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Polymerisation block

A peculiar and intriguing effect of polysarcosine, which was used as an initiator of block polymerisation, was observed by Ballard and Bamford (101). Their results are shown in Fig. 21 and indicate that the initial rates of D,L-phenyl alanine NCA polymerisation are affected by the degree of polymerisation of the initiator. For a constant monomer concentration and a constant concentration of the initiating amine the... [Pg.60]

As shown in Table 9 acetylation of polysarcosine destroys the effect and the addition of such a polymer to phenylalanine dimethyl amide only slightly accelerates the process. (5) No effect is observed when sarcosine NCA is block-polymerised in poly-D.L-phenylalanine. [Pg.61]

Since oxiranes are representative heterocyclic monomers containing an endo-cyclic heteroatom, and the most commonly polymerised of such monomers, they have been subjected to copolymerisations with heterocyclic monomers containing both an endocyclic and an exocyclic heteroatom. Coordination copolymerisations of heterocyclic monomers with different functions are focused on oxirane copolymerisation with cyclic dicarboxylic acid anhydride and cyclic carbonate. However, the statistical copolymerisation of heterocyclic monomers with an endocyclic heteroatom and monomers with both endocyclic and exocyclic heteroatoms have only a limited importance. Also, the block copolymerisation of oxirane with lactone or cyclic dicarboxylic acid anhydride is of interest both from the synthetic and from the mechanistic point of view. Block copolymerisation deserves special interest in terms of the exceptionally wide potential utility of block copolymers obtained from comonomers with various functions. It should be noted, however, that the variety of comonomers that might be subjected to a random, alternating and block polymerisation involving a nucleophilic attack on the coordinating monomer is rather small. [Pg.467]

In this study, the quantitatively kinetic model for linear block polymerisation up to a high degree of conversion is proposed on the basis of experimental material concerns to kinetics of photoinitiated polymerisation of glycidyl methacrylate (GMA) obtained over a wide range of variation of the available parameters. [Pg.103]

The observed generality (for example, order increasing npon initiator) are the kinetic features for block polymerisation up to the high degrees of conversions of matrix photopolymerisation [35]. Also for polymerisation in the presence of porous fillers [36] or at adsorption immobilisation on the carrier snrface of the polymeric initiator [37], and these indicate that the solid phase creates the special ordered structure of the reaction space, in which the transmitting and segmental mobility of macroradicals are sharply reduced. That is why polymerisation in the ordered reaction space can proceed in accordance with other kinetic regularities, rather than in liquid monomer space. [Pg.126]

The fluorine-containing polymers for materials with complete internal light-reflection are reviewed. The general kinetic control features for the synthesis of block polymerisation fluoroalkylmethacrylates (FMA), their copolymerisation with different vinyl monomers, their relative activity and the polymerisation of FMA in presence of nitroxyl radicals are discussed. The basic properties of the more frequently used FMA for materials with complete internal light-reflection, are characterised. The new optical transparent fluorine polymers, also containing per-fluorinated cyclobutane and aromatic fragments are reviewed. Data from the literature and original results are presented. [Pg.209]

Due to good optical and rheological characteristics, homopolymers of fluorine-containing methacrylates and their copolymers with other methacrylates are more often used in fibre-optic practice [2, 20-24, 26-34]. But selection of a polymer with the best optical and mechanical properties requires establishment of the dependence of the structure and properties of the polymers on the structure and reactivity of initial monomers. To solve this problem the study of the kinetics of block polymerisation and copolymerisation process of fluoroalkyl-(meth)acrylates is desirable. [Pg.213]

Monoliths Block polymerisate of various methacrylates and agglomerated silica Extremely high speed Uno, BioRad CIM, BIA... [Pg.302]

N-Alkylpyrroles may be obtained by the Knorr synthesis or by the reaction of the pyrrolyl metallates, ie, Na, K, and Tl, with alkyl haUdes such as iodomethane, eg, 1-methylpyrrole [96-54-8]. Alkylation of pyrroles at the other ring positions can be carried out under mild conditions with allyhc or hensylic hahdes or under more stringent conditions (100—150°C) with CH I. However, unless most of the other ring positions are blocked, poly alkylation and polymerisation tend to occur. N-Alkylation of pyrroles is favored by polar solvents and weakly coordinating cations (Na", K" ). More strongly coordinating cations (Li", Mg " ) lead to more C-alkylation. [Pg.357]

Considerable advances have taken place in the 1990s with regard to cationic polymerisation of styrene. Its uses to make block copolymers and even living cationic polymerisation have been reported (171). [Pg.518]

SASOLII a.ndIII. Two additional plants weie built and aie in operation in South Africa near Secunda. The combined annual coal consumption for SASOL II, commissioned in 1980, and SASOL III, in 1983, is 25 x 10 t, and these plants together produce approximately 1.3 x lO" m (80,000 barrels) per day of transportation fuels. A block flow diagram for these processes is shown in Figure 15. The product distribution for SASOL II and III is much narrower in comparison to SASOL I. The later plants use only fluid-bed reactor technology, and extensive use of secondary catalytic processing of intermediates (alkylation, polymerisation, etc) is practiced to maximise the production of transportation fuels. [Pg.292]

Anionic polymerisation techniques aie one of many ways to synthesise a special class of block copolymers, lefeiied to as star block copolymers (eq. 25) (33). Specifically, a "living" SB block is coupled with a silyl haUde coupling agent. The term living polymerisation refers to a chain polymerisation that proceeds in the absence of termination or transfer reactions. [Pg.180]

Step-Growth Gopolymerization. A sample of a block copolymer prepared by condensation polymerisation is shown in equation 30 (37). In this process, a prepolymer diol (HO—Z—OH) is capped with isocyanate end groups and chain extended with a low molecular-weight diol (HO—E—OH) to give a so-called segmented block copolymer, containing polyurethane hard blocks and O—Z—O soft blocks. [Pg.180]

A copolymer is made by polymerisation of two monomers, adding them randomly (a random copolymer) or in an ordered way (a block copolymer). An example is styrene-butadiene rubber, SBR. Styrene, extreme left, loses its double bond in the marriage butadiene, richer in double bonds to start with, keeps one. [Pg.53]

In the absence of impurities there is frequently no termination step in anionic polymerisations. Hence the monomer will continue to grow until all the monomer is consumed. Under certain conditions addition of further monomer, even after an interval of several weeks, will eause the dormant polymerisation process to proceed. The process is known as living polymerisation and the products as living polymers. Of particular interest is the fact that the follow-up monomer may be of a different species and this enables block copolymers to be produced. This technique is important with certain types of thermoplastic elastomer and some rather specialised styrene-based plastics. [Pg.36]

Tbe system may be used for homopolymers and for block copolymers. Some commercial SBS triblock thermoplastic rubbers and the closely related K-resins produced by Phillips are of this type. Anionic polymerisation methods are of current interest in the preparation of certain diene rubbers. [Pg.37]

When casting large blocks, the exotherm problem is more severe and it may be necessary to polymerise inside a pressure vessel and thus raise the boiling point of the monomer. [Pg.403]

Closely related to these but thermoplastic rather than rubber-like in character are the K-resins developed hy Phillips. These resins comprise star-shaped butadiene-styrene block copolymers containing about 75% styrene and, like SBS thermoplastic elastomers, are produced by sequential anionic polymerisation (see Chapter 2). [Pg.451]

Cobalt naphthenate is generally supplied in solution in styrene, the solution commonly having a cobalt concentration of 0.5-1.0%. The cobalt solution is normally used in quantities of 0.5-4.0% based on the polyester. The accelerator solution is rather unstable as the styrene will tend to polymerise and thus although the accelerator may be metered from burettes, the latter will block up unless frequently cleaned. Cobalt naphthenate solutions in white spirit and dimethyl phthalate have proved unsatisfactory. In the first case dispersion is difficult and laminates remain highly coloured whilst with the latter inferior end-products are obtained and the solution is unstable. Stable solutions of cobalt octoate in dimethyl phthalate are possible and these are often preferred because they impart less colour to the laminate. [Pg.703]

Fig. 4. The effect of chain pull-out of PVP on for three PS-PVP diblocks whose PVP block varied from degree of polymerisation 49 to 220 [4]. Fig. 4. The effect of chain pull-out of PVP on for three PS-PVP diblocks whose PVP block varied from degree of polymerisation 49 to 220 [4].
Methods of synthesising these polymers are available and may include polymerisation of low molar mass units ( blocks ) of homopolymer which are later reacted together to yield the copolymer. [Pg.39]

Dimitrov I, Schlaad H (2003) Synthesis of nearly monodisperse polyst3Tene-polypeptide block copolymers via polymerisation of N-carboxyanhydrides. Chem Commun 2944—2945... [Pg.24]

Fig. 3 Industrial pilot plant (10 t a ) with three micro-reactor blocks for radical polymerisation at the Idemitsu site in Japan [16],... Fig. 3 Industrial pilot plant (10 t a ) with three micro-reactor blocks for radical polymerisation at the Idemitsu site in Japan [16],...
ROMP is without doubt the most important incarnation of olefin metathesis in polymer chemistry [98]. Preconditions enabling this process involve a strained cyclic olefinic monomer and a suitable initiator. The driving force in ROMP is the release of ring strain, rendering the last step in the catalytic cycle irreversible (Scheme 3.6). The synthesis of well-defined polymers of complex architectures such as multi-functionaUsed block-copolymers is enabled by living polymerisation, one of the main benefits of ROMP [92, 98]. [Pg.82]


See other pages where Polymerisation block is mentioned: [Pg.76]    [Pg.19]    [Pg.101]    [Pg.44]    [Pg.27]    [Pg.76]    [Pg.19]    [Pg.101]    [Pg.44]    [Pg.27]    [Pg.323]    [Pg.304]    [Pg.332]    [Pg.363]    [Pg.498]    [Pg.347]    [Pg.466]    [Pg.384]    [Pg.310]    [Pg.479]    [Pg.339]    [Pg.203]    [Pg.152]    [Pg.35]    [Pg.26]    [Pg.153]    [Pg.410]    [Pg.24]   


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Block copolymers atom transfer radical polymerisation

Block copolymers from radical polymerisation

Block emulsion polymerisation

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