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Equilibration polymerization

Scheme 3. Equilibration Polymerization Processes (Shown utilizing base catalysis). Scheme 3. Equilibration Polymerization Processes (Shown utilizing base catalysis).
The cyclic populations of a range of equilibrated polymeric methyl siloxanes (R(CH3)SiO)x where R is hydrogen, methyl, ethyl, n-propyl, 3,3,3-trifluoropropyl and phenyl have all been studied in recent years (16,18-20, 47, 48). Of these, the poly(dimethylsiloxane) system has received the most attention. It is the most important commercial silicone and it has proved to be more amenable to detailed experimental study than other silicones including those listed above. [Pg.48]

The oligomers utilized in this study to date have been prepared by the equilibration polymerization of a cyclic tetramer in the presence of functional disiloxanes utilizing a... [Pg.30]

Figure 1.4 Size-exclusion chromatography of a living, equilibrated polymerization mixture e Figure 1.4 Size-exclusion chromatography of a living, equilibrated polymerization mixture e<aprolactone (CL)/ triazabicyclodecene (TBD)/benzyl alcohol (BzOH). Conditions [CL] = 0.5 mol I", [TBD] = 2 X lOr mol I", [BzOH] = 2.5 x lO" moll THF solvent, SOX (A. Duda and A. Kowalski, unpublished results).
Following the completion of the polymerization process, the beaded polymer is recovered from the suspension mixture and freed from the stabilizer, diluents, and traces of monomers and initiators. For laboratory and small-scale preparation, repeated washings with water, methanol, or acetone are appropriate. Complete removal of the monomer diluent, solvents, and initiator, especially from macroporous resin, may require a long equilibration time with warm methanol or acetone. In industry, this is usually accomplished by stream stripping. [Pg.8]

Several important assumptions are involved in the derivation of the Mayo-Lewis equation and care must be taken when it is applied to ionic copolymerization systems. In ring-opening polymerizations, depolymerization and equilibration of the heterochain copolymers may become important in some cases. In such cases, the copolymer composition is no longer determined by die four propagation reactions. [Pg.9]

In a multiphase formulation, such as an oil-in-water emulsion, preservative molecules will distribute themselves in an unstable equilibrium between the bulk aqueous phase and (i) the oil phase by partition, (ii) the surfactant micelles by solubilization, (iii) polymeric suspending agents and other solutes by competitive displacement of water of solvation, (iv) particulate and container surfaces by adsorption and, (v) any microorganisms present. Generally, the overall preservative efficiency can be related to the small proportion of preservative molecules remaining unbound in the bulk aqueous phase, although as this becomes depleted some slow re-equilibration between the components can be anticipated. The loss of neutral molecules into oil and micellar phases may be favoured over ionized species, although considerable variation in distribution is found between different systems. [Pg.367]

In order to formulate an answer to the obviously important question of the length of this interval of acceleration and to ascertain under what conditions it may be long enough to observe experimentally, we shall examine the non-steady-state interval from the point of view of reaction kinetics. Let us suppose, however, that the polymerization is photoinitiated, with or without the aid of a sensitizer. It is then possible to commence the generation of radicals abruptly by exposure of the polymerization cell to the active radiation (usually in the near ultraviolet), and the considerable period required for temperature equilibration in an otherwise initiated polymerization can be avoided. Then the rate of generation of radicals (see p. 114) will be 2//a s, and the rate of their destruction 2kt [M ]. Hence... [Pg.149]

An even more serious problem concerns the corresponding time scales on the most microscopic level, vibrations of bond lengths and bond angles have characteristic times of approx. rvib 10-13 s somewhat slower are the jumps over the barriers of the torsional potential (Fig. 1.3), which take place with a time constant of typically cj-1 10-11 s. On the semi-microscopic level, the time that a polymer coil needs to equilibrate its configuration is at least a factor of the order larger, where Np is the degree of polymerization, t = cj 1Np. This formula applies for the Rouse model [21,22], i. e., for non-... [Pg.49]


See other pages where Equilibration polymerization is mentioned: [Pg.183]    [Pg.656]    [Pg.249]    [Pg.308]    [Pg.33]    [Pg.195]    [Pg.196]    [Pg.25]    [Pg.25]    [Pg.53]    [Pg.773]    [Pg.223]    [Pg.225]    [Pg.8]    [Pg.8]    [Pg.183]    [Pg.656]    [Pg.249]    [Pg.308]    [Pg.33]    [Pg.195]    [Pg.196]    [Pg.25]    [Pg.25]    [Pg.53]    [Pg.773]    [Pg.223]    [Pg.225]    [Pg.8]    [Pg.8]    [Pg.250]    [Pg.107]    [Pg.559]    [Pg.251]    [Pg.455]    [Pg.487]    [Pg.498]    [Pg.503]    [Pg.2]    [Pg.33]    [Pg.5]    [Pg.17]    [Pg.19]    [Pg.25]    [Pg.28]    [Pg.76]    [Pg.127]    [Pg.127]    [Pg.100]    [Pg.321]    [Pg.330]    [Pg.824]    [Pg.721]    [Pg.318]   


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Disiloxane equilibration polymerization

Equilibrated

Equilibration

Equilibration polymerization processes

Equilibrator

Ring-opening polymerizations equilibration reactions

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