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Metallocene polyethylene constrained geometry catalysts

Constrained-geometry catalysts for C2H4 polymerization 88 that are counterparts of well-known ansa-metallocene systems have been prepared and shown to be active, in combination with MAO, toward polymerization of ethylene the product is almost entirely polyethylene, with ca. 1% of 1-octene obtained. The titanium complex was found to be four times as active as the zirconium species.1... [Pg.34]

These monocyclopentadienyl amidotitanium complexes, which are classified as constrained-geometry catalysts, are capable of producing low-density polyethylene (ethylene copolymers with C4, C(, or Cg 1-alkenes) that also contain long-chain branches, in contrast to strictly linear low-density polyethylene (ethylene copolymers with C4, C(, or Cg 1-alkenes) produced by bent metallocene-based catalysts [30,105,148,149]. [Pg.80]

In addition to the metallocenes described previously, so-called halfsandwich compounds or constrained-geometry catalysts (Fig. 3) such as dimethylsilyl-t-butylamido cyclopentadienyl titanium dichloride are used. These catalysts are excellent for producing polyethylenes with long-chain branching and can incorporate high amounts of comonomers such as 1-octene... [Pg.95]

Although ethylene/1-olefin copolymers were well documented in the late 1950s with the discovery of the chromium-based Phillips catalyst and the titanimn-based Ziegler catalyst, it was the discovery of metallocene-based single-site catalysts and the constrained geometry catalyst system that significantly increased the various types of new ethylene-based copolymers that are available for commercial applications. These new catalysts created new products, applications and markets for the polyethylene industry. [Pg.205]

The long-chain branched metallocene polyethylenes made with the constrained geometry catalysts described in Chapter 3 pose their own special problem, because the level of branching, 0.01 to 0.1 LCB per 1,000 carbon atoms, is too low to be detected by means of GPC-MALLS. For these materials the factor j8 in Eq. 2.104 has been established to be 0.5 by use of C-13 NMR [57], and this makes it possible to use GPC-LALLS-DV to determine the distribution of radii of gyration and the number of branches per 1000 carbon atoms. Then using the results... [Pg.45]

The first commercial process for making LLDPE was the Sclair technology developed by Dupont Canada and now implemented by NOVA Chemicals. This process involves high-temperature solution polymerization. Much LLDPE is now made in gas-phase reactors with butene or hexene as the co-monomer. The constrained-geometry catalyst (CGC) is a metallocene catalyst developed by Dow Chemical for the manufacture of linear, very-low density polyethylene resins by solution polymerization with octene as the comonomer. For a given co-monomer content, the solid-state density is lower for octene than for lower a-olefins. [Pg.71]

Figure 3.2 Algorithm for Monte Carlo simulations of branching distribution in branched metallocene polyethylenes made using a constrained-geometry catalyst. A large number of molecules are "created"according to rules based on the relative probabilities of propagation (pp) and monomer addition Ip). From Soares and Hamielec [871. Figure 3.2 Algorithm for Monte Carlo simulations of branching distribution in branched metallocene polyethylenes made using a constrained-geometry catalyst. A large number of molecules are "created"according to rules based on the relative probabilities of propagation (pp) and monomer addition Ip). From Soares and Hamielec [871.
Figure9.21 Storage modulus versus frequency data [57] for a series of metallocene (constrained geometry catalyst) polyethylenes with progressively increasing levels of long-chain branching, as given in Table 9.1, compared to the predictions of the hierarchical model at 160 C.The parameter values used in the hierarchical model are M = 1167, G 5 = 2.0 10 Pa, Tg = 3.5 -10 s with a = 4/3.These values were obtained from fits of model predictions to rheological data for model hydrogenated 1,4-poly butadiene combs, except that was adjusted to account for a difference in temperature. From Park and Larson [59]. Figure9.21 Storage modulus versus frequency data [57] for a series of metallocene (constrained geometry catalyst) polyethylenes with progressively increasing levels of long-chain branching, as given in Table 9.1, compared to the predictions of the hierarchical model at 160 C.The parameter values used in the hierarchical model are M = 1167, G 5 = 2.0 10 Pa, Tg = 3.5 -10 s with a = 4/3.These values were obtained from fits of model predictions to rheological data for model hydrogenated 1,4-poly butadiene combs, except that was adjusted to account for a difference in temperature. From Park and Larson [59].
Wood-Adams, P. M. The effect of long-chain branching on the rheological behavior of polyethylenes synthesized using constrained geometry and metallocene catalysts. Doctoral Thesis (1998) McGill University... [Pg.410]


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