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Additives emulsion polymerization

A kinetic model for the particle growth stage for continuous-addition emulsion polymerization has been proposed (35). Below the monomer... [Pg.429]

Fig. 6. Apparatus for continuous-addition emulsion polymerization of a VDC-acrylate mixture (153). Fig. 6. Apparatus for continuous-addition emulsion polymerization of a VDC-acrylate mixture (153).
A kinetic model for the particle growth stage for continuous-addition emulsion polymerization has been proposed (35). Below the monomer saturation point, the steady-state rate of polymerization, depends on the rate of monomer addition, R, according to the following reciprocal relationship ... [Pg.429]

Of the fibers listed in Table II only the polyesters, polyamides, spandexes, acetates, and rayon are discussed in this chapter. While the acrylics and modacrylics are the third most important class of commercial fibers because their polymerization chemistry is also discussed in other chapters concerned with vinyl addition emulsion polymerizations, it will only be briefly summarized here. For the same reason polypropylene polymerization chemistry is also not covered in this section. However, two additional topics, carbon fiber formation and polybenzimidazoles have been included on the basis of the current Interest in high-performance fibers for composite materials. [Pg.442]

High Percent Solids Continuous Addition Emulsion Polymerization of Vinyl... [Pg.203]

The authors collected the test data shown in Table 9.10. From these data it can be noted that the number-average molecular weight, or Af , of a commercial emulsion SBR such as IISRP 1500 or 1712 is typically 90,000-175,000. The primary molecular weight of a solution-polymerized polymer produced with an anionic lithium catalyst can, in contrast, be increased toward 250,000 without gelation. In addition, emulsion-polymerized SBR contains only about 92% rubber hydrocarbon as a result of the presence of residues from the production process solution polymers tend to be near 100% hydrocarbon. As a consequence, the authors concluded that the number-average molecular weight... [Pg.424]

In addition, emulsion polymerizations exhibit promising benefits and the possibility for efficient control of the composition and size of particles. As a result, this causes these processes to exhibit excellent results in the polymerization of monomers with low reactivity, such as vegetable oils and their derivatives [21,22]. Apropos to the production of polymer/inorganic hybrid nanoparticles, pertain promising results of products intended for medical/pharmaceutical area, particularly magnetic nanoparticles used for the induction of controlled hyperthermia procedures in treatment of... [Pg.210]

Wessling RA. Kinetics of continuous addition emulsion polymerization. J Appl Polym Sci 1968 12 309-319. [Pg.269]

Several polymerization techniques are in widespread usage. Our discussion is biased in favor of methods that reveal additional aspects of addition polymerization and not on the relative importance of the methods in industrial practice. We shall discuss four polymerization techniques bulk, solution, suspension, and emulsion polymerization. [Pg.396]

There is a great deal more that could be said about emulsion polymerization or, for that matter, about free-radical polymerization in general. We shall conclude our discussion of the free-radical aspect of chain-growth polymerization at this point, however. This is not the end of chain-growth polymerization, however. There are four additional topics to be considered ... [Pg.403]

The incidence of these defects is best determined by high resolution F nmr (111,112) infrared (113) and laser mass spectrometry (114) are alternative methods. Typical commercial polymers show 3—6 mol % defect content. Polymerization methods have a particularly strong effect on the sequence of these defects. In contrast to suspension polymerized PVDF, emulsion polymerized PVDF forms a higher fraction of head-to-head defects that are not followed by tail-to-tail addition (115,116). Crystallinity and other properties of PVDF or copolymers of VDF are influenced by these defect stmctures (117). [Pg.387]

There are two principal PVC resins for producing vinyl foams suspension resin and dispersion resin. The suspension resin is prepared by suspension polymerization with a relatively large particle size in the 30—250 p.m range and the dispersion resin is prepared by emulsion polymerization with a fine particle size in the 0.2—2 p.m range (245). The latter is used in the manufacture of vinyl plastisols which can be fused without the appHcation of pressure. In addition, plastisol blending resins, which are fine particle size suspension resins, can be used as a partial replacement for the dispersion resin in a plastisol system to reduce the resin costs. [Pg.420]

In the paste coating method, a PVC paste, which contains emulsion-polymerized PVC and additives, is appHed onto a substrate and heated to gelation before fusion to produce a coating layer. This method is employed for products with a thin layer, ie, of 0.007—0.05 mm thickness. For foamed vinyl-coated fabrics, a substrate is laminated onto a transfer paper on which a PVC paste containing a foam-blowing agent has been appHed and geUed. After removal of the transfer paper, the paste is blown. [Pg.93]

Copolymers with butadiene, ie, those containing at least 60 wt % butadiene, are an important family of mbbers. In addition to synthetic mbber, these compositions have extensive uses as paper coatings, water-based paints, and carpet backing. Because of unfavorable reaction kinetics in a mass system, these copolymers are made in an emulsion polymerization system, which favors chain propagation but not termination (199). The result is economically acceptable rates with desirable chain lengths. Usually such processes are mn batchwise in order to achieve satisfactory particle size distribution. [Pg.520]

In addition to appHcations in dyeing, sodium formaldehyde sulfoxylate is used as a component of the redox system in emulsion polymerization of styrene—butadiene mbber recipes. [Pg.151]

Emulsion Polymerization. Emulsion polymerization is used commercially to make vinyhdene chloride copolymers. In some apphcations, the resulting latex is used directiy, usually with additional stabilizing ingredients, as a coating vehicle to apply the polymer to various substrates. In other... [Pg.438]

Table 14. Recipe for Emulsion Polymerization by Continuous Addition ... Table 14. Recipe for Emulsion Polymerization by Continuous Addition ...

See other pages where Additives emulsion polymerization is mentioned: [Pg.163]    [Pg.213]    [Pg.123]    [Pg.1062]    [Pg.1177]    [Pg.211]    [Pg.2065]    [Pg.288]    [Pg.163]    [Pg.213]    [Pg.123]    [Pg.1062]    [Pg.1177]    [Pg.211]    [Pg.2065]    [Pg.288]    [Pg.271]    [Pg.168]    [Pg.168]    [Pg.279]    [Pg.386]    [Pg.266]    [Pg.267]    [Pg.252]    [Pg.311]    [Pg.491]    [Pg.493]    [Pg.74]    [Pg.243]    [Pg.244]    [Pg.439]    [Pg.439]    [Pg.459]    [Pg.464]   
See also in sourсe #XX -- [ Pg.357 , Pg.358 , Pg.359 , Pg.360 , Pg.361 , Pg.362 , Pg.363 , Pg.364 , Pg.365 , Pg.366 ]




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Addition polymerization

Additional polymerization

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Additives polymerization

Emulsion additives

Emulsion polymerization

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Polymeric additives

Polymerization emulsion polymerizations

Reversible addition-fragmentation chain transfer emulsion polymerization

Seeded emulsion polymerization molecular weight additives

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