Table 1 Results of ethylene polymerisation runs using procatalysts 1 and 2a
Activity/
Procatalyst
(mmol)
Activator
(mmol/equiv)
Pressure
C2H4/bar
Yield
PE/g
g mmol21
h21 bar21
Run
1
T/°C
25
50
25
50
25
50
25
50
25
25
50
Solvent
toluene
Mw
1a
(10)
1a
(0.5)
1b
(20)
1b
(0.6)
1c
(10)
1c
(0.6)
1d
(20)
1d
MAO
(1.0/100)
MAO
(0.5/1000)
MAO
(8.0/400)
MAO
(0.6/1000)
MAO
(1.0/100)
MAO
(0.6/1000)
MAO
(8.0/400)
MAO
1
10
1
5.8
26.9
5.7
1170
5430
570
203000
611000
29000
242000
52000
562000
260
2
isobutane
toluene
3
4
isobutane
toluene
10
1
56.5
6.2
9340
1230
11020
120
5
6
isobutane
toluene
10
1
63.1
1.2
7
8
isobutane
toluene
10
1
7.8
1280
740
470
(0.6)
1e
(10)
2
(10)
2
(0.6/1000)
MAO
(1.0/100)
MAO
(1.0/100)
MAO
9
3.7
15000
26000
14000
10
11
toluene
1
2.3
460
isobutane
10
3.7
450
(0.5)
(0.5/1000)
a General conditions: 1 atm Schlenk tests carried out in toluene over 30 min, reaction quenched with dil. HCl and the solid PE washed with MeOH (50 cm3)
and dried in a vacuum oven at 50 °C. 10 atm tests performed in 1 l autoclave, procatalyst dissolved in toluene, isobutane solvent, triisobutylaluminium
scavenger, runs carried out over 60 min.
The results of ethylene polymerization tests are collected in
Table 1. Several features are noteworthy. In general, the
activities of the iron catalysts are exceptionally high, in many
cases comparable or even higher than those seen by metal-
locenes under analogous conditions. All of the catalysts produce
essentially linear polyethylene with molecular weights that are
dependent upon the aryl substitution pattern. Most notable is a
dramatic fall-off in molecular weight to a-olefin oligomers for
derivatives with one o-methyl substituent (runs 7,8) compared
with derivatives that contain methyl substituents in both ortho
positions. Clearly steric protection of the active site is a crucial
factor in controlling molecular weight.
There is also a marked dependence of the polymer molecular
weight on ethylene pressure for the iron catalyst system, an
effect that is not seen for the cobalt catalyst 2 (runs 10, 11); the
cobalt catalyst also displays a considerably lower activity than
its iron analogue. 13C NMR end-group analysis of the polymers
generated by 1a–c (runs 2, 4, 6) reveals isopropyl end-groups in
addition to low levels of vinyl unsaturation. This is consistent
with a termination mechanism involving alkyl group transfer
from the AlBui3 scavenger in addition to b-H transfer. The
polymers formed from 1d and the aldimine catalyst 1e contain
a larger proportion of vinyl end-groups ( > 4 per 1000 carbons)
indicating that b-H transfer plays a more dominant role in chain
termination for these catalysts.
Notes and References
† E-mail: v.gibson@ic.ac.uk
‡ Satisfactory elemental analyses have been obtained.
§Crystal data for 1a: C33H43N3Cl2Fe·0.5H2O, M = 617.5, triclinic, P1 (no.
2), a = 8.779(1), b = 9.876(1), c = 20.976(1) Å, a = 83.70(1), b =
88.18(1), g = 65.67(1)°, V = 1646.9(3) Å3, Z = 2, Dc = 1.245 g cm23
m(Cu-Ka) = 53.6 cm21, F(000) = 654. A deep blue platy needle of
dimensions 0.40 3 0.20 3 0.03 mm was used. 4878 independent reflections
were measured on a Siemens P4/PC diffractometer with Cu-Ka radiation
using w-scans. The structure was solved by direct methods and all of the
non-hydrogen atoms were refined anisotropically using full-matrix least-
squares based on F2 to give R1 = 0.061, wR2 = 0.144 for 3595 independent
observed, absorption corrected reflections [ıFoı > 4s(ıFoı), 2q @ 120°]
and 362 parameters. CCDC 182/812.
¯
,
1 K. B. Sinclair and R. B. Wilson, Chem. Ind., 1994, 857.
2 A. M. Thayer, Chem. Eng. News, Sept 11, 1995, 15.
3 R. G. Harvan, Chem. Ind., 1997, 212.
4 H. H. Brintzinger, D. Fischer, R. Mu¨lhaupt, B. Rieger and R. M.
Waymouth, Angew. Chem., Int. Ed. Engl., 1995, 34, 1143.
5 M. Bochmann, J. Chem. Soc., Dalton Trans., 1996, 255.
6 T. J. Marks, Acc. Chem. Res., 1992, 25, 57.
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117, 6414.
9 L. K. Johnson, S. Mecking and M. Brookhart, J. Am. Chem. Soc., 1996,
118, 267.
10 C. M. Killian, D. J. Tempel, L. K. Johnson and M. Brookhart, J. Am.
Chem. Soc., 1996, 118, 11664.
11 L. K. Johnson, C. M. Killian, S. D. Arthur, J. Feldman, E. F. McCord,
S. J. McLain, K. A. Kreutzer, A. M. A. Bennett, E. B. Coughlin, S. D.
Ittel, A. Parthasarathy, D. J. Tempel and M. S. Brookhart, Pat. Appl.
WO 96/23010, 1996, DuPont.
The new catalyst family described herein represents a
significant addition to the growing armoury of technologically
important olefin polymerization catalysts.
BP Chemicals Ltd is thanked for financial support. Dr J.
Boyle and Dr G. Audley are thanked for NMR and GPC
measurements, respectively.
Received in Liverpool, UK, 10th March 1998; 8/01933I
850
Chem. Commun., 1998