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M. Karlsson et al. / Journal of Molecular Catalysis A: Chemical 259 (2006) 231–237
Table 2
the stability of the palladium alkyl complex formed by insertion
of the olefin in the Pd–H bond, bulkier ligands promote for-
mation of the linear alkyl complex. Based on steric arguments
alone, the N3P ligand would give predominantly the branched
isomer. On the other hand, if the insertion of the olefin in the
Pd–H bonds yields two isomeric Pd-alkyls (linear and branched)
which are in rapid equilibrium and which insert CO at differ-
ent rates, there would be mainly electronic rather than steric
control. Unfortunately, since the two spectator ligands N3P and
TPPTS differ with respect to both steric bulk and donor strength,
they do not provide a clear-cut answer as to the cause of the
regio-control.
Hydrocarboxylation of penteneoic acid
Substrate (pentenoic acid)
Conversion (%)
n/i
Run (1)
Run (2)
94
91
3.1
3.1
General reaction conditions: PCO = 50 bar; T = 100 ◦C; precursor: PdCl2-
(PhCN)2 (0.016 mmol); ligand: N3P (0.14 mmol); substrate/Pd: 560; pH 1.8;
acid: MeSO3H; solvent: H2O; total volume: 15 ml; reaction time: 1 h.
of the catalyst into toluene represents a reverse procedure, in
that the aqueous phase contains the product, for which any
appropriate method of work-up can be used to recover the
product.
3.5. Mass-transfer
The results using 4-pentenoic acid, displayed in Table 2,
demonstrate that the reverse recycling procedure can be applied
with only a minor loss in activity. Pentenoic acid reaches 94%
conversion in one hour while styrene needs five hours for 92%
conversion. This, again, is a strong indication that the solubil-
ity of styrene limits its rate of reaction. The linear to branched
ratio of 3.1 is slightly higher than the selectivity in the 1-octene
reaction. Coordination of the carbonyl group on 4-pentenoic
acid to the palladium atom in the alkyl intermediates would
lead to seven or six-membered ring structures for the linear and
branched alkyl complexes, respectively. Based on the higher sta-
bility of a six-membered ring, the branched isomer is expected,
providing carbonyl interaction occurs. The preferential forma-
tion of the linear isomer observed, however, indicates that the
carboxylic group on the substrate plays no role in determining
the regioselectivity.
A slow rate of phase boundary mass transfer frequently
causes problems with the reaction rate in biphasic reaction mix-
tures, and this is also the case when applying catalyst based
on the N3P ligand in the hydrocarboxylation reaction. This is
evident by comparing the conversions for 1-octene and styrene
under the same reaction conditions. Styrene, having a reported
solubility of 1.1 mmol/l in water [2], is much more water-soluble
than 1-octene and has a conversion of 92% while 1-octene of
only 30% (Table 1). Still, it is probably the solubility of styrene
in water which determines its reaction rate. Additionally, we
observed that 1-octene slowly isomerises under the reaction
conditions, and the product mixture contained approximately
10% of 2-ethyl heptanoic acid. The influence of phase bound-
ary mass transfer on the reaction rate also became evident by
comparing reaction rates for both styrene and 1-octene in neat
form or dissolved in toluene—a much higher reaction rate was
found by adding the reactant olefins in undiluted form directly
to the aqueous reaction mixture. Even so, the reaction rate is
most likely limited by the low water solubility of these two
substrates.
Besides the main product, adipic acid, 8% 2-methyl-1,5-
pentanedioic acid was also observed as a result of isomerization
of 4-pentenoic acid.
4. Conclusions
The importance of mass-transfer rates is also nicely
demonstrated in the reaction of 4-penteneoic acid. Initially,
this substrate was chosen to evaluate the possibility of using
a “reverse” recycling procedure to recover and reuse a cat-
alytic system based on an amphiphilic phosphine ligand.
4-Penteneoic acid represents a class of alkenes highly soluble
in water, and its product in the hydrocarboxylation reaction,
adipic acid, is even more water-soluble. This, of course,
makes the separation of catalyst and product, and hence the
catalyst recycling, cumbersome. Although in the case of
penteneoic acid it is possible to separate the substrate and the
product from the catalyst by repeated extractions, this method
poses the risk of introducing air into the system, ultimately
leading to oxidation of phosphine ligands. One can also easily
find substrates/products with solubility so close to that of
the amphiphilic catalysts that separation becomes virtually
impossible. In such a case, the amphiphilic catalyst presents a
clear advantage over the mere water-soluble ones (e.g. catalysts
employing sulfonated phosphines), since an amphiphilic cata-
lyst can be transferred into an organic phase while keeping the
reactants/products in a basified aqueous phase. Compared to the
normal recycling procedure for amphiphilic catalysts, extraction
The hydrocarboxylation of styrene, 1-octene and 4-pente-
neoic acid using a palladium catalyst employing the amphiphilic
phosphine N3P demonstrates that the reaction rate is strongly
dependent on the solubility of the substrates.
Using N3P in the hydrocarboxylation reaction it is possible
to recycle the catalyst, both by extracting the substrate and by
extracting the catalyst into an organic solvent. This is a clear
advantage compared to the more commonly used ligand, trisul-
fonated triphenylphosphine (TPPTS). The catalyst employing
N3P also shows an inverted regioselectivity compared to the
TPPTS system.
A whole range of reaction intermediates, from zerovalent
complexes to alkyl and acyl complexes were identified by means
of NMR.
Acknowledgements
Financial support from TFR (the Swedish Research Council
for Engineering Sciences) and SSF (Swedish Foundation for
Strategic research) is gratefully acknowledged.