Zr Complexes with Phenoxy-Imine Chelate Ligands
J. Am. Chem. Soc., Vol. 123, No. 28, 2001 6849
Olefin Polymerization Using Complex 1. A zirconium
complex having two 3-tert-butylsalicylideneaniline ligands, bis-
[N-(3-tert-butylsalicylidene)anilinato]zirconium(IV)dichloride (1),
was investigated as an ethylene polymerization catalyst using
methylalumoxane (MAO) as a cocatalyst at 25 °C under
ethylene at atmospheric pressure. The results are summarized
in Table 1.
Complex 1 displayed an activity of 197 kg of polymer/mmol
of cat‚h (entry 1), which is much higher than the activity
displayed by Cp2ZrCl2 (entry 7) at the same catalyst concentra-
tion. Difficulty with stirring was encountered for entry 1 because
of the large amount of polyethylene produced. Accordingly,
screens were run with reduced catalyst concentrations in order
to obtain a more accurate activity for complex 1. As a result,
complex 1 was found to display a very high activity of 550 kg
of polymer/mmol of cat‚h with a viscosity average molecular
weight (Mv) value of 0.9 × 104. The activity obtained at reduced
catalyst concentration (550 kg of polymer/mmol of cat‚h, entry
2) was ∼20 times larger than that exhibited by Cp2ZrCl2 at 25
°C. The molecular weight distribution (Mw/Mn) of the polymer
obtained from complex 1 was 2.06, suggesting that the polymer
is produced by a single active species.2d Transition melting
temperature (Tm) of the polymer was 128 °C. Analysis using
13C NMR spectroscopy indicates that the polymer is a linear
Figure 1. Relationship between the polymerization time and the
polymer yield obtained with complex 1/MAO. Conditions: 25 °C, 0.1
MPa ethylene pressure; solvent, toluene 400 mL; complex 1, 0.08 µmol;
MAO (A1), 1.25 mmol.
polyethylene having virtually no branching (see Supporting
Information). Infrared spectroscopy reveals a vinyl end group
concentration of ∼2.4/1000 carbon atoms, which suggests that
â-hydrogen transfer is the main termination pathway. Increasing
Al/Zr ratio from 6250/1 to 312 500/1 gave rise to no significant
changes in the catalytic performance, except the activity in entry
1 (see Table 1, caption b). This observation confirms that chain
transfer to aluminum does not play a dominant role in chain
termination.
To investigate the catalytic lifetime of complex 1, ethylene
polymerizations were conducted for 5, 15, and 30 min. The
relationship between the polymerization time and the polymer
yield indicates that the 1/MAO catalyst has a catalytic lifetime
of at least 30 min, as shown in Figure 1.
The effects of the polymerization temperature on the catalytic
activity of 1/MAO were studied. The results were compared
with those for Cp2ZrCl2 (Figure 2). In the case of Cp2ZrCl2,
the activity was 7 kg of polymer/mmol of cat‚h at 0 °C and
gradually increased to ∼100 kg of polymer/mmol of cat‚h at
75 °C. In comparison, 1/MAO provided 295 kg of polymer/
mmol of cat‚h activity at 0 °C. Moreover, its activity increased
to a maximum of 587 kg of polymer/mmol of cat‚h at 40 °C.
Above 40 °C, the activity decreased. However, over a temper-
ature range of 0 to 75 °C, the activity remained above 100 kg
of polymer/mmol of cat‚h.
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In addition to MAO, the catalytic performance of complex 1
with Ph3CB(C6F5)4/i-Bu3Al as the cocatalyst was investi-
gated.24,25 This catalyst system gave unexpectedly high molec-
3
ular weight polyethylene. At 25 °C, complex 1 with Ph CB-
(C6F5)4/ i-Bu3Al resulted in an Mv value of 383 × 104 with 4
kg of polymer/mmol of cat‚h. Furthermore, at 50 °C, this catalyst
system produced exceptionally higher molecular weight poly-
ethylene (Mv 505 × 104) with 11 kg of polymer/mmol of cat‚h.
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