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Multicomponent polymeric studies

The pseudo-kinetic rate constant method for multicomponent polymerization has been applied in some copolymerization studies (3-5), and its derivation and specific approximations have been made clear (6,7). The pseudo-kinetic rate constants basically... [Pg.242]

The study of multicomponent polymeric systems is now one of advanced domains in modem polymer science. Recent years have revealed their growing importance from both scientific and practical points of view. [Pg.294]

However, over the last decade, important advances have been made in IR micro-spectroscopy with a synchrotron source [16], which can provide new opportunities and motivation for the study of polymeric materials. The most utilized key synchrotron parameter for this community is the ability, thanks to the source brightness, to differentiate the chemical nature of the constituents in multicomponent polymeric systems. When the sizes of the different domains are in the range of the IR wavelength (micron scale), the spatial differentiation and study of each of these domains is possible using SR-FTIR micro-spectroscopy. Such analytical tools allow the study of various aspects related to the chemical composition, structure and morphology of the polymeric materials. Some of the areas that have benefited from synchrotron infrared over the last four years are reviewed in this section. [Pg.144]

It is therefore, hopeful that the present study will constitute a reasonable first step towards the development of a unified theory for the interpretation of the rheological behavior of homogeneous, multicomponent polymeric materials in the entangled regime. [Pg.382]

Figure 8.13 Microfluidic setup for kinetic studies of a multicomponent polymerization reaction, (a) World-to-chip interface for fluidic connections and probes, (b) Schematic of the microreactor. Aqueous solutions of APS, NIPAm, TEMED, and water were introduced into the MF reactor at inlets (i)—(iv), respectively. Mixing and polymerization occurred in (v) and characterization of the reaction occurred at Pi, Pi, and P) by ATR-... Figure 8.13 Microfluidic setup for kinetic studies of a multicomponent polymerization reaction, (a) World-to-chip interface for fluidic connections and probes, (b) Schematic of the microreactor. Aqueous solutions of APS, NIPAm, TEMED, and water were introduced into the MF reactor at inlets (i)—(iv), respectively. Mixing and polymerization occurred in (v) and characterization of the reaction occurred at Pi, Pi, and P) by ATR-...
Thus, morphological studies of the multicomponent polymeric materials have been carried out by employing miaoscopy and scattering methods. Commercially available optical miaoscopes, transmission electron microscopes (TEMs), scanning electron microscopes (SEMs), and atomic force microscopes (AFMs) have been widely used in these... [Pg.527]

Although a number of techniques have been devised to investigate the bulk domain structure of multicomponent polymer systems the detailed structure of the surface, i.e., the outermost few tens of angstroms, has been studied in much less detail. Since many of the important properties of a polymeric solid are dependent upon the surface structure and since the surface can differ considerably from the bulk a technique which can differentiate the surface from bulk properties is likely to be of considerable importance. [Pg.319]

Multicomponent films were studied in [2963], and multilayer membranes in [279,2964-2967]. The polymeric membranes studied in [2968] were modified by post-treatment. Also, a-alumina identical to the material in Membralox membrane from SCT, studied in [1851], probably underwent surface treatment. [Pg.864]

The kinetics of emulsion polymerization reactions are complex because of the numerous chemical and physical phenomena that can occur in the multicomponent, multiphase mixture. A large amount of literature exists on kinetics problems. The general references listed at the end of this chapter contain many important papers. The review paper by Ugelstad and Hansen (11) is a comprehensive treatment of batch kinetics. The purpose of the remainder of this chapter is to present the general kinetics problems and some of the published results. The reader should use the references cited earlier for a more detailed study. [Pg.141]

An enormous number of possible multicomponent systems, makes it impossible to di.scuss them here in detail. However it should be mentioned that there are two general approaches in the sol-gel synthesis of multicomponent systems hydrolysis of mixed-alkoxide or metal organic precursors, and sequential addition of alkoxides to partially hydroly/.ed precursors (I9j. The first method was invented by Dislich [20], based on the idea to form complex via alcolation that contains all metals in proper stoichiometry. The second approach which is based on the sequential addition of alkoxides in the reverse order of their respective reactivities, was introduced by Thomas [18] and Yoldas [21,22]. The idea is that the newly added unhyhdrolyzed alkoxide will condense with partially hydrolyzed sites on the polymeric species fonned by the preceding hydrolysis and condensation, rather than reacting with themselves. The homogeneity of the product will depend on the size of the polymeric species to which the last component is added. T)ie most widely studied multicomponent systems are AI O,-SiO.. B.O,-SiO and TiO-SiO. ... [Pg.46]

In this chapter, the possibihty of using late transition metal catalysts to synthesize polyolefins in supercritical carbon dioxide was demonstrated [43]. The multicomponent phase behavior of polyolefin systems at supercritical conditions was studied experimentally by measuring cloud-point curves as well as by modeling polymer systems at supercritical conditions. The cloud-point measurements show that CO2 acts as a strong antisolvent for the ethylene-PEP system, which implies that the polymerization concerned will involve a precipitation reaction. The model calculations prove that SAFT is able to describe the ethylene-PEP-CO2 system accurately. Solubility measurements of the Brookhart catalyst reveal that the maximum catalyst solubility is rather low (in the order of 1x10 mol L ). However, a number of strategies are given to enhance this value. [Pg.183]


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