong>tr<strong>en</strong>ched coagulants,<br />
emulsifiers, surfactants etc.<br />
Oft<strong>en</strong> requires rapid agitation<br />
Precipitation<br />
Susp<strong>en</strong>sion<br />
Molecular weight distribution<br />
ma<strong>in</strong>ta<strong>in</strong>ed by control of<br />
<strong>polymerization</strong> <strong>en</strong>vironm<strong>en</strong>t<br />
Easy agitation<br />
Higher-purity product wh<strong>en</strong><br />
compared to emulsion<br />
May require solution and reprecipitation of<br />
product to remove unwanted material<br />
Precipitation may act to limit molecularweight<br />
disallow<strong>in</strong>g formation of ultrahighmolecular-weight<br />
products<br />
S<strong>en</strong>sitive to agitation<br />
Particle size difficult to control<br />
Table I- 1: Characteristics of the ma<strong>in</strong> v<strong>in</strong>yl <strong>chloride</strong> <strong>polymerization</strong> methods<br />
I.C. Physical Considerations On <strong>V<strong>in</strong>yl</strong> Chloride Monomer<br />
At ambi<strong>en</strong>t temperature and pressure, v<strong>in</strong>yl <strong>chloride</strong> (VCM) is a colorless gas, with its boil<strong>in</strong>g<br />
temperature of -13.8 °C and a sweet, ethereal odor accord<strong>in</strong>g to Blout et al. (1949). VCM is stored or<br />
shipped as a liquid, which has a vapor pressure of about 3 bar at ambi<strong>en</strong>t temperatures. VCM is highly<br />
flammable and forms explosive mixtures with air. Hazardous properties of VCM are its narcotic effect<br />
<strong>in</strong> the case of <strong>in</strong>halation of high conc<strong>en</strong>trations and its carc<strong>in</strong>og<strong>en</strong>ity, caus<strong>in</strong>g angiosarcomas<br />
(Cameron et al., 1981). The toxicological data on VCM are pres<strong>en</strong>ted <strong>in</strong> App<strong>en</strong>dix A1 of this thesis.<br />
The solubility of VCM <strong>in</strong> water is about 8.8·10 -3 P/P 0 (kg/kg water), where P is the partial pressure and<br />
P 0 the saturation pressure of VCM.<br />
The liquid d<strong>en</strong>sity at 25 °C is 901.3 kg/m 3 and the d<strong>en</strong>sity of technical PVC falls <strong>in</strong>to the range of<br />
1390-1400 kg/m 3 . The heat of <strong>polymerization</strong> has be<strong>en</strong> determ<strong>in</strong>ed to be ∆H p = -97.6 kJ/mol (Saeki<br />
and Emura, 2002). The <strong>in</strong>terfacial t<strong>en</strong>sion at the water/VCM <strong>in</strong>terface without additives is found to be<br />
32 mN/m (Nilsson et al., 1985).<br />
I.D. <strong>V<strong>in</strong>yl</strong> Chloride Susp<strong>en</strong>sion <strong>polymerization</strong><br />
The susp<strong>en</strong>sion <strong>polymerization</strong> process of v<strong>in</strong>yl <strong>chloride</strong> (S-PVC) is a process carried out <strong>in</strong> millions<br />
of ‘small <strong>reactor</strong>s’ repres<strong>en</strong>ted by the monomer droplets themselves.<br />
20