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Reactions copolymerization

It is apparent from items (l)-(3) above that linear copolymers-even those with the same proportions of different kinds of repeat units-can be very different in structure and properties. In classifying a copolymer as random, alternating, or block, it should be realized that we are describing the average character of the molecule accidental variations from the basic patterns may be present. In Chap. 7 we shall see how an experimental investigation of the sequence of repeat units in a copolymer is a valuable tool for understanding copolymerization reactions. This type of information along with other details of structure are collectively known as the microstructure of a polymer. [Pg.12]

These observations suggest how the terminal mechanism can be proved to apply to a copolymerization reaction if experiments exist which permit the number of sequences of a particular length to be determined. If this is possible, we should count the number of Mi s (this is given by the copolymer composition) and the number of Mi Mi and Mi Mi Mi sequences. Specified sequences, of any definite composition, of two units are called dyads those of three units, triads those of four units, tetrads those of five units, pentads and so on. Next we examine the ratio NmjMi/Nmi nd NmjMiMi/NmiMi If these are the same, then the mechanism is shown to have terminal control if not, it may be penultimate control. To prove the penultimate model it would also be necessary to count the number of Mi tetrads. If the tetrad/triad ratio were the same as the triad/dyad ratio, the penultimate model is proved. [Pg.456]

Transfer reactions, analogous to those discussed for homopolymer, also occur during the copolymerization reaction and result in formate end groups. [Pg.58]

Polymerization and Spinning Solvent. Dimethyl sulfoxide is used as a solvent for the polymerization of acrylonitrile and other vinyl monomers, eg, methyl methacrylate and styrene (82,83). The low incidence of transfer from the growing chain to DMSO leads to high molecular weights. Copolymerization reactions of acrylonitrile with other vinyl monomers are also mn in DMSO. Monomer mixtures of acrylonitrile, styrene, vinyUdene chloride, methallylsulfonic acid, styrenesulfonic acid, etc, are polymerized in DMSO—water (84). In some cases, the fibers are spun from the reaction solutions into DMSO—water baths. [Pg.112]

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 water solubilities of the functional comonomers are reasonably high since they are usually polar compounds. Therefore, the initiation in the water phase may be too rapid when the initiator or the comonomer concentration is high. In such a case, the particle growth stage cannot be suppressed by the diffusion capture mechanism and the solution or dispersion polymerization of the functional comonomer within water phase may accompany the emulsion copolymerization reaction. This leads to the formation of polymeric products in the form of particle, aggregate, or soluble polymer with different compositions and molecular weights. The yield for the incorporation of functional comonomer into the uniform polymeric particles may be low since some of the functional comonomer may polymerize by an undesired mechanism. [Pg.216]

A number of metal chelates containing transition metals in their higher oxidation states are known to decompose by one electron transfer process to generate free radical species, which may initiate graft copolymerization reactions. Different transition metals, such as Zn, Fe, V, Co, Cr, Al, etc., have been used in the preparation of metal acetyl acetonates and other diketonates. Several studies demonstrated earlier that metal acetyl acetonates can be used as initiators for vinyl polymeriza-... [Pg.487]

Recently, Si et al. [59,60] have investigated the synthesis of polymerizable amines, such as N-(3-dimethyl-aminopropyl) acrylamide(DMAPAA) and N-(3-dimeth-ylaminopropyl) methacrylamide (DMAPMA), and their copolymerization reaction. DMAPAA or DMAPMA in conjunction with ammonium persulfate was used as a redox initiator for vinyl polymerization. Copolymers having amino pendant groups, such as copolymer of... [Pg.552]

The number of aldehyde groups in the copolymers of type 5 has been found to be always smaller than that of cyanogroups. This is a characteristic feature of the copolymerization of AN with 4. An especially great difference is observed when the copolymerization reaction is carried out in benzene and DMF at elevated temperatures. In this case the content of aldehyde groups amounts to only 50—60% of the amount of aldehyde groups calculated from the nitrogen content in the copolymers19. ... [Pg.103]

Reactivity ratios for the copolymerization of AN with 7 in methanol at 60 °C, proved to be equal to rx AN= 3,6 0,2 and r%n = 0 0,06, i.e., AN is a much more active component in this binary system. The low reactivity of the vinyl double bond in 7 is explained by the specific effect of the sulfonyl group on its polarity26. In addition to that, the radical formed from 7 does not seem to be stabilized by the sulfonyl group and readily takes part in the chain transfer reaction and chain termination. As a result of this, the rate of copolymerization reaction and the molecular mass of the copolymers decrease with increasing content of 7 in the initial mixture. [Pg.106]

The kinetic order of the copolymerization reaction with respect to the initiator is equal to 0,5, and the total activation energy amounts to 14,4 kcal/mol (60,3 kJ/mol). [Pg.109]

The various copolymerization models that appear in the literature (terminal, penultimate, complex dissociation, complex participation, etc.) should not be considered as alternative descriptions. They are approximations made through necessity to reduce complexity. They should, at best, be considered as a subset of some overall scheme for copolymerization. Any unified theory, if such is possible, would have to take into account all of the factors mentioned above. The models used to describe copolymerization reaction mechanisms arc normally chosen to be the simplest possible model capable of explaining a given set of experimental data. They do not necessarily provide, nor are they meant to be, a complete description of the mechanism. Much of the impetus for model development and drive for understanding of the mechanism of copolymerization conies from the need to predict composition and rates. Developments in models have followed the development and application of analytical techniques that demonstrate the inadequacy of an earlier model. [Pg.337]

The synthetic techniques leading to the formation of siloxane containing linear or graft copolymers will be classified according to the type and nature of the copolymerization reactions as shown below. [Pg.28]

Using copolymerization theory and well known phase equilibrium laws a mathematical model is reported for predicting conversions in an emulsion polymerization reactor. The model is demonstrated to accurately predict conversions from the head space vapor compositions during copolymerization reactions for two commercial products. However, it appears that for products with compositions lower than the azeotropic compositions the model becomes semi-empirical. [Pg.305]

Development of a reduced-order model for metallocene-catalyzed ethylene-norbornene copolymerization reaction... [Pg.845]

Copolymerization reactions with p-methoxy-a-methylstyrene were also attempted at 0°C, and a methanol-insoluble product having an Mjj of 1600 was obtained over a period of 36 h. From the 250-MHz 1h-NMR spectrum, it was found that p-methoxy-a-methylstyrene was present in the polymer to the extent of 14%. [Pg.457]


See other pages where Reactions copolymerization is mentioned: [Pg.367]    [Pg.367]    [Pg.400]    [Pg.315]    [Pg.177]    [Pg.482]    [Pg.62]    [Pg.217]    [Pg.217]    [Pg.218]    [Pg.222]    [Pg.486]    [Pg.489]    [Pg.506]    [Pg.112]    [Pg.8]    [Pg.25]    [Pg.51]    [Pg.51]    [Pg.51]    [Pg.52]    [Pg.54]    [Pg.55]    [Pg.57]    [Pg.845]    [Pg.679]    [Pg.185]    [Pg.290]    [Pg.291]    [Pg.292]    [Pg.458]    [Pg.459]   
See also in sourсe #XX -- [ Pg.217 ]

See also in sourсe #XX -- [ Pg.185 ]

See also in sourсe #XX -- [ Pg.106 ]

See also in sourсe #XX -- [ Pg.88 , Pg.134 ]




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Block copolymerization radical reactions

Chain copolymerization anionic reaction

Chain copolymerization cationic reaction

Chain copolymerization radical reaction

Chain copolymerization ring-opening reaction

Chain-reaction polymerization copolymerization

Constant rate copolymerization reaction

Copolymerization coupling reactions

Copolymerization reaction media

Copolymerization reactions, acid

Copolymerization, reaction rate

Different Reaction Conditions for Graft Copolymerization

Emulsion copolymerization reaction

Epoxide copolymerization reaction

Free radical copolymerization chain extension reactions

Free radical reactions, graft copolymerization

Free-radical copolymerization, transfer reactions

Graft copolymerization reaction

In-line monitoring of a copolymerization reaction

Kinetics copolymerization reactions

Model copolymerization reactions

Quantitative reactivity studies copolymerization reactions

Radical reactions, copolymerizations

Reaction mechanism copolymerization

Redox copolymerization reactions

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