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Cobalt polymerization conditions

Table 1. Solution polymerization results for butadiene usir cobalt(II) pyridyl bis(imine) complexes. Polymerization conditions [l,3-butadiaie]= 1 mol/L [Cal.] = 2.00 x 10" mol/L ... Table 1. Solution polymerization results for butadiene usir cobalt(II) pyridyl bis(imine) complexes. Polymerization conditions [l,3-butadiaie]= 1 mol/L [Cal.] = 2.00 x 10" mol/L ...
Since the partial insolubility of the starch-ceric ammonium nitrate reaction product complicates the interpretation of solubility data, we ran a second series of graft polymerizations using cobalt-60 as an initiator in an attempt to remove this variable (Table II). If combination of PAN macroradicals is occuring during graft polymerization, it should occur during cobalt-60 initiated polymerizations as well as in those initiated by ceric ammonium nitrate. In the first four reactions of Table II, starch was irradiated as a water slurry under graft polymerization conditions, but in the absence of acrylonitrile, to determine the influence of different doses of irradiation on starch solubility. [Pg.198]

Based on this mechanistic background, it is now possible to move to the more practical aspects of CM RP, such as the choice of adequate polymerization conditions (i.e., the cobalt complex structure), of temperature, solvent, and the use of additives. For each monomer, all of these parameters must be taken into account in order to adjust the polymer-cobalt bond strength. [Pg.69]

As noted in Section 4.2, the CMRP mechanism depends on the polymerization conditions. Typically, DT occurs when the amount of generated radicals exceeds the initial cobalt(ll) concentration, whereas a RT pathway dominates in all other situations [24]. In the DT mode (Equation 4.3), the polymerization kinetics, as well as the level of control, is related to the amount and the rate of release of radicals a large excess of radicals will promote extensive termination reactions... [Pg.71]

Although the potential of CMRP for macromolecular engineering clearly exists, it depends heavily on the range of monomers that can be controlled by a single cobalt catalyst This statement justifies the suggestion that further efforts must he devoted to the quest for more versatile complexes, and for the optimization of polymerization conditions for challenging monomers. [Pg.75]

A side reaction in catalytic hydroformylation is aldehyde hydrogenation. In fact, for the same catalyst, the experimental conditions can be so modified that aldehyde hydrogenation takes place, producing the corresponding alcohols. As an example, binulcear cobalt polymeric complex brings about the conversion of aldehydes to alcohols when higher temperatures are used (Pittman and Evans, 1973). [Pg.231]

An unusual method for the preparation of syndiotactic polybutadiene was reported by The Goodyear Tire Rubber Co. (43) a preformed cobalt-type catalyst prepared under anhydrous conditions was found to polymerize 1,3-butadiene in an emulsion-type recipe to give syndiotactic polybutadienes of various melting points (120—190°C). These polymers were characterized by infrared spectroscopy and nuclear magnetic resonance (44—46). Both the Ube Industries catalyst mentioned previously and the Goodyear catalyst were further modified to control the molecular weight and melting point of syndio-polybutadiene by the addition of various modifiers such as alcohols, nitriles, aldehydes, ketones, ethers, and cyano compounds. [Pg.531]

The corresponding reactions of transient Co(OEP)H with alkyl halides and epoxides in DMF has been proposed to proceed by an ionic rather than a radical mechanism, with loss of from Co(OEP)H to give [Co(TAP), and products arising from nucleophilic attack on the substrates. " " Overall, a general kinetic model for the reaction of cobalt porphyrins with alkenes under free radical conditions has been developed." Cobalt porphyrin hydride complexes are also important as intermediates in the cobalt porphyrin-catalyzed chain transfer polymerization of alkenes (see below). [Pg.289]

Figure 4.1 summarizes the different routes that can potentially lead to carbon deposition during FTS (a) CO dissociation occurs on cobalt to form an adsorbed atomic carbon, which is also referred to as surface carbide, which can further react to produce the FT intermediates and products. The adsorbed atomic carbon may also form bulk carbide or a polymeric type of carbon. Carbon deposition may also result (b) from the Boudouard reaction and (c) due to further reaction and dehydrogenation of the FTS product (what is commonly called coke), a reaction that should be limited at typical FT reaction conditions. Carbon formed on the surface of cobalt can also spill over or migrate to the support. This is reported to readily occur on Co/A1203 catalysts.43 The chemical nature of the carbonaceous deposits during FTS will depend on the conditions of temperature and pressure, the age of the catalyst, the chemical nature of the feed, and the products formed. [Pg.54]

Lu and coworkers have synthesized a related bifunctional cobalt(lll) salen catalyst similar to that seen in Fig. 11 that contains an attached quaternary ammonium salt (Fig. 13) [36]. This catalyst was found to be very effective at copolymerizing propylene oxide and CO2. For example, in a reaction carried out at 90°C and 2.5 MPa pressure, a high molecular weight poly(propylene carbonate) = 59,000 and PDI = 1.22) was obtained with only 6% propylene carbonate byproduct. For a polymerization process performed under these reaction conditions for 0.5 h, a TOF (turnover frequency) of 5,160 h was reported. For comparative purposes, the best TOF observed for a binary catalyst system of (salen)CoX (where X is 2,4-dinitrophenolate) onium salt or base for the copolymerization of propylene oxide and CO2 at 25°C was 400-500 h for a process performed at 1.5 MPa pressure [21, 37]. On the other hand, employing catalysts of the type shown in Fig. 12, TOFs as high as 13,000 h with >99% selectivity for copolymers withMn 170,000 were obtained at 75°C and 2.0 MPa pressure [35]. The cobalt catalyst in Fig. 13 has also been shown to be effective for selective copolymer formation from styrene oxide and carbon dioxide [38]. [Pg.14]

As an active initiator for a co-polymerization, acyl-cobalt complexes also work well. As demonstrated by Alper and Lee, an equimolar mixture of Go2(GO)s, benzyl bromide (BnBr), and dihydro-1,10-phenanthroline 17, possibly generating BnGOGo(GO)4 under the reaction conditions, co-polymerized PO or 1,2-butene oxide with GO, and the... [Pg.606]

C. At pH/concentration conditions just below saturation the adsorbed species is probably a polymeric form of cobalt (II) hydroxide. At higher pH values the nucleation of cobalt (II) hydroxide is completed and the silica with adsorbed cobalt (II) behaves as cobalt (II) hydroxide. Some mutual coagulation between Si02 and precipitated Co(OH)2 may occur for the higher Co (II) concentrations. [Pg.80]

In contrast to cobalt, rhodium permits a one-step oxo alcohol synthesis in the presence of certain monomeric and polymeric amines (8, 9, 10). Included in this group are triethylamine, N-alkylpiperidines, N-methylpyrrolidine, and N,N-dimethylbenzylamine (DMBA). Initial kinetic data on this amine-promoted alcohol synthesis (under severe reaction conditions) have been reported by B. Fell and coworkers (II), but no attempt has been made to characterize the catalytic species in the reaction cycle. [Pg.250]

Good evidence has been obtained that heterogeneous iron, ruthenium, cobalt, and nickel catalysts which convert synthesis gas to methane or higher alkanes (Fischer-Tropsch process) effect the initial dissociation of CO to a catalyst-bound carbide (8-13). The carbide is subsequently reduced by H2to a catalyst-bound methylidene, which under reaction conditions is either polymerized or further hydrogenated 13). This is essentially identical to the hydrocarbon synthesis mechanism advanced by Fischer and Tropsch in 1926 14). For these reactions, formyl intermediates seem all but excluded. [Pg.3]

Various metal ions, including iron(II), cobalt(II), and maganese(II) (77), as well as magnesium(II) (78), can be photo-oxidized by dyes. Under some conditions, in air, peroxides can be formed which initiate polymerization. [Pg.460]

The spacer units in 3.60 are assembled from polyphosphazenes that bear p-bromophc-noxy side groups via a lithiation reaction, and treatment with a diorganochlorophosphine to give 3.62. The chemistry is summarized in reaction sequence (45).107 Polymer 3.62 coordinates to a variety of metallo species,108 including osmium cluster compounds and cobalt carbonyl hydroformylation catalysts. When used as a polymeric hydroformylation catalyst, this latter species proved how stable the polyphosphazene backbone is under the drastic conditions often needed for these types of reactions. The weakest bonds in the molecule proved to be those between the phosphine phosphorus atoms and the aromatic spacer groups. [Pg.95]

Metal—Carbon Bonds in Cobalt-Catalyzed Polymerization. Concentrations of metal-carbon bonds were determined (using tritium labelled alcohol) with increase in conversions. Experiments were made in two solvents (petrol and benzene) with two cobalt salts (chloride and naphthenate) under conditions giving rise either to liquid mixed structure or to high trans polybutadiene. The data are summarized in Table XI. Table XII and Figure 11 shows optical properties of some cobalt salts and complexes. [Pg.58]

The polymerization of conjugated dienes to products with a controlled structure usually occurs in the presence of alkylaluminium compounds. The choice not only the transition metal but also of its ligands is of importance. Some systems produce a certain kind of stereochemical structure irrespective of external conditions. So, for example, vanadium compounds yield predominantly the trans-1,4 structure whereas cobalt salts yield the c -1,4 structure. Other catalysts are very sensitive, and a small external effect completely changes their stereochemical activity [267b] [e. g. Cr(acetylacetona-te)3-R3Al]. Examples of several catalytic systems are summarized in Table 7. [Pg.134]


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Polymerization conditions

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