C O M M U N I C A T I O N S
Table 1. Representative Ethylene Polymerization Resultsa
structure (as shown by X-ray diffraction) and produces high MW
PE. However, in solution (toluene), 3 and/or growing higher-alkyl
analogues break up to form mononuclear species (as shown by
NMR) that produce low MW PE, similar to conventional (PO)P-
d(R)(L) catalysts. The overall MWD is broad and reflects the degree
of cage fragmentation under the given polymerization conditions.
Similar reasoning explains the behavior of 2a-c. This proposal is
supported by the polymerization behavior of 3 in CH2Cl2 at 25 °C.
Under these conditions, 3 is initially completely soluble and 90%
intact and produces PE that contains a substantial high MW
component (entry 9). The broad MWD is again due to fragmentation
of 3 and/or growing higher-alkyl analogues. The lower temperature
disfavors fragmentation, but this effect may be counteracted by the
higher polarity of the solvent (ꢀ: CH2Cl2, 8.9; toluene, 2.4).
Surprisingly, 4 produces only ethylene oligomers (Table 1, entry
11) in good yield. The oligomers display a Schulz-Flory distribution
(ꢀ ) 0.69), consistent with single site catalysis. These results show
that a pendant free ArSO3- group strongly enhances chain transfer.
This work shows that the incorporation of the pendant ArSO3Li
group in (Li-OPO)PdMe(L) catalysts dramatically influences their
ethylene polymerization behavior. (Li-OPO)PdMe(L) complexes
self-assemble into tetranuclear species that produce very high MW
PE. In solution, the tetramers fragment into mononuclear species
that behave like normal (PO)Pd(R)(L) catalysts and produce low
MW PE. When the Li+ counterion is sequestered by a cryptand,
only ethylene oligomers are formed. The unusual production of a
high MW polymer by the tetranuclear species may result from steric
effects. The crystal structure of 3 shows that one axial face of the
Pd center is blocked by the Li4S4O12 cage, which may disfavor
associative chain transfer.5 It is also possible that cooperative effects
between the Pd centers in 3 are important.6 The free ArSO3- group
in 4 may facilitate chain transfer by displacing the olefin in
Pd(H)(olefin) intermediates generated by ꢀ-H elimination or by
stabilizing the transition state for ꢀ-H transfer to monomer by
coordinating to Pd. We are exploring multinuclear catalysts based
on more robust self-assembled cages.
e
g
P
(psi)
T
(°C)
time
(h)
yield
(g)
Mw
(103)
Tm
(°C)
entry
cat.
PDIe
1b
2b
3b
4b
5b
6b
7c
PO1
PO2
3
410
435
410
410
410
410
410
410
80
80
80
80
80
80
80
80
80
25
25
25
2
2
2
2
2
1
2
2
2.84
4.36
6.25
0.85
4.85
1.35
0.35
5.18
1.91
0.45
2.25
13.2
58.8
7.87
1110
382
2.0
2.5
2.6
28
49
31
2.0
60
29
2.2
-
131.4
132.9
131.7
135.4
134.3
134.3
129.3
138.7
136.5
136.3
-
2a
2b
2c
PO1
3
3
PO2
4
284
6.39
1000
915
8c
9d
10d
11d
24
24
24
80
80
29.0
oligof
a Solvent ) 50 mL, [Pd] ) 0.2 mM (10 µmol). b Solvent ) toluene.
c Solvent ) hexanes. d Solvent ) CH2Cl2. e GPC. f C4-C18 oligomers.
g DSC.
The reaction of 3 with the cryptand Krypt211 yields [Li-
(Krypt211)][(OPO)PdMe(py′)] (4). The [OPO]2- ligand of 4 binds
to Pd as a κ2-P,O chelator, and the pendant sulfonate group interacts
weakly with the Pd (Pd-O distance: 3.08 Å; sum of van der Waals
radii of Pd and O: 3.15 Å). 2d undergoes Pd-Me bond homolysis
in fluorescent room light in CD2Cl2 to yield {(OPO)Pd}2 (5) and
CH3D.4 The [OPO]2- ligands in 5 act as κ3-O,P,O pincers to each
-
Pd and also bridge via one SO3 oxygen.
In toluene at 80 °C (410 psi ethylene), mononuclear {2-(Ar2P)-
4-Me-benzenesulfonate}PdMe(py) catalysts (PO1: Ar ) Ph; PO2:
Ar ) 2-Et-Ph) produce linear PE with low to moderate MW and a
narrow molecular weight distribution (MWD; Table 1, entries 1,2),
characteristic of single site catalysis. 3 behaves similarly (entry 3).
Under these conditions, PO1 and PO2 are completely soluble and
3 is highly soluble. In contrast, 2a-c produce very high MW linear
PE with a broad bimodal MWD (entries 4-6 and Figure 2a),
suggestive of multisite catalysis. The insoluble 2a yields PE with
a large high MW fraction, while sparingly soluble 2b,c yield PEs
with a large low MW fraction.
To explore the influence of catalyst solubility, the polymer-
ization behaviors of PO1 and 3 were compared under homoge-
neous and heterogeneous conditions. PO1 behaves similarly in
toluene (initially homogeneous) and hexanes (heterogeneous) except
that the MW decreases slightly in hexanes (Table 1, entries 1,7).
In contrast, 3 generates low MW PE with a narrow MWD in toluene
(as noted above) but produces high MW PE with a broad MWD
and a significant high MW component in hexanes (entries 3,8, and
Figure 2b). These results show that the solubility of the catalyst
per se does not control the MW but rather suggest that the nuclearity
of the catalyst is a key factor. That is, under heterogeneous
conditions (hexanes), 3 substantially maintains its tetranuclear
Acknowledgment. This work was supported by the U.S.
Department of Energy (DE-FG-02-00ER15036). The authors thank
T. Huang, P. D. Hustad, and T. T. Wenzel (Dow) and M. Mitobe
and Y. Kawashima (Sumitomo) for help with GPC.
Supporting Information Available: Experimental procedures and
characterization of complexes (PDF, CIF). This material is available
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Figure 2. GPC traces of PE samples obtained from (a) 2a, 2b, and 2c in
toluene at 80 °C and (b) 3 in toluene and hexanes at 80 °C. See Table 1.
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J. AM. CHEM. SOC. VOL. 132, NO. 1, 2010 53