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Solvent concentration polymerization

Terpolymers from dimethy]-a.-methy]styrene (3,4-isomer preferred)—a-methylstyrene—styrene blends in a 1 1 1 weight ratio have been shown to be useful in adhesive appHcations. The use of ring-alkylated styrenes aids in the solubiHty of the polymer in less polar solvents and polymeric systems (75). Monomer concentrations of no greater than 20% and temperatures of less than —20° C are necessary to achieve the desired properties. [Pg.356]

Alkyl sulphoxides occur widely in small concentrations in plant and animal tissues. No gaseous sulphoxides are known and they tend to be colourless, odourless, relatively unstable solids soluble in water, ethyl alcohol and ether. They are freely basic, and with acids form salts of the type (R2S0H) X. Because sulphoxides are highly polar their boiling points are high. Their main use is as solvents for polymerization, spinning, extractions, base-catalysed chemical reactions and for pesticides. [Pg.38]

In the literature there is only one serious attempt to develop a detailed mechanistic model of free radical polymerization at high conversions (l. > ) This model after Cardenas and 0 Driscoll is discussed in some detail pointing out its important limitations. The present authors then describe the development of a semi-empirical model based on the free volume theory and show that this model adequately accounts for chain entanglements and glassy-state transition in bulk and solution polymerization of methyl methacrylate over wide ranges of temperature and solvent concentration. [Pg.43]

A useful model should account for a reduction of kt and kp with increase in polymer molecular weight and concentration and decrease in solvent concentration at polymerization temperatures both below and above the Tg of the polymer produced. For a mechanistic model this would involve many complex steps and a large number of adjustable parameters. It appears that the only realistic solution is to develop a semi-empirical model. In this context the free-volume theory appears to be a good starting point. [Pg.49]

A new rate model for free radical homopolymerization which accounts for diffusion-controlled termination and propagation, and which gives a limiting conversion, has been developed based on ft ee-volume theory concepts. The model gives excellent agreement with measured rate data for bulk and solution polymerization of MMA over wide ranges of temperature and initiator and solvent concentrations. [Pg.58]

Figure 6, Ejfect of solvent concentration on the molecular weight-conversion rehtionships of a tubular-addition polymerization reactor of fix size using a specified initiator type. Each point along the curves represents an optimum initiator feed concentrationr-reactor jacket temperature combination, (kinetic parameters of the initiator Ea = 24,948 Kcal/mol In k/ = 26,494 In sec f = 0.5)... Figure 6, Ejfect of solvent concentration on the molecular weight-conversion rehtionships of a tubular-addition polymerization reactor of fix size using a specified initiator type. Each point along the curves represents an optimum initiator feed concentrationr-reactor jacket temperature combination, (kinetic parameters of the initiator Ea = 24,948 Kcal/mol In k/ = 26,494 In sec f = 0.5)...
Quaternary ammonium azides will displace halogens in a synthesis of alkyl azides. Dichloromethane has been used as a solvent, although this can slowly form diazido-methane which may be concentrated by distillation dining work-up, thereafter easily exploding [1]. An accident attributed to this cause is described, and acetonitrile recommended as a preferable solvent, supported polymeric azides, excess of which can be removed by filtration are also preferred in place of the tetrabutylam-monium salt [2]. A similar explosion was previously recorded when the quaternary azide was generated in situ from sodium azide and a phase transfer catalyst in a part aqueous system [3,4],... [Pg.160]

For instance, aromatic solvent vapours were determined with polyurethane MIPs combined with SAW transducers [124]. That is, first, the hydrophilic quartz surface of SAW was hydrophobized with NW-dimethylaminotrimethylsilane. Then a solution for polymerization was prepared by mixing functional monomers, such as 4,4 -dihydroxydiphenyldimethylmethane, 4,4 -diisocyanatodiphenylmethane and 30% 2,4,4 -triisocyanatodiphenylmethane, with the 1,3,5-trihydroxybenzene crosslinker in the ethyl acetate or ethanol template used also as the solvent for polymerization. Subsequently, the hydrophobized resonator surface was spin-coated with an aliquot of this solution. Finally, the free-radical polymerization has been initiated thermally to form a polyurethane MIP film. The desired vapour concentration and relative humidity of the analyte were achieved by mixing dry air and saturated steam with solvent vapours generated with thermoregulated bubblers. [Pg.215]

Summarizing, aminosilanes show a fast adsorption on the silica surface. An equilibrium monolayer coating is formed. Modification in aqueous solvent causes polymerization on top of the initial monolayer. For modification from organic solvent, the reactions can be better controlled. With the bifunctional AEAPTS, a secondary silane layer adsorbs on the free primary amine groups of the first monolayer. At high concentration and after long reaction times, for both aminosilane types, a further non-specific deposition occurs. [Pg.218]

These indicate that the graft polymerization took place between cellulose radicals and monomers. The chain length decreased with increasing the solvent concentrations and were markedly affected by solvent used. [Pg.124]

Low-angle X-ray diffraction and electron microscopy have demostrated that SB copolymers exhibit mesophases in different solvents for solvents concentrations smaller than about 45% and that the periodic structure of the mesophases in neither destroyed by slow evaporation of the solvent, nor by polymerization of the solvent66 71. ... [Pg.100]

For MMA concentrations smaller than about 45%, the structure is lamellar (see Fig. 23 a, corresponding to a concentration of 28% of the added MMA). For solvent concentrations higher than 45%, droplets of the polymerized monomer appear and their size and their number increase with dilution as can be seen on Figs. 23 b and... [Pg.112]

The study by low-angle X-ray scattering, electron microscopy, and differential scanning calorimetry of the mesophases obtained by dissolution of BSB copolymers in preferential solvents for the polystyrene block and of dry BSB copolymers obtained by slow evaporation of the solvent from the mesophases has allowed to establish the respective effect of different factors which control the structure of the mesophases and their geometrical parameters. It has been shown that the nature, concentration, polymerization of the solvent, and temperature have the same effect on BSB copolymers as on SB copolymers35,88-91. ... [Pg.117]

Using anionic polymerization in THF solution and with diphenylmethylsodium as initiator, Grosius et al.2ls have synthetized block copolymers poly(vinyl-2-pyridine)-poly(vinyl4-pyridine). They have studied by low-angle X-ray scattering the structure of a copolymer V 2 P V 4 P with molecular weight of the blocks 15000 and 8000 respectively. In octanol, they have found a lamellar and a cylindrical structure as a function of solvent concentration. In THF, dioxan, and benzene they have only found a cylindrical structure. [Pg.136]

Effect of Solvent. Besides polymerizing in DMSO solvent, we also polymerized bisphenol A with 4,4 -dichlorodiphenylsulfone in the following solvents (a) mixtures of DMSO and chlorobenzene (b) di-methylacetamide (DMAc) (c) dimethylformamide (DMF) (d) hexa-methylphosphoramide. We found that the reaction rate constant (k2) was the same in the chlorobenzene-DMSO mixtures as in pure DMSO. However, if the chlorobenzene concentration was too high, the solubility of the bisphenol-A-diphenoxide salt was reduced, thereby precipitating some of the salt and effecting a slower polymerization. At a monomer concentration of 0.075M, the critical chlorobenzene concentration for precipitation was found to be between 35 and 50 vol. % at 100 °C. [Pg.718]

The key problems in a polymerization CSTR are the determination and characterization of micro- and macromixing, and the possibility of multiple steady states due to the exothermic nature of the reactions. Recent studies of CSTRs for bulk or solution free-radical polymerization indicate the possibility of multiple steady states due to the large heat evolution and difficult heat transfer that are characteristic of the reactors. Furthermore, even in simple solution polymerization (for example, in methyl methacrylate polymerization in ethyl acetate solvent), autocatalytic kinetics can lead to runaway conditions even with perfect temperature control for certain combinations of solvent concentration and reactor residence time. In practice, the heat evolution can be an additional source of autocatalytic behavior. [Pg.143]

In dilute solutions and in the more strongly donor solvents, monomeric species predominate but in Et20, at high Mg concentrations, polymeric species are present. The equilibria have been studied by nmr and by EXAFS4 spectra. [Pg.129]

Styrene polymerization initiated by trifluoroacetic acid can be used as a standard in demonstrating the effects of solvent and concentration. Polymerization is favored in more polar solvents and at high acid concentration [101]. Only the 1 1 adduct is formed when acid is slowly added to styrene [100]. However, fast polymerization occurs when styrene is added to the concentrated acid [Eq. (24)]. [Pg.169]

There is also a more general consequence of Rp varying as kplktl/1. If a monomer is polymerized in dilute solution, the kinetics follows the predicted first-order dependence on monomer concentration. In concentrated solutions, or in bulk polymerizations, where a pot full of monomer undiluted by solvent is polymerized, there is often a big acceleration in the polymerization rate at some point For monomers such as methyl acrylate, this can occur after conversions of just 1% and can result in an explosion (as illustrated schematically in Figure 4-18) ... [Pg.102]

Fig. 30. Kinetics of ethylene polymerization with the catalyst system TiCl4/MgCl2 — TEA at different TEA concentrations. (Polymerization conditions T = 70 °C, P = 1.05 bar, Ti = 0.05 mmol/1, solvent = n-heptane)... Fig. 30. Kinetics of ethylene polymerization with the catalyst system TiCl4/MgCl2 — TEA at different TEA concentrations. (Polymerization conditions T = 70 °C, P = 1.05 bar, Ti = 0.05 mmol/1, solvent = n-heptane)...
Local motions which occur in macromolecular systems can be probed from the diffusion process of small molecules in concentrated polymeric solutions. The translational diffusion is detected from NMR over a time scale which may vary from about 1 to 100 ms. Such a time interval corresponds to a very large number of elementary collisions and a long random path consequently, details about mechanisms of molecular jump are not disclosed from this NMR approach. However, the dynamical behaviour of small solvent molecules, immersed in a polymer melt and observed over a long time interval, permits the determination of characteristic parameters of the diffusion process. Applying the Langevin s equation, the self-diffusion coefficient Ds is defined as... [Pg.31]


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Polymerizing solvent

Solvent concentration

Solvents polymerization

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