Paper
Catalysis Science & Technology
were >98% by 1H NMR spectroscopic analysis. These reaction
times are similar to the 15–20 h reaction times reported by
Parrish and Buchwald for a similar Pd(0) catalyst formed
in situ by a similar DVB-crosslinked polystyrene supported
ligand and by the soluble polystyrene ligand described above.
Isolated yields of products from are listed in Table 1. These
isolated yields like those reported above are an average yield
for 5 cycles since the five 1 mmol scale reactions were com-
bined prior to workup.
Recycling of the PIB catalyst 21 was effected with product
separation in methanol and catalyst recycling in heptane.
This separation was effective as was the case with polyIJ4-
alkylstyrene) supported Pd ligated by the phosphine 15 with
Pd leaching of 0.1% Pd leaching or 0.02% in reactions that
used 1.5 mol% of the Pd catalyst 22 in coupling of bromo-
benzene with N-methylaniline or morpholine, respectively.
The product phases were colorless.
synthesis. Either of these polymers form Pd catalysts that
show excellent catalytic activity in Buchwald–Hartwig
amination reactions affording good isolated yields of
arylamines from secondary alkyl or benzylic amines and
bromobenzene or chlorobenzene. Successful catalyst
recycling was effective and using biphasic liquid/liquid sepa-
ration. Pd leaching was analyzed by ICP-MS analysis and was
uniformly very low with typical values for Pd leaching consis-
tently <0.1% for reactions that used 1.5 or 1 mol% of the Pd
catalyst.
Acknowledgements
Initial support of our work on these phase selectively soluble
polymers by the R. A. Welch Foundation (grant A-0639) and of
our work on polyIJ4-alkylstyrene) and polyisobutylene
supported Pd catalysts by the Qatar National Research Foun-
We did not examine the polar phase that contained
ca. 0.1% of leached Pd for catalytic activity in any of these
reactions. The concentration of Pd in that phase was ca.
1000-fold lower that the concentration of Pd in the heptane
phase and at these Pd concentrations, catalyst activity would
not be significant.
Both the polyIJ4-alkylstyrene) terpolymer support above
and the commercial PIB used below have low PDI values (the
PIB reportedly has a PDI of ca. 1.3).23 While the narrow PDI
may affect leaching of catalyst in the first or second cycle, the
high heptane phase solubility of these polymers is likely the
most important feature in achieving low Pd leaching. For
example, a simple diphenylphosphine-ligated Pd catalysts
attached to a similar polyIJ4-alkylstyrene) terpolymer prepared
by conventional AIBN polymerization had Pd leaching that is
only slightly higher than that for Pd ligated by 15.20
We also explored an alternative product isolation scheme
with the PIB-bound catalyst 22. This scheme used Amberlyst
15 as an in situ sequestrant following a protocol we had previ-
ously described.24
dation
acknowledged.
(project
number
4-081-1-016)
is
gratefully
Notes and references
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Conclusions
In summary, we have prepared two versions of a soluble poly-
mer supported hindered dicyclohexylbiarylphosphine ligand.
RAFT chemistry afforded highly phase selectively soluble
polyIJ4-alkylstyrene)supports that incorporate such ligands by
post-polymerization phosphinylation or directly using
a
phosphine-containing monomer. Polyisobutylene with termi-
nal dicyclohexylbiarylphosphine groups can be prepared from
a bromo-terminated polyisobutylene by a Williamson ether
2382 | Catal. Sci. Technol., 2015, 5, 2378–2383
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