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Catalyst copolymer

This mechanism of initiation is confirmed by the fact that, when the PAN-PEO block copolymer is treated with diisocyanate in benzene in the presence of pyridine acting as catalyst, copolymers lose their solubility in DMF as a result of the formation of intermolecular chemical bonds75). [Pg.131]

Figure 4. Pulsed FT C-13 NMR spectrum of the polyalkane obtained by hydrogenating an alternating propylene butadiene copolymer made with a titanium catalyst, Copolymer B. The spectrum was obtained at ambient temperature from... Figure 4. Pulsed FT C-13 NMR spectrum of the polyalkane obtained by hydrogenating an alternating propylene butadiene copolymer made with a titanium catalyst, Copolymer B. The spectrum was obtained at ambient temperature from...
Hydride polyaddition of divinyl-containing compounds was carried out for various lengths of a,co-dihydridedimethylsiloxanes. The reaction run was searched by a decrease of active =Si-H groups concentration. It was found that for rhodium acetylacetonatedicarbonyl as a catalyst, copolymers soluble in organic solvents were obtained, which were structured after some time. This may be explained by the fact that in spite of polymers re-precipitated from toluene solution by methyl alcohol, rhodium catalyst remains in polymeric systems, which decompose and induce structuring (cross-linking) of copolymers. [Pg.159]

The polymerizations were carried out in refluxing o-dichlorobenzene in the presence of 2-hydroxypyridine as catalyst. In the absence of catalyst, only low-molecular-weight polymers (IV <0.3 dL/g) could be isolated from solution. However, when 2-hydroxypyridine was used as a condensation catalyst, copolymers having IVs in excess of 0.45 dL/g could be prepared readily. The results are summarized in Table I. [Pg.170]

Toxicology LD50 (oral, mouse) 408 mg/kg, (IP, mouse) 10 mg/kg, (subcut., mouse) 125 mg/kg poison by IP and subcut. routes mod. toxic by ing. mutagenic data TSCA listed Hazardous Decomp. Prods. Heated to decomp., emits very toxic fumes of HCI and NOx HMIS Health 3, Flammability 1, Reactivity 2 Uses Antioxidant reducing agent catalyst copolymer inhibitor preservative for photographic developers ammoniation reagent... [Pg.2124]

The organometallic polymer shown in scheme 3 was synthesized using phosphoric acid, persulfate, or azobisisobutyronitrile (AIBN) as catalyst. Copolymers prepared with methyl methacrylate, styrene, and chloroprene as well as the homopolymer were crosslinked with formaldehyde. These polymers rmderwent reversible chemical oxidation with ceric sulfate. [Pg.9]

Specifically chemical considerations are especially evident in Chap. 7, where copolymers and stereoregular polymers are discussed. Since two monomers are required for the formation of a copolymers, the differences in their reactivity affects both the composition of the product and the distribution of components in it. Likewise, the catalysts that produce stereoregularity are highly specific, highly reactive, and poorly understood chemical reagents. [Pg.265]

In spite of the assortment of things discussed in this chapter, there are also a variety of topics that could be included but which are not owing to space limitations. We do not discuss copolymers formed by the step-growth mechanism, for example, or the use of Ziegler-Natta catalysts to regulate geometrical isomerism in, say, butadiene polymerization. Some other important omissions are noted in passing in the body of the chapter. [Pg.424]

The weight percent propylene in ethylene-propylene copolymers for different Ziegler-Natta catalysts was measuredt for the initial polymer produced from identical feedstocks. The following results were obtained ... [Pg.502]

Hexafluoiopiopylene and tetiafluoioethylene aie copolymerized, with trichloiacetyl peroxide as the catalyst, at low temperature (43). Newer catalytic methods, including irradiation, achieve copolymerization at different temperatures (44,45). Aqueous and nonaqueous dispersion polymerizations appear to be the most convenient routes to commercial production (1,46—50). The polymerization conditions are similar to those of TFE homopolymer dispersion polymerization. The copolymer of HFP—TFE is a random copolymer that is, HFP units add to the growing chains at random intervals. The optimal composition of the copolymer requires that the mechanical properties are retained in the usable range and that the melt viscosity is low enough for easy melt processing. [Pg.359]

Hydrocarbon resins (qv) are prepared by copolymerization of vinyltoluene, styrene, and a-methylstyrene in the presence of a Eriedel-Crafts catalyst (AlCl ). These resins are compatible with wax and ethylene—vinyl acetate copolymer (197). [Pg.563]

Another type of soHd supetacid is based on perfluorinated resin sulfonic acid such as the acid form of Du Font s Nafion resin, a copolymer of a perfluorinated epoxide and vinylsulfonic acid or soHd, high molecular weight petfluotoalkanesulfonic acids such as petfluotodecanesulfonic acid, CF2(CF2)qS02H. Such sohd catalysts have been found efficient in many alkylations of aromatic hydrocarbons (225) and other Friedel-Crafts reactions (226). [Pg.565]

The aqueous phase into which the monomer mix is dispersed is also prepared in a separate tank before transferring to the copolymerization ketde. It contains a catalyst, such as benzoyl peroxide [94-36-0], to initiate and sustain the polymerization reaction, and chemicals that aid in stabilizing the emulsion after the desired degree of dispersion is achieved. Careful adherence to predeterrnined reaction time and temperature profiles for each copolymer formulation is necessary to assure good physical durabiHty of the final ion-exchange product. [Pg.373]

Weak Base Anion Exchangers. Both styreoic and acryHc copolymers can be converted to weak base anion-exchange resias, but differeat syathetic routes are aecessary. Styreae—DVB copolymers are chloromethylated and aminated ia a two-step process. Chloromethyl groups are attached to the aromatic rings (5) by reactioa of chloromethyl methyl ether [107-30-2] CH2OCH2CI, with the copolymer ia the preseace of a Friedel-Crafts catalyst such as aluminum chloride [7446-70-0], AlCl, iroa(III) chloride [7705-08-0], FeCl, or ziac chloride [7646-85-7], ZaCl. ... [Pg.374]

Aqueous ring-opening metathesis polymerization (ROMP) was first described in 1989 (90) and it has been appHed to maleic anhydride (91). Furan [110-00-9] reacts in a Diels-Alder reaction with maleic anhydride to give exo-7-oxabicyclo[2.2.1]hept-5-ene-2,3—dicarboxylate anhydride [6118-51 -0] (24). The condensed product is treated with a soluble mthenium(Ill) [7440-18-8] catalyst in water to give upon acidification the polymer (25). Several apphcations for this new copolymer have been suggested (91). [Pg.453]

EinaHy, in 1976, Kaminsky and Sinn in Germany discovered a new family of catalysts for ethylene polymerization. These catalysts (ie, Kaminsky catalysts) contain two components a metallocene complex, usually a zkconocene, and an organoaluminum compound, methylaluminoxane (8,9). These catalysts and thek various later modifications enable the synthesis of ethylene copolymers with a high degree of branching uniformity. Formally classified as MDPE, LLDPE, or VLDPE, the resins thus produced have a number of properties that set them apart from common PE resins in terms of performance... [Pg.367]

High density polyethylene (HDPE) is defined by ASTM D1248-84 as a product of ethylene polymerisation with a density of 0.940 g/cm or higher. This range includes both homopolymers of ethylene and its copolymers with small amounts of a-olefins. The first commercial processes for HDPE manufacture were developed in the early 1950s and utilised a variety of transition-metal polymerisation catalysts based on molybdenum (1), chromium (2,3), and titanium (4). Commercial production of HDPE was started in 1956 in the United States by Phillips Petroleum Company and in Europe by Hoechst (5). HDPE is one of the largest volume commodity plastics produced in the world, with a worldwide capacity in 1994 of over 14 x 10 t/yr and a 32% share of the total polyethylene production. [Pg.379]


See other pages where Catalyst copolymer is mentioned: [Pg.1014]    [Pg.1014]    [Pg.1014]    [Pg.1589]    [Pg.310]    [Pg.1014]    [Pg.1014]    [Pg.357]    [Pg.1014]    [Pg.162]    [Pg.707]    [Pg.192]    [Pg.962]    [Pg.962]    [Pg.1014]    [Pg.1014]    [Pg.1014]    [Pg.1589]    [Pg.310]    [Pg.1014]    [Pg.1014]    [Pg.357]    [Pg.1014]    [Pg.162]    [Pg.707]    [Pg.192]    [Pg.962]    [Pg.962]    [Pg.247]    [Pg.374]    [Pg.419]    [Pg.420]    [Pg.302]    [Pg.316]    [Pg.181]    [Pg.329]    [Pg.277]    [Pg.355]    [Pg.356]    [Pg.514]    [Pg.374]    [Pg.467]    [Pg.367]    [Pg.383]   
See also in sourсe #XX -- [ Pg.707 ]




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Block copolymer catalyst

Block copolymer-based catalyst

Catalyst copolymer, preparation

Catalyst random copolymer

Catalyst supports copolymers

Catalysts Covalently Bound to the Amphiphilic Block Copolymer

Chemical polymerization catalyst copolymers

Copolymer Isolation and Catalyst Recycling

Copolymers early transition metal catalysts

Copolymers late transition metal catalysts

Ethylene/propylene copolymers single-site” catalysts

Ethylene/propylene copolymers titanium-based catalysts

Ethylene/propylene copolymers vanadium-based catalysts

Homogeneous catalysts alternating copolymers

Living catalysts copolymers

Metallocene catalysts copolymer production

New Ethylene Copolymers Based on Single-Site Catalysts

Novel Ethylene Copolymers Based on Single-Site Catalysts

Ziegler catalysts, copolymers from

Ziegler-Natta catalysts alternating copolymers

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