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Isobutylene monomers polymerization

Monomers, such as ethylene, propylene, isobutylene, and isoprene, containing the carbon-carbon double bond undergo chain polymerization. Polymerization is initiated by radical, anionic or cationic catalysts (initiators) depending on the monomer. Polymerization involves addition of the initiating species R, whether a radical, cation, or anion, to the double bond followed by its propagation by subsequent additions of monomer... [Pg.10]

Isobutylene is polymerized under conditions where chain transfer to monomer is the predominant chain-breaking reaction. A 4.0-g sample of the polymer was found to decolorize 6.0 mL of an 0.01 M solution of bromine in carbon tetrachloride. Calculate the number-average molecular weight of the polyisobutylene. [Pg.461]

Traditional Ziegler-Natta and metallocene initiators polymerize a variety of monomers, including ethylene and a-olefins such as propene, 1-butene, 4-methyl-1-pentene, vinylcyclo-hexane, and styrene. 1,1-Disubstituted alkenes such as isobutylene are polymerized by some metallocene initiators, but the reaction proceeds by a cationic polymerization [Baird, 2000]. Polymerizations of styrene, 1,2-disubstituted alkenes, and alkynes are discussed in this section polymerization of 1,3-dienes is discussed in Sec. 8-10. The polymerization of polar monomers is discussed in Sec. 8-12. [Pg.682]

It is of interest to examine the reason for the absence of polymerization in the isobutylene-Al2Me6-n-pentane system. According to our NMR results, methyl group exchange is decidedly faster in the presence of isobutylene than in pure cyclopentane, and consequently if the isobutylene monomer itself is able to interact with Al2Me6, by analogy with... [Pg.320]

Table 3.4 and Table 3.5 show the degradation products of the polymeric isomeric butyl esters. It is apparent with the products of poly-n-butyl acrylate that the identification of w-butyl formate, n-butyl acetate, the saturated and unsaturated dimers extends the earlier reports of Grassie and co-workers [42]. The formation of n-butyl acetate is consistent with that of methyl acetate formation and is simple scission at the chain end and hydrogen addition. With polyisobutyl acrylate the formation of isobutylene monomer and oligomers occurs. [Pg.77]

Isobutylene monomer is directly used in the polymerization process for producing both butyl rubber (HR) and DIMS rubber. [Pg.456]

In cationic polymerization the active species is the ion which is formed by the addition of a proton from the initiator system to a monomer. For vinyl monomers the type of substituents which promote this type of polymerization are those which are electron supplying, like alkyl, 1,1-dialkyl, aryl, and alkoxy. Isobutylene and a-methyl styrene are examples of monomers which have been polymerized via cationic intermediates. [Pg.411]

Thermoplastic resins produced from pure monomers such as styrene, alkyl-substituted styrenes, and isobutylene are produced commercially. An advantage of these resins is the fact that they are typically lighter in color than Gardner 1 (water-white) without being hydrogenated. Among the earliest resins in this category were those made from styrene and sold as Piccolastic. Styrene and alkyl-substituted styrenes such as a-methylstyrene are very reactive toward Friedel-Crafts polymerization catalysts. [Pg.355]

With the avadabihty of polymerization catalysts, extensive efforts were devoted to developing economical processes for manufacture of isoprene. Several synthetic routes have been commercialized. With natural mbber as an alternative, the ultimate value of the polymer was more or less dictated by that market. The first commercial use of isoprene in the United States started in 1940. It was used as a minor comonomer with isobutylene for the preparation of butyl mbber. Polyisoprene was commercialized extensively in the 1960s (6). In the 1990s isoprene is used almost exclusively as a monomer for polymerization (see ELASTOLffiRS,SYNTHETic-POLYisoPRENE). [Pg.462]

Butyl and Halobutyl Rubber. Butyl mbber is made by the polymerization of isobutylene a small amount of isoprene is added to provide sites for curing. It is designated HR because of these monomers. Halogenation of butyl mbber with bromine or chlorine increases the reaction rate for vulcanization and laminates or blends of halobutyl are feasible for production of mbber goods. It is estimated that of the - 100 million kg of butyl (UR) and halobutyl (HIIR) mbber in North America, over 90% is used in tire apphcations. The halogenated polymer is used in the innerliner of tubeless tires. Butyl mbber is used to make innertubes and curing bladders. The two major suppHers of butyl and halobutyl polymers in North America are Exxon and Bayer (see ELASTOLffiRS,SYNTHETIC-BUTYLrubber). [Pg.232]

Monomers for manufacture of butyl mbber are 2-methylpropene [115-11-7] (isobutylene) and 2-methyl-l.3-butadiene [78-79-5] (isoprene) (see Olefins). Polybutenes are copolymers of isobutylene and / -butenes from mixed-C olefin-containing streams. For the production of high mol wt butyl mbber, isobutylene must be of >99.5 wt % purity, and isoprene of >98 wt % purity is used. Water and oxygenated organic compounds iaterfere with the cationic polymerization mechanism, and are minimized by feed purification systems. [Pg.480]

Cationic polymerizations work better when the monomers possess an electron-donating group that stabilizes the intermediate carbocation. For example, isobutylene produces a stable carbocation, and usually copolymerizes with a small amount of isoprene using cationic initiators. The product polymer is a synthetic rubber widely used for tire inner tubes ... [Pg.307]

The initiator can be a radical, an acid, or a base. Historically, as we saw in Section 7.10, radical polymerization was the most common method because it can be carried out with practically any vinyl monomer. Acid-catalyzed (cationic) polymerization, by contrast, is effective only with vinyl monomers that contain an electron-donating group (EDG) capable of stabilizing the chain-carrying carbocation intermediate. Thus, isobutylene (2-methyl-propene) polymerizes rapidly under cationic conditions, but ethylene, vinyl chloride, and acrylonitrile do not. Isobutylene polymerization is carried out commercially at -80 °C, using BF3 and a small amount of water to generate BF3OH- H+ catalyst. The product is used in the manufacture of truck and bicycle inner tubes. [Pg.1207]

Thus with aMeSt, the kinetic chain is relatively short, monomer is consumed mainly by initiation and propagation, and chain transfer by the HSiCCHj CH H C Q initiator is unfavorable (see Sect. III.B.3.b.i.). In contrast, with isobutylene the kinetic chain may live longer because it is sustained by thermodynamically favorable chain transfer by the initiator. Scheme 5 illustrates the mechanism of isobutylene polymerization by the HSi(CH3)2CH2CH29>CH2Cl/Me3Al system. The kinetic chain is sustained by chain transfer loops shown on the left margin of the Scheme. [Pg.41]

Table 12. The effect of monomer concentration on the polymerization of isobutylene using the HSi(CH3)2CH2CH2y>CH2Cl/Me3Al initiating system... Table 12. The effect of monomer concentration on the polymerization of isobutylene using the HSi(CH3)2CH2CH2y>CH2Cl/Me3Al initiating system...
The effect of monomer concentration was studied using n-pentane solvent and maintaining the total volume of isobutylene plus n-pentane constant. Methyl halide concentration was kept constant so as to maintain constant medium polarity. Attempts were made to keep conversions below 20%. At -30 °C, due to almost explosive polymerizations, conversions could only be maintained below 40%. [Pg.90]

While the effect of monomer concentration [M] on Mv of PIB has been studied by a number of workers using a ariety of initiator systems11-13, such studies have not yet been carried out using M . The objective of this phase of research was to determine the effect of [M] on M and thus to calculate relative rate constants of isobutylene polymerization from GPC data. [Pg.121]

Another consequence of this hypothesis is that for every isobutylene polymerization system, there must exist three temperature regions over which molecular weight control is, respectively by termination, a combination of transfer to monomer and termination, and transfer to monomer alone although due to experimental limitations all three regions may not be possible to detect. [Pg.142]


See other pages where Isobutylene monomers polymerization is mentioned: [Pg.196]    [Pg.470]    [Pg.79]    [Pg.13]    [Pg.3]    [Pg.18]    [Pg.59]    [Pg.189]    [Pg.61]    [Pg.160]    [Pg.907]    [Pg.77]    [Pg.563]    [Pg.246]    [Pg.480]    [Pg.483]    [Pg.320]    [Pg.41]    [Pg.44]    [Pg.48]    [Pg.85]    [Pg.85]    [Pg.86]    [Pg.89]    [Pg.102]    [Pg.138]    [Pg.140]    [Pg.142]    [Pg.142]   
See also in sourсe #XX -- [ Pg.102 ]




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