A. Wolfson et al. / Tetrahedron: Asymmetry 13 (2002) 465–468
467
2. Experimental
2.1. Preparation of the catalyst
steps: first, sorption of a particular solvent into the
polymer takes place depending on the nature of both
polymer and solvent; this is followed by dissolution of
the chiral complex. Changing the nature of the film and
the solvent influences the permeability of the reactants
(substrate and hydrogen).
The Rh-salt [bis(1,5-cyclooctadiene) rhodium(l)trifluoro-
methanesulfonate, 99%] and methyl-DuPHOS ligand
[(−)-1,2-bis-(2R,5R)-2,5-dimethylphosphacyclopentyl)-
benzene, 98%] were purchased from Strem. The Rh-
MeDuPHOS catalyst was prepared in a glove box by
dissolving the rhodium salt and the DuPHOS ligand
separately in methanol (5 mmol salt in methanol (0.25
mL) and ligand (6 mmol) in methanol (0.2 mL), respec-
tively) and stirring for 40 min. The ligand solution (5%
excess) was added dropwise to the rhodium salt solution
under constant stirring. After 30 minutes, the methanol
was flushed out with nitrogen.
We tested the occluded complexes as catalysts in the
asymmetric hydrogenation of methyl 2-acetamidoacry-
late (MAC) in aqueous medium with Rh-MeDuPHOS
occluded in PVA films, as illustrated in Table 3. The
initial results obtained with Rh-MeDuPHOS occluded
in PVA films (Table 3) showed that it was possible to
perform the hydrogenation reaction in water and also
to recycle the heterogeneous catalyst (entries 3 and 4)
without any subsequent loss in activity or enantioselec-
tivity. The reaction rate when physically crosslinked
PVA film was used was slightly higher than that
observed for chemically crosslinked film, probably due
to the higher permeabilities of the physically
crosslinked support. The PVA films tested were much
denser than the PDMS film and the sorption of water
to PVA film was higher. Although no complete com-
parison can be made between PVA and PDMS films,
occlusion of the chiral metal complex in hydrophilic
and hydrophobic films demonstrates the feasibility of
working with different polymers and solvents.
2.2. Preparation of films
Polyvinyl alcohol films were prepared using two
crosslinking methods:10 (a) physical crosslinking in
water and (b) chemical crosslinking in water with the
addition of malic acid as crosslinker and acetic acid or
hydrochloric acid as catalyst. In both cases, an amount
of 0.5 g PVA (99% hydrolyzed, MW=50000, purchased
from Aldrich) was dissolved in distilled (5 g) water by
warming to 50°C for 5 min (in some cases ethylene
glycol was used instead of water, in which case the
mixture was warmed to 120°C). The chiral complex was
then dissolved in methanol (0.5 mL), added to the PVA
solution and poured into a Petri dish. Water was evap-
orated in a vacuum oven at 80°C for 3 h. Evaporation
was performed under a nitrogen atmosphere. After
evaporation the film was easily removed from the Petri
dish and added in pieces to the reaction mixture in the
reactor. For the chemically crosslinked PVA film, 3
wt% each of malic acid and acetic acid (both purchased
from Aldrich) were dissolved in water (5 mL) before the
addition of PVA (0.5 g).
In conclusion, for the first time a chiral transition-metal
complex was successfully incorporated into polyvinyl
alcohol films. The preparation of the heterogeneous
system was very easy and did not involve modification
of the metal complex. Leaching of Rh-MeDuPHOS
from the PVA film was studied and compared to that
from the PDMS system. It was found that using a poor
solvent for the chiral complex prevents leaching. The
heterogeneous catalytic system was successfully reused
without loss of activity and enantioselectivity. Other
substrates and complexes will have to be tested in order
to determine the scope and limitations of this new
catalytic system.
2.3. Leaching procedure
Leaching of the complex and solvent sorption were
tested in various solvents (20 mL) for 24 h. The extent
of leaching of the metal complex from the polymer
matrices was measured by analyzing the liquid phase
after separation with a PQ3/VG ICP-MS system. The
sorption of the solvents was measured by weighing the
polymer before and after sorption.
Table 3. Enantioselective hydrogenation of methyl 2-
acetamidoacrylate with Rh-MeDuPHOS occluded in PVA
and PDMS filmsa
Entry
Solvent
TOF (h−1 b
)
E.e. (%)
2.4. Typical hydrogenation procedure
1
2
3
4
Waterc
12.6
14.9
12.4
12.2
96.9
96.1
95.7
95.1
A 25 mL reactor with magnetic stirring was used for
both the homogeneous and the heterogeneous reac-
tions. In the homogeneous reactions, the complex was
dissolved in the reaction solvent. In the heterogeneous-
catalyzed reactions the film was added in pieces to the
reaction medium under a nitrogen atmosphere. A vol-
ume of solvent (18 mL) was added to the reactor
together with the substrate (0.1 g). The reaction was
performed at 25°C with high-purity hydrogen
(99.995%) at a pressure of 2 bar. Samples were with-
drawn periodically to determine the reaction rate and
Waterd
Watere (first cycle)
Watere (second cycle)
a Reaction conditions: 25°C, H2 (2 atm), MAC (0.1 g), solvent (19
mL), catalyst (10 mmol).
b After 6 h.
c PDMS dimethylvinyl terminated, average molecular weight of 5426,
with 20 wt% silica.
d Physically crosslinked PVA.
e Chemically crosslinked PVA.