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3
zole), the mechanism of selection is modified to cause
the preferential formation of l-diads (enantiomorphic
site control) [19]. Similar highly efficient enantioselec-
tivity by the enantiomorphic catalyst is displayed by
systems containing the chiral phosphino-oxazoline
chelate ligands, despite their C1-symmetry. However, in
this case high enantioface discrimination does not
take place in the first insertion step to give the
1-phenylethyl-palladium intermediate; high enantio-
selectivity is displayed probably already for the second
olefin insertion but surely for the third and successive
insertions. The importance of the growing chain for
efficient enantioface selection has been similarly proven
for the Ziegler–Natta olefin polymerization with metal-
locene [30,31]. For the pyridine–oxazoline modified
catalytic system, the chirality of the catalyst site is not
sufficient to overcome the effect of the chirality of the
growing chain. A prevailingly syndiotactic copolymer,
as for the 2,2%-bipyridine ligand, is thus produced. Site
selective coordination of the olefin at the metal center is
probably involved in the stereocontrol of both catalysts
1 and 2.
17.8 Hz, J(H,H)=3.8 Hz), 2.62 (dd, 1H, CH2 (D2),
2J(H,H)=18.1 Hz, J(H,H)=4.0 Hz), 3.41 (dd, 1H,
3
CH2 (D1), 2J(H,H)=17.8 Hz, 3J(H,H)=10.6 Hz), 3.47
2
3
(dd, 1H, CH2 (D2), J(H,H)=18.1 Hz, J(H,H)=10.0
Hz), 3.68 (q, 1H, CH(CH3) (D1 or D2), J(H,H)=7.1
3
3
Hz), 3.88 (q, 1H, CH(CH3) (D1 or D2), J(H,H)=7.1
Hz), 4.75 (dd, 1H, CH (D2), 3J(H,H)=4.0 Hz,
3J(H,H)=10.0 Hz), 4.77 (dd, 1H, CH (D1), 3J(H,H)=
3.8 Hz, 3J(H,H)=10.6 Hz), 5.78 (d, 1H, H2CꢁC (D1 or
2
D2), J(H,H)=0.7 Hz), 5.80 (d, 1H, H2CꢁC (D1 or
2
D2), J(H,H)=0.7 Hz), 6.15 (d, 1H, H2CꢁC (D1 or
2
D2), J(H,H)=0.7 Hz), 6.16 (d, 1H, H2CꢁC (D1 or
2
D2), J(H,H)=0.7 Hz).
2,4-Diphenyl-pent-1en-3-one (9): 1H-NMR (CDCl3,
3
500 MHz): 1.46 (d, 3H, CH3, J(H,H)=6.9 Hz), 4.35
(q, 1H, CH(CH3), 3J(H,H)=6.9 Hz), 5.75 (d, 1H,
H2CꢁC, 2J(H,H)=0.7 Hz), 6.01 (d, 1H, H2CꢁC,
2J(H,H)=0.7 Hz).
4.2. Copolymerization experiments
4.2.1. Copolymerization reaction of styrene and CO
The copolymerization using the catalytic system 1 is
described in detail as an example (entry 1 in Table 1).
A 250 ml stainless steel autoclave under an atmo-
sphere of N2 was charged with 1,4-benzoquinone (0.216
g; 2.0 mmol). The palladium complex (1, 0.11 mmol)
was dissolved in methanol (10 ml) in a Schlenk tube,
and stirred for 15 min. After adding styrene (50 ml; 435
mmol), the solution was transferred to the pre-evacu-
ated autoclave. After pressurising to 320 bar of CO, the
autoclave was placed in an oil bath and the mixture
stirred and heated to 50°C. After 46 h, the autoclave
was cooled down to room temperature (r.t.) and the
residual gas released. The mixture was poured into
MeOH, and the unsoluble copolymer filtered off,
washed again with methanol and dried. Yield 5.5 g
(productivity 74.4 mmol g−1(Pd) h). Prior to NMR
analysis, some of the recovered copolymer was ex-
tracted with MeOH in a Kumagawa extractor.
4. Experimental
4.1. General
Complexes 1 and 2 were prepared as described previ-
ously by reaction of the ligands with PdCl2(NCPh)2 to
PdCl2(L L%), followed by treatment with silver tri-
fluoromethanesulfonate, which led to the corresponding
[Pd(H2O)2(L L%)](OTf)2 [21,32].
The low molecular weight products were character-
ised by NMR and GC-MS. The enantiomeric excess
was determined by gas chromatography using hep-
takis(6-O-TBDMS-2,3-O-methyl)-b-cyclodextrin as the
stationary phase. The NMR spectra were measured on
a Bruker AMX 400 and on AMX 500 with tetramethyl-
silane as the internal standard. The solvent normally
used for co- and terpolymers was a (CF3)2CDOD–
CDCl3 1:1 mixture. 2D spectra (COSY
well as HC- and HCC-correlation) were employed to
obtain correct assignment.
The characterization of dimethyl 2-phenylbutane-
dioate (8) [33] and of (E)-1,4-diphenylpent-1-en-3-one
(10) [34] was already reported. 2,4,7-Triphenyloct-1-en-
3,6-dione (7) and 2,4-diphenylpent-1-en-3-one (9) were
isolated through chromatography on silica from car-
bonylation mixtures of styrene obtained as previously
described [35].
,
INADEQUATE as
4.2.2. Copolymerization reaction of ethene and CO
A similar procedure under comparable conditions
was used for the copolymerization reaction of ethene
and CO (entry 2 in Table 1). 50 ml of toluene, the
solvent, were added to 10 ml methanol. Ethene (485
mmol) was added with a ‘Bu¨chi press-flow gas con-
troller bpc’. During the copolymerization reaction (41
h), the pressure was kept constant by adding a gas
mixture of 1:1 ethene–CO. Yield 0.56 g (productivity
20.2 mmol g−1(Pd) h).
2,4,7-Triphenyl-oct-1-en-3,6-dion (7) was obtained as
a mixture of the two diastereomers (D1 and D2).
1H-NMR (CDCl3, 500 MHz): 1.39 (d, 3H, CH3 (D1 or
4.2.3. Terpolymerization reaction of styrene, ethene and
CO
For the terpolymerisation of ethene, styrene and CO
a similar procedure to that of the copolymerization of
3
D2), J(H,H)=7.0 Hz), 1.41 (d, 3H, CH3 (D1 or D2),
2
3J(H,H)=7.1 Hz), 2.54 (dd, 1H, CH2 (D1), J(H,H)=