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Droplet size polymerization techniques

The styrene-DVB copolymer beads are prepared by suspension (pearl) polymerization technique. The monomers are mixed and a polymerization catalyst such as benzoyl peroxide is added. The mixture is then dispersed into small droplets in a thoroughly agitated aqueous solution that is kept at a temperature required for polymerization (usually 85°C-100°C). A suspension stabilizer (gelatin, polyvinyl alcohol, sodium oleate, magnesium silicate, etc.) in the aqueous phase prevents agglomeration of the droplets. The size of the droplets depends chiefly on the stabilizer, the viscosity of the solution, and the agitation, and it can be varied within wide limits. As polymerization takes place, the droplets are transformed into polymer beads. For most purposes, a bead size of 0.1-0.5 mm is preferred, but beads from 1 pm to 2 mm in diameter can be prepared without much difficulty. [Pg.640]

For the successful preparation of emulsions, the wetting conditions on the membrane surface are crucial. It is necessary that the membrane surface is only wetted by the liquid that forms the continuous phase. The droplet size correlates with the membrane pore size by a simple relation, Dd = /Dm where / is a value typically between 2 and 8 (35). Droplets can be produced with diameters in the pm-, as well as in the sub-micrometre range. This technique has been successfully applied to produce monodisperse emulsions and multiple emulsions, as well as to carry out polymerizations leading to polymer particle in the pm size range with narrow size distributions (36, 37). Further advantages (38) are as follows the droplet size is controllable and generally a quite narrow DSD can be achieved, the method is reproducible and the scale-up is easy just by increasing the number of membrane modules, the characteristic features are independent of scale-up, batch as well as continuous operations modes are possible, the continuous phase is exposed to a lower stress. [Pg.183]

Another size scale, which, however, is important for each polymerization technique, is the shrinkage of the reaction volume due to the density increase during polymerization The size of a monomer droplet decreases due to polymerization of the monomer according to equation (8.32), where Pmon and Ppoi are the densities of the monomer and polymer, respectively ... [Pg.192]

Fig. 2 Schematic illustrations of encapsulation of porous silicon nanoparticles in block copolymer micelles or by miniemulsion polymerization. Instead of attempting to functionalize the nanoparticle surface directly, a functional group X is incorporated into a suitable block copolymer (top) or in the monomer droplet of a miniemulsion polymerization technique (bottom). These techniques expand the range of functionalities that can be incorporated into SiNC-based systems and facilitate greater synthetic control. The main disadvantage of such systems is the increased size of the final object which may obviate particular applications, e.g., some intracellular imaging applications... Fig. 2 Schematic illustrations of encapsulation of porous silicon nanoparticles in block copolymer micelles or by miniemulsion polymerization. Instead of attempting to functionalize the nanoparticle surface directly, a functional group X is incorporated into a suitable block copolymer (top) or in the monomer droplet of a miniemulsion polymerization technique (bottom). These techniques expand the range of functionalities that can be incorporated into SiNC-based systems and facilitate greater synthetic control. The main disadvantage of such systems is the increased size of the final object which may obviate particular applications, e.g., some intracellular imaging applications...
Abstract Monodispersed biodegradable poly(n-butylcyanoacrylate) nanocapsules containing DNA molecules (790 base pairs) within an aqueous core were prepared by anionic polymerization of n-butyl-cyanoacrylate at the droplets interface in inverse miniemulsion. The aqueous droplets in the size range of 300-700 nm dispersed in the hydrophobic continuous phase were formulated using the miniemulsion technique that allows an easy control of the droplet size and size distribution. After polymerization, the capsules were transferred into an aqueous phase. The effect of several reaction parameters such as the amount of monomer, type of the non-ionic surfactant (i.e. Span 80 and Tween 80) and type of the continuous phase (i.e. Miglyol 812N and... [Pg.120]

A few distributions of VCM suspensions in water viewed by light microscopy into specially designed pressure cells appear in the literature (23,24), but no analyses of droplet size distribution under different conditions of reactor agitation or polymeric additive addition have been reported. A technique for fixing VCM emulsions by osmium tetroxide (25) may prove useful to study the VCM/water system in greater detail. Mersmann and Grossmann (26) have studied the dispersion of liquids in non-miscible two-phase systems, which include chlorinated liquids such as carbon tetrachloride in water. The influence of stirrer type and speed on the development of an equilibrium droplet size distribution is discussed. Different empirical relationships to calculate the Sauter mean diameter of droplet distributions from reactor operating parameters are also reviewed. [Pg.251]


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See also in sourсe #XX -- [ Pg.195 , Pg.196 , Pg.197 ]

See also in sourсe #XX -- [ Pg.195 , Pg.196 , Pg.197 ]




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