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Polymerization compared with conventional

Cationic polymerization with Lewis acids yields resinous homopolymers containing cycHc stmctures and reduced unsaturation (58—60). Polymerization with triethyl aluminum and titanium tetrachloride gave a product thought to have a cycHc ladder stmcture (61). Anionic polymeriza tion with lithium metal initiators gave a low yield of a mbbery product. The material had good freeze resistance compared with conventional polychloroprene (62). [Pg.540]

The net result is that the rate of polymerization is lower by about a factor of 10, when polysilanes are compared with conventional photoinitiators such as benzoin methyl ether. [Pg.17]

Polymerization conditions with temperatures of 60 °C were mild compared with conventional ATRP in solution, where typically temperatures around 100 °C are applied. Despite these mild conditions, high polymerization rates and high conversion within only 3 h were achieved. Moreover, it could be demonstrated that the catalyst, being covalently bound to the surfactant, can easily be removed by filtering off the latex and subsequent washing with methanol. By this procedure the copper content of the resulting PMMA was reduced from the theoretical value of 0.73% to 0.06% and the polymer appeared colorless while the washing fraction was colored [65]. [Pg.293]

Table 1. Kinetic parameters of some macromonomers in radical polymerization as compared with conventional monomers ... Table 1. Kinetic parameters of some macromonomers in radical polymerization as compared with conventional monomers ...
The styrene is a high-purity product, suitable for polymerization, at a very attractive cost compared with conventional styrene production routes. If desired, the mixed xylenes can also be extracted from the pygas, upgrading their value as chemical feedstock. The process is economically attractive for typical pygas and supplemental feeds, which contain 15,000 tpy or more styrene. [Pg.191]

Recently, biodiesel has been used as a solvent in free radical-initiated polymerization reactions (Figure 5.8). It should be noted that in contrast to polymerization reactions in some other green solvents, including SCCO2, there is no need to modify the initiator for reactions in biodiesel. All the resulting polymers except poly(methyl methacrylate) were soluble in the biodiesel. Lower molecular weights were obtained compared with conventional polymerization... [Pg.107]

In a study, copper-catalyzed radical copolymerization of nBA and methacryloxy-capped poly(MMA) was compared with conventional radical copolymerization.267 431 The graft copolymers G-l obtained with copper catalysts are more homogeneous in terms of MWD (Mw/Mn 1.6 vs 3) and the number of side chains. This is attributed to diffusion control being less important in the metal-catalyzed radical polymerization, where the growing radical species is rapidly converted into the dormant covalent species. [Pg.503]

On the other hand, polymeric beads of supported ILs ( polymer-supported imidazolium salt, PSIS) were also prepared via the covalent anchoring of an imidazolium salt to a polystyrene resin.These PSISs, which have the advantage of significantly enhancing the nucleophilicity of metal salts compared with conventional methods, have been used as efficient catalysts for nucleophilic fiuorination and for other nucleophilic substitution reactions. In particular, the authors found that the applied PSIS had many practical merits product recovery and purification was simple and catalyst recovery and reuse were easy (Figure 4.12). [Pg.176]

Determination. GC two different SFE systems are compared high temperature method in some cases yields a more exhaustive extraction, but also less clean extracts whereas medium temperature may sometimes cause problems with quantitative recoveries, but it yields very clean extracts The use, advantages and disadvantages of silica sorbents, polymeric, functionalized, carbon-based and mixed available sorbents are discussed Determination. LC—MS best conditions, extraction solvent methanol—acetone (1 1, v/v) temperature 50°C pressure 1500 psi two static cycles recoveries >10%. LOD between 1 to 5 /ag/kg loss of volatile molecules is produce at elevated temperatures Determination GC-MS Best conditions extractant methanol temperature lOffC, pressure 100 atm combined with 15 min static and then 10 min dynamic recovery 111% (RSD 4%) and 106% (RSD 5%) extraction efficiency of the PLE was compared with conventional Soxhlet and bath ultrasonication GC-MS an extraction time of 1 h was employed. [Pg.115]

The methodology of active ester synthesis, as shown in Fig. 2, is generally applicable and covers a wide range of nucleophiles, including primary, secondary and aromatic amines, primary alcohols and phenols. Thus, chemical modification d polymeric active esters (i.e. active ester synthesis) provides a single-step route for the preparation of functional polymers in general. The syntl sis of various polymer types by the active ester method is advanced in Sects. 5-7. Here, an example of a relativdy simpk fiinctional group (OH) is discussed to illustrate the versatility of the active ester method, as compared with conventional methods of polymer functionalization. [Pg.5]

Polymeric micelles form stable pseudostationary phases with a critical micelle concentration of virtually zero (aggregation number of 1), and are tolerant of high organic solvent concentrations in the electrolyte solution. Mass transfer kinetics are slow compared with conventional surfactant micelles, and peak distortion from mass overloading is a problem for some polymer compositions. Preliminary studies indicate that polymeric surfactants are effective pseudostationary phases in micellar electrokinetic chromatography, but only a limited number of practical applications have been demonstrated, and uptake has been slow. [Pg.657]

Ritter et al. have synthesized a variety of (meth)acrylamides in good yields from (meth)acrylic acid and aliphatic and aromatic amines under solvent-free microwave irradiation conditions [14]. It was found that addition of a polymerization initiator (AIBN) to the reaction mixture led directly to poly(meth)acrylamides in a single step. In these polymerization procedures, 11.6 mmol methacrylic acid was mixed with 11.6 mmol amine and 0.58 mmol AIBN in a pressure-resistant test tube. The tubes were sealed and irradiated in a single-mode microwave reactor for 30 min at 140 W (Scheme 14.4). The experiments were performed without temperature control and were not compared with conventional conditions. [Pg.656]

This study revealed that under microwave conditions polymerization phenomena such as polymerization selectivity, polymerization temperature shift, and polymerization temperature shift as a result of the microwave power setting, can be observed when products are compared with those obtained under conventional conditions. To explain these phenomena it was proposed that a new dipole partition function is present in the microwave field, so values of thermodynamic properties such as internal energy and Gibbs free energy of materials with permanent dipole moments change under microwave conditions, which in turn leads to shifts in the reaction equilibrium and kinetics compared with conventional conditions at the same temperature [46]. [Pg.666]

Synthesis of conjugated p-phenylene ladder polymers by means of a microwave-assisted reaction has been achieved by Scherf et al. (Scheme 14.35) [72]. The polymerization reactions were performed in THE solution at 130 °C in the presence of palladium catalyst with phosphine ligands with irradiation in a single-mode micro-wave reactor for 11 min. Compared with conventional thermal procedures, the reaction time was reduced from days to a couple of minutes and molecular weight distributions ( PDI ca 1.8) of the polymers were changed substantially. [Pg.676]

The ring-opening polymerization (ROP) of p-dioxanone using triethylaluminum or tin powder as catalysts has also been performed solvent free using a scientific microwave unit (Scheme 3.6). Increased-molecular-weight products were obtained in shorter reaction times as compared with conventional heating. [Pg.61]

Polymeric nanocomposites are an important class of new emerging nanomaterials that exhibits remarkable improvanents of material properties compared with conventional micro- and macrocomposite materials. The small dimension of the filler particles and, accordingly, large surface of the phase separation give the final product characteristics, which considerably exceed traditional ones at minimal filler concentration (Mikitaev et al. 2008). The formation of the polymeric nanocomposite may be represented as the process of filling of the free space in disperse phase with polymer in the form of melt or solution or with monomer followed by its in situ polymerization by chemical or radiation influence on the formed composite structure. The scheme of the polymeric nanocomposite synthesis under radiation is shown in Figure 18.5. [Pg.428]

Miniemulsion is a special class of emulsion that is stabilized against coalescence by a surfactant and Ostwald ripening by an osmotic pressure agent, or costabilizer. Compared with conventional emulsion polymerization process, the miniemulsion polymerization process allows all types of monomers to be used in the formation of nanoparticles or nanocapsules, including those not miscible with the continuous phase. Each miniemulsion droplet can indeed be treated as a nanoreactor, and the colloidal stability of the miniemulsion ensures a perfect copy from the droplets to the final product. The versatility of polymerization process makes it possible to prepare nanocapsules with various types of core materials, such as hydrophilic or hydrophobic, liquid or solid, organic or inorganic materials. Different techniques can be used to initiate the capsule wall formation, such as radical, ionic polymerization, polyaddition, polycondensation, or phase separation from preformed polymers. [Pg.324]

Controlled anionic polymerization of alkyl methacrylates initiated by 1,1-diphenyUiexyllithium using a flow microreactor gives the corresponding poly (aUcyl methacrylate)s with high level of control of molecular weight under easily accessible temperatures compared with conventional batch macropolymerization, e.g., —28°C for methyl methacrylate (MMA) (MJMn = 1.16), 0°C for butyl methacrylate (BuMA) MJM = 1.24), and 24°C for tert-butyl methacrylate (f-BuMA) (Mw/Mn = 1.12). Precise control of the reaction temperature and fast mixing of a monomer and an initiator seem to be responsible (Fig. 16) [161]. [Pg.18]

This approach has been used to imprint theophylline [74], which was attached to the surface of silica gel particles and an imprinted polymer assembled around the inorganic particles. When polymerization was complete, the silica was dissolved away with hydrofluoric acid. This yielded imprinted polymer particles with a narrow pore size distribution with diameters between 254 and 257 A compared with conventionally prepared imprinted polymers which have pore diameters in the range 30-1000 A. The imprinted polymer showed a high selectivity for theophylline over the related compounds caffeine and theobromine. [Pg.273]


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Conventional polymerization

Polymerization, with

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