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Melt, generally processing

In order to make useful products from polymers we typically follow a three-step process in which we sequentially melt, shape, and cool the polymer. Naturally, given the wide variety of polymers available and their myriad applications, variations on this general process abound. In this chapter, we will concentrate on extrusion, some variant of which is used in the majority of commercial fabrication processes. [Pg.213]

If you analyze the four spontaneous endothermic processes mentioned previously, you ll see that each involves an increase in the randomness of the system. When ice melts, for example, randomness increases because the highly ordered crystalline arrangement of tightly held water molecules collapses and the molecules become free to move about in the liquid. When liquid water vaporizes, randomness further increases because the molecules can now move independently in the much larger volume of the gas. In general, processes that convert a solid to a liquid or a liquid to a gas involve an increase in randomness and thus an increase in entropy (Figure 17.3). [Pg.724]

Generally, processing temperatures for THV are comparable to those used for most thermoplastics. In extrusion, melt temperatures at the die are in the 230°C to 250°C (446°F to 482°F) range. These relatively low processing temperatures open new options for combinations of different melts (coextrusion, cross-head extrusion. [Pg.77]

Ring closure of Af-(]-cyanoalkyl)alkylidene Af-oxides (these compounds are nitrones, cf. Section 4.2) is induced by nucleophilic attack by the thiophenate ion (Scheme 2.1.10). The reactions are accelerated by the addition of small amounts of piperidine, but inhibited by temperatures above the melting points of the nitrones. In these reactions, 4-phenylthioimidazoles (23) are formed usually in 80-90% yields. Deficiencies in the general process include the problems of first making the nitrones, and the fact that other thiolate nucleophiles (methyl, ethyl, benzyl) are much less successful, giving only low yields of 4-alkyIthioimidazoles [63]. [Pg.15]

Electrochemical studies in alkaline melts are complicated by the absence ol detailed information on the chemistry of corresponding systems, and in particular or solvation processes. Moist melts generally represent the limiting case of strong base solutions. It would undoubtedly useful to study the changes in the kinetics and the composition of the products of anodic electrocrystallization in a model system upor the gradual transition from common alkaline solutions to concentrated bases, anc then to alkaline melts with different water contents. [Pg.95]

The advantages of using melt-congealing processes are numerous. Generally, no solvent is required in the formulation and manufacturing processes, and the subsequent environmental requirement of solvent capture and recycle is eliminated. Processing times are often much shorter because solvent evaporation is... [Pg.771]

Development of this model is continuing in our laboratory, and among the aspects still under development are capabilities for transient flows, reactive fluids, free surfaces, and wall slip. Although incorporation of fluid elasticity is desired due to its importance in many polymer melt flows, such a development has proven elusive to a number of well qualified groups in the past several years. At present, it seems prudent to let the theoretical aspects of elastic effects be developed further before attempting their incorporation in a general process model. [Pg.276]

Commercially, it is polymerized by free-radical polymerization mechanism, usually in an aqueous (or nonaqueous) media via addition polymerization of TFE and hexafluoropropylene. The initiator for the polymerization is usually water-soluble peroxide, such as potassium persulfate. Chain transfer agents could be used to control the molecular weight of the resin. In general, the polymerization regime and conditions resemble those used to produce PTFE by emulsion polymerization. For melt fabrication processes, FEP is recovered, dried, and melt-extruded into cubes. It is also available in dispersion form. [Pg.1035]

The general process for melt polycondensation of poly anhydrides is shown in Fig. 3. It consists of... [Pg.2249]

For this comparison, a melt-spinning process was chosen. Each special thermoplastic process influences the structure and thus the properties of the obtained polymer samples differently. This is particularly pronounced for fibers, since especially melt spinning is a process which makes extremely high demands on the deformation ability of the polymer melts at high deformation speeds. Particularly the tensile stress within the fiber formation zone is a very important factor to reach a high orientation of the macromolecules along the fiber axis and a stress-induced crystallization. This crystallization should be discussed in relation to PLA and PHB multifilaments, and at the same time the general property spectrum of these polymers should be represented. [Pg.203]


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See also in sourсe #XX -- [ Pg.37 , Pg.38 , Pg.42 , Pg.347 ]




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