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Site of Polymerization

The initiator is present in the water phase, and this is where the initiating radicals are produced. The rate of radical production R, is typically of the order of radicals L s . (The symbol p is often used instead of R, in emulsion polymerization terminology.) The locus of polymerization is now of prime concern. The site of pol3mierization is not the monomer droplets since the initiators employed are insoluble in the organic monomer. Such initiators are referred to as oil-insoluble initiators. This situation distinguishes emulsion polymerization from suspension polymerization. Oil-soluble initiators are used in suspension polymerization and reaction occurs in the monomer droplets. The absence of polymerization in the monomer droplets in emulsion polymerization has been experimentally verified. If one halts an emulsion polymerization at an appropriate point before complete conversion is achieved, the monomer droplets can be separated and analyzed. An insignificant amount (approximately 0.1%) of polymer is found in the monomer droplets in such experiments. Polymerization takes place almost exclusively in the micelles. Monomer droplets do not compete effectively with micelles in capturing radicals produced in solution because of the much smaller total surface area of the droplets. [Pg.353]

Polymerization of the monomer in solution undoubtedly takes place but does not contribute significantly, since the monomer concentration is low and propagating radicals would precipitate out of aqueous solution at very small (oligomeric) size. The micelles act as a meeting place for the organic (oil-soluble) monomer and the water-soluble initiator. The micelles are favored as the reaction site because of their high monomer concentration (similar to bulk monomer concentration) compared to the monomer in solution. As polymerization proceeds, the micelles grow by the addition of monomer from the aqueous solution whose concentration is replenished by dissolution of monomer from the monomer droplets. A simplified schematic representation of an emulsion polymerization system is shown in Fig. 4-1. The system consists of three types of particles monomer droplets, inactive micelles in which [Pg.353]


There are two strategies for constructing a polymer with benzyl ester in the middle of the skeleton. One is to make polymer skeletons with the same molecular weight, and then combine two skeletons with benzyl ester. The other is to synthesize a chemical with propagation sites of polymerization at both sides of benzyl ester, and use the chemical as an initiator of living polymerization. Since the former strategy did not work well, probably due to low reactivity of polymer molecules with benzyl esters, the latter approach will be mentioned. [Pg.624]

However, emulsion polymerizations involve the formation of colloidal polymer particles that are essentially permanently suspended in the reaction medium. The reaction mechanism involves the migration of monomer molecules from liquid monomer droplets to sites of polymerization that originate in micelles consisting of surface-active agent molecules surrounding monomer molecules. Emulsion polymerizations are usually characterized by the requirement of surfactants during the initiation of the process and by the use of water-soluble initiators. This process also permits good control of the exothermic nature of the polymerization. [Pg.30]

Film penetration studies show unequivocally that lecithin-cholesterol mixtures containing from 0 to 50 mole % cholesterol and lecithin—lactoside mixtures containing from 0 to 80 mole % Ci6-dihydroceramide lactoside have the same effect as pure lecithin. This suggests the presence of a lipid complex in which lecithin prevents the interaction of the cholesterol or ceramide lactoside with globulin. Over these ranges of composition the lipid film would consist of a mixture of the lecithin-cholesterol or the lecithin-lactoside complex with excess lecithin. One may picture two models in which the protein contact is restricted to molecules of lecithin. In one, individual polar groups of the protein interact with the excess lecithin molecules as well as with the lecithin portions of the complex. In the other model, the protein as a whole interacts with the lecithin sites of polymeric lipid structures. The latter, which could be referred to as surface micelles (I), are visualized also through the term "mono-... [Pg.171]

Schuller [150] and Guillot [98] both observed that the copolymer compositions obtained from emulsion polymerization reactions did not agree with the Mayo Lewis equation, where the reactivity ratios were obtained from homogeneous polymerization experiments. They concluded that this is due to the fact that the copolymerization equation can be used only for the exact monomer concentrations at the site of polymerization. Therefore, Schuller defined new reactivity ratios, TI and T2, to account for the fact that the monomer concentrations in a latex particle are dependent on the monomer partition coefficients (fCj and K2) and the monomer-to-water ratio (xp) ... [Pg.195]

In contrast to the Wzy/Wzx-independent O antigens (see Section 6.10.2.2.2), no obvious ABC transporters have been identified in wzy-dependent systems. At least three proteins (Wzx, Wzy, and Wzz) are involved in this export pathway but currently, there is no information concerning the manner in which these proteins interact with one another to facilitate the formation of predicted functional complexes. Once the individual Und-PP-linked O subunits are formed, they must be exported to the site of polymerization at the periplasmic face of the plasma membrane (Figure 2(a)). [Pg.304]

It would appear self-evident that operations carried out at reflux temperatures would encounter difficulties resulting from the problem of returning the monomer to the sites of polymerization in the reaction medium. In part, this problem may be overcome by returning the refluxing distillate well beneath the surface of the dispersion rather than to the top of the medium. [Pg.205]

Kinetic results [11-13] The rate of styraiepolymerizaticm initiated by potassium persulfate in a monodisperse polystyrene (PS) seed latex (c. 200 run in diameter) was ctxistant from 0% up to 60% convositxi, while the monomer concentration in the particles decreased significantly. In order for the polymerization rate to remain constant while the total monomer concentration was halved, the monomer concentration at the site of polymerization must be constant. In terms of the Smith-Ewart theory. Case 2, the rate of polymerization per particle, / pp, is expressed as... [Pg.568]

Fig. 1. Resonance valence-bond ground state structures of DTT, which assume the several possible sites of polymerization. [Pg.413]

Y.B. Monakov, N.N. Sigaeva and V.N. Urazbaev in Active Sites of Polymerization. Multiplicity Stereospecific and Kinetic Heterogeneity, Brill Academic Publishers, Leiden, Netherlands, 2005. [Pg.206]

Since pyrrole and thiophene polymerization occurs at a positions, functionalization has been carried out generally at /3 sites. A-functionalization is a further possibility for pyrrole. In any case, both the A-substitution in pyrrole and the ]3-substitution, either in pyrrole or in thiophene, correspond to the introduction of a functionality at an ortho position with regard to the site of polymerization. [Pg.66]

Wzy-dependent pathway is most widespread in O polysaccharide biosynthesis. Following the assembly of O repeating units, the individual und-PP-linked O units are exported to the site of polymerization at the periplasmic face of the plasma membrane (Figure 2). This process requires a Wzx protein, the O unit transporter (flippase), which is highly hydrophobic with 12 potential transmembrane domains. Although the Wzx proteins share little primary sequence similarity, they do share structural features with bacterial permeases... [Pg.206]

The ultrasonic irradiation of the reaction mixture at the initial time of the polymerization of butadiene and isoprene imder action Ti-Al catalyst result in an increase of process rate. Polymerization occurs at the single active site reactivity of which depends on the nature of diene. With ultrasonic treatment the reactivity of the active sites of polymerization of isoprene greater than for the butadiene polymerization. Reduction of polymerization reactivity site butadiene reduces cis-specificity titanium catalyst. In all cases ultrasoimd irradiation produces a polydienes with a narrow molecular weight distribution. [Pg.114]

Monakov, Y. B., Sigaeva, N. N. Urazbaev, V. N. (2005). Active Sites of Polymerization. Multiplicity Steivospecific and Kinetic Heterogeneity, Leiden Brill Academie, 397 p. [Pg.115]


See other pages where Site of Polymerization is mentioned: [Pg.353]    [Pg.29]    [Pg.499]    [Pg.58]    [Pg.154]    [Pg.79]    [Pg.11]    [Pg.725]    [Pg.353]    [Pg.467]    [Pg.36]    [Pg.299]    [Pg.48]    [Pg.11]    [Pg.369]    [Pg.219]    [Pg.222]    [Pg.252]    [Pg.203]    [Pg.1505]    [Pg.1003]    [Pg.19]   


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