C O M M U N I C A T I O N S
Table 1. Results of Ethylene Polymerization with 3a-ca
b
T
[°C]
time
[min]
TOF
[mol(C2H4) mol(Ti)-1 h-1
polymer yield
[g]
Tm
[°C]
Mn (calcd)
Mw/Mnc
entry
complex
Mnc [104 g mol-1
]
]
[104 g mol-1
]
1
2
3
4
5
6
7
3c
3a
3b
3a
3a
3a
3a
25
25
25
0
50
75
25
15
15
15
15
15
15
60
21 400
37 100
14 300
30 000
42 900
42 900
36 100
0.15
0.26
0.10
0.21
0.30
0.30
1.01
138
139
139
140
139
139
137
26
27
19
19
32
26
99
(15)
26
(10)
21
30
30
1.45
1.01
2.62
1.13
1.03
1.15
1.17
100
a Reaction conditions: 1 atm of ethylene pressure, 1 µmol of catalyst, toluene 250 mL, 2000 equiv of MAO (molar ratio). b Measured by DSC.
c Determined by GPC referenced to linear PE (cf. SI for details).
substituents also affect the activation reaction, which is effective only
for 3a but not for analogues lacking o-fluorine substitution.
Acknowledgment. Financial support by the DFG (Me 1388/
3-3) is gratefully acknowledged. S.M. is indebted to the Fonds der
Chemischen Industrie. We thank Lars Bolk (Konstanz) and Dieter
Lilge (Basell, Frankfurt) for GPC analysis and Hans Brintzinger
and Inigo Go¨ttker-Schnetmann for fruitful discussions.
Supporting Information Available: Preparative procedures and
characterization data, X-ray data for 3a. This material is available free
References
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Figure 2. Plots of Mn and Mw/Mn versus time for ethylene polymerization
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The effect of polymerization temperature was studied (entries
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25, 50, and 75 °C (Figure 2 and SI). A linear increase of Mn with
polymerization time and narrow molecular weight distributions were
observed for all runs, thus corroborating the highly controlled nature
of the polymerization.
By comparison to the well studied highly active phenoxyimine
catalysts,3 the lower insertion rates with 3a facilitate control of the
polymerization reactions. A generally lower reactivity may also
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The utility of 3a is also illustrated by the preparation of block
copolymers, with a hard PE block and a soft atactic polypropylene
block. After complete ethylene consumption at 25 °C, addition of
propylene afforded a block copolymer with apparent Mn 1.9 × 105
g mol-1, Mw/Mn 1.12, PE content 60 wt %. Notably, the living
character is also retained at 50 °C (Mn 2.4 × 105 g mol-1, Mw/Mn
1.12, PE content 40 wt %. For details, cf. SI).
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In conclusion, the conveniently accessible novel enolatoimine
Ti complex 3a upon MAO activation polymerizes ethylene in a
living fashion with unprecedented molecular weight control and
temperature stability. This provides viable access to high molecular
weight PE with an extremely narrow molecular weight distribution
(Mw/Mn 1.01) and corresponding block copolymers. In addition to
phenoxyimine Ti complexes, this is another example of a system in
which o-F substitution appears beneficial for living polymerization of
ethylene as well as propylene. Our studies indicate that these
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(15) DSC (SI) shows typical behaviour of UHMWPE. In the first heating trace
a narrow melt transition (144 °C) and high crystallinity (76%) are observed
for the nascent polymer. In the second heating cycle, crystallinity is much
lower (49%) due to entanglement hindering recrystallization from the melt.
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J. AM. CHEM. SOC. VOL. 130, NO. 40, 2008 13205