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Polymerization and Copolymerization

In principle, it is possible to polymerize chloroprene by anionic-, cationic-, and Ziegler Natta catalysis techniques [4] but because of the lack of useful properties, production safety, and economical considerations, free radical emulsion polymerization is [Pg.3]

Disadvantages Expensive feedstock Process difficult to control [Pg.4]

Chloroprene in the form of an aqueous emulsion is converted with the aid of radical initiators into homopolymers or, in the presence of comonomers, into copolymers [5]. [Pg.4]

Comonomers, which have been used with success, are those with chemical strucmres similar to that of chloroprene, in particular [Pg.4]

3-Dichloro-butadiene to reduce the crystallization tendency, that is, the stiffness of the chain. [Pg.4]


Chemical Properties. Higher a-olefins are exceedingly reactive because their double bond provides the reactive site for catalytic activation as well as numerous radical and ionic reactions. These olefins also participate in additional reactions, such as oxidations, hydrogenation, double-bond isomerization, complex formation with transition-metal derivatives, polymerization, and copolymerization with other olefins in the presence of Ziegler-Natta, metallocene, and cationic catalysts. All olefins readily form peroxides by exposure to air. [Pg.426]

The reactions of alkyl hydroperoxides with ferrous ion (eq. 11) generate alkoxy radicals. These free-radical initiator systems are used industrially for the emulsion polymerization and copolymerization of vinyl monomers, eg, butadiene—styrene. The use of hydroperoxides in the presence of transition-metal ions to synthesize a large variety of products has been reviewed (48,51). [Pg.104]

A great number of other aHyl compounds have been prepared, especially aHyl ethers and aHyl ether derivatives of carbohydrates and other polymers. They are made by the reaction of hydroxyl groups with aHyl chloride in the presence of alkaU (1). Polymerizations and copolymerizations are generally slow and incomplete. Products have only limited use in coatings, inks, and specialties. Properties of a few aHyl ethers are given in Table 10. [Pg.88]

Styrene is a colorless Hquid with an aromatic odor. Important physical properties of styrene are shown in Table 1 (1). Styrene is infinitely soluble in acetone, carbon tetrachloride, benzene, ether, / -heptane, and ethanol. Nearly all of the commercial styrene is consumed in polymerization and copolymerization processes. Common methods in plastics technology such as mass, suspension, solution, and emulsion polymerization can be used to manufacture polystyrene and styrene copolymers with different physical characteristics, but processes relating to the first two methods account for most of the styrene polymers currendy (ca 1996) being manufactured (2—8). Polymerization generally takes place by free-radical reactions initiated thermally or catalyticaHy. Polymerization occurs slowly even at ambient temperatures. It can be retarded by inhibitors. [Pg.476]

Monomethylacryloyl and vinylbenzyl derivatives of sucrose have been prepared as intermediates for polymers, and preparation of a range of copolymers of styrene and O-methjiacryloylsucrose has been described (114). Synthesis of 4- and 6-0-acryloylsucrose has been achieved by acid-catalyzed hydrolysis of 4,6-0-(l-ethoxy-2-propenyhdene)sucrose (76). These acryloyl derivatives have been polymerized and copolymerized with styrene (qv). [Pg.37]

Polymerization. The most important reaction of vinyl chloride is its polymerization and copolymerization in the presence of a radical-generating initiator. [Pg.414]

Bis(3-nitrofurazanoxymethyl)oxetane 221 was synthesized in 52% yield by base-promoted ring closure of the corresponding 3-hydroxy-l-propyl triflate, 219, which is readily available from the diol and triflic anhydride. Oxetane 221 can also be prepared in 74% yield by treatment of the trifurazanyl ether 220 with DBU. Polymerization and copolymerization reactions of oxetane 220 have also been investigated (97MI7) (Scheme 148). [Pg.139]

The synthetic methods of macromolecules having an active pendant group include (1) the transformation reactions of polymer and copolymers, and (2) polymerization and copolymerization of functional monomers having active pendant groups. The macromolecules, either in the shape of film or microbeads, can be used as the substrate. As we have mentioned previously, the rate of polymerization initiated with the Ce(IV) ion redox system is much faster than that initiated by Ce(l V) ion alone, as expressed in / r 1. Therefore, the graft... [Pg.547]

Butadiene is easily polymerized and copolymerized with other monomers. It reacts by addition to other reagents such as chlorine, hydrocyanic acid, and sulfur dioxide, producing chemicals of great commercial value. [Pg.256]

Considerable interest was placed on 2-vinylfuran in the years 1930-1950 and a number of patents and publications on its polymerization and copolymerization appeared. This work was aimed at exploring the potential of the new polymer and concentrated therefore, on descriptive aspects of its preparation, properties and possible applications (for bibliographies on this topic, see3, 80 81)). Little was done to shed light on the more fundamental aspects of the systems studied until about 20 years ago. The present publication reviews these later studies. [Pg.69]

The distinguishing features of the polymerization and copolymerization to these interesting monomers have been described in a number of papers48 49 There are, however, no systematic investigations described in the literature to study the laws governing the reaction of AN copolymerization with quartemary salts of substituted vinyl pyridines. [Pg.114]

Pulsed laser photolysis (PLP) has emerged as the most reliable method for extracting absolute rate constants for the propagation step of radical polymerizations,343 The method can be traced to the work of Aleksandrov el al.370 PLP in its present form owes its existence to the extensive work of Olaj and eoworkers 71 and the efforts of an 1UPAC working party/45"351 The method has now been successfully applied to establish rate constants, /rp(overall), for many polymerizations and copolymerizations. [Pg.217]

The major applications of catalytic chain transfer are in molecular weight control and in synthesis of macromonomcrs based on methacrylate esters. However, they have also been shown effective in polymerizations and copolymerizations of MAA, MAM, MAN, AMS, S and some other monomers. [Pg.310]

Propagation reactions in radical polymerization and copolymerization arc generally highly exothermic and can be assumed to be irreversible. Exceptions to this general rule arc those involving monomers with low ceiling temperatures (Section 4.5.1). The thermodynamics of copolymerization has been reviewed by Sawada.85... [Pg.353]

BPO is commonly used as an initiator for S polymerizations and copolymerizations and it has been reported that its use can lead to yellowing and impaired stability in PS.13 1 1 The initiation and termination pathways observed for S polymerization when BPO is used as initiator have been discussed in Sections 3.2 and 3.4.2.2.1. These give rise to benzoyloxy and phenyl end-groups as follows (Scheme 8.1). [Pg.415]

K. Takahashi et al, The Polymerization and Copolymerization of Nitro Alkyl Acrylates and Nitroalkyl Methacrylates , JApplPolymerSci... [Pg.323]

It can be polymerized and copolymerized with acrylates to give useful pro pint ingredients Refs 1) Beil, not found 2) S.F. Reed, USP 3427295 (1969) CA 70,96158 (1969)... [Pg.601]

Uses. There are about forty to fifty organic peroxides commercially available in more than seventy formulations designed for specific applications which include (1) initiators for vinyl monomer polymerizations, and copolymerizations of monomers such as vinyl chloride, ethylene, styrene, vinyl acetate, acrylics, fluoroolefms and buta-dienestyrene (2) curing agents for thermoset polyesters, styrenated alkyds and oils, silicone rubbers and poly allyl diglycol carbonates ... [Pg.681]

Thermal Rimaway in Chain-Addition Polymerizations and Copolymerizations... [Pg.15]

The objectives of this presentation are to discuss the general behavior of non isothermal chain-addition polymerizations and copolymerizations and to propose dimensionless criteria for estimating non isothermal reactor performance, in particular thermal runaway and instability, and its effect upon polymer properties. Most of the results presented are based upon work (i"8), both theoretical and experimental, conducted in the author s laboratories at Stevens Institute of Technology. Analytical methods include a Semenov-type theoretical approach (1,2,9) as well as computer simulations similar to those used by Barkelew LS) ... [Pg.15]

Tables IV and V contain appropriate balance equations for nonisothermal free-radical polymerizations and copolymerizations, which are seen to conform to equation 2k. Following the procedure outlined above, we obtain the CT s for homopolymerizations listed in Table VI. Corresponding CT s for copolymerizations can be. obtained in a similar way, and indeed the first and fourth listed in Table VII were. The remaining ones, however, were derived via an alternate route based upon the definitions in Table VI labeled "equivalent" together with approximate forms for pj, which were necessitated by application of the Semenov-type runaway analysis to copolymerizations, and which will subsequently be described. Some useful dimensionless parameters defined in terms of these CT s appear in Tables VIII, IX and X. Tables IV and V contain appropriate balance equations for nonisothermal free-radical polymerizations and copolymerizations, which are seen to conform to equation 2k. Following the procedure outlined above, we obtain the CT s for homopolymerizations listed in Table VI. Corresponding CT s for copolymerizations can be. obtained in a similar way, and indeed the first and fourth listed in Table VII were. The remaining ones, however, were derived via an alternate route based upon the definitions in Table VI labeled "equivalent" together with approximate forms for pj, which were necessitated by application of the Semenov-type runaway analysis to copolymerizations, and which will subsequently be described. Some useful dimensionless parameters defined in terms of these CT s appear in Tables VIII, IX and X.
BATCH MATERIAL BALANCE EQUATIONS FOR FREE-RADICAL POLYMERIZATIONS AND COPOLYMERIZATIONS... [Pg.22]

Benvenuti M and Lenz RW. Polymerization and copolymerization of beta-batyrolactone and benzyl-beta-malolactonate by aluminoxane catalyst. J Polym Sci, Part A Polym Chem, 1991, 29, 793. [Pg.250]

Yamashita, Y., Tsuda, T., Ishida, H., and Hasegawa, M., Polymerization and Copolymerization of e-Caprolactone, Koeyo Kagaku Zasshi, 71, 755-757, 1968. [Pg.114]

Table 2. Molecular parameters of polymers obtained by self-condensing vinyl polymerization and copolymerization... Table 2. Molecular parameters of polymers obtained by self-condensing vinyl polymerization and copolymerization...
M. N. Sunil Kumar. Review on polymeric and copolymeric pour point depressants for waxy crude oils and studies on bombay high crude oil. Quart J Tech Pap (Inst Petrol), pages 47-71, October-December 1989. [Pg.466]

Matsumoto, A. Free-Radical Crosslinking Polymerization and Copolymerization of Multivinyl Compounds. Vol. 123, pp. 41-80. [Pg.212]


See other pages where Polymerization and Copolymerization is mentioned: [Pg.80]    [Pg.476]    [Pg.61]    [Pg.62]    [Pg.547]    [Pg.551]    [Pg.106]    [Pg.195]    [Pg.211]    [Pg.400]    [Pg.50]    [Pg.16]    [Pg.21]    [Pg.32]    [Pg.190]    [Pg.161]    [Pg.679]    [Pg.107]    [Pg.166]    [Pg.291]    [Pg.437]   


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