catalyst phase could be recycled in 5 consecutive runs without
loss in activity. Rh-analysis of the water layers by means of
atomic absorption spectrometry confirmed a quantitative
( > 99%) catalyst/product separation.
N-Acetyl-5-methoxytryptamine was subsequently prepared
in a one-pot procedure starting from allylamine (see ESI). By
successive acetylation of allylamine, selective hydroformyla-
tion, hydrazone formation with 4-methoxyphenylhydrazine
(HCl salt) and a Fischer indole reaction, melatonin was isolated
from the aqueous reaction mixture in 44% yield (not opti-
mised).
In conclusion, we have demonstrated that the hydro-
formylation of N-allylacetamide proceeds smoothly in a one-
phase aqueous medium, as well as in an aqueous–organic two-
phase protocol under mild reaction conditions. Although we
could not take full advantage of the rate accelerating effect of
water in the inverted two-phase catalyst system, the linear
aldehyde was obtained in high selectivity and efficient catalyst/
product separation was achieved. The organic soluble catalyst
was recycled and the aqueous product phase was applied
without purification in the synthesis of N-acetyl-5-methoxy-
tryptamine. Mechanistic details and the scope of the inverted
two-phase system are currently under investigation.
We thank Dr G. Papadogianakis and Dr G. Besenyei for the
fruitful discussions and Mr J. Padmos for the Rh-analysis.
Financial support by NWO-CW is also gratefully acknowl-
edged.
Scheme 2 Proposed intermediates in the Rh/tppts catalysed hydro-
formylation of N-allylacetamide.
The high partition coefficients of 4-acetamidobutanal and
3-acetamido-2-methylpropanal in the water layers forestalled
our attempts to extract them from the aqueous reaction mixtures
with an organic solvent. Especially in the synthesis of
pharmaceuticals the presence of traces of heavy metals is
undesirable. In order to achieve efficient product/catalyst
separation, we turned to an ‘inverse two-phase catalyst system’,
containing the hydrophobic Rh–PPh3 catalyst in a toluene–
water mixture. In such a system the catalyst remains dissolved
in the organic phase, while the products will move to the water
layer; the opposite of standard aqueous biphasic catalysis.
In the biphasic system, the Rh–PPh3 catalysed reaction (Exp.
6) proceeded considerably slower compared to Rh–tppts (Exp.
5), consistent with our observation (see above) that the reaction
rate decreases when the hydroformylation is carried out in an
apolar solvent, such as toluene. In addition, due to mass transfer
limitations, the reaction rate decreased substantially after ca.
50% conversion (see Fig. 1). Such a decrease was less
pronounced in the case of Rh–tppts, that operates in the aqueous
layer, where the substrate concentration remains sufficiently
high, resulting in a zero-order reaction profile until ca. 80%
conversion. Nevertheless, due to the presence of water, the
selectivity towards the aldehydes remained high (98%, Exp. 6)
and the Rh–PPh3 catalyst could conveniently be separated from
the aqueous product phase.
Notes and references
1 K. Weissermel and H. J. Arpe, Industrial Organic Chemistry, 3rd edn.
VCH, Weinheim, 1997; Applied Homogeneous Catalysis with Organo-
metallic Compounds, ed. B. Cornils and W. A. Herrmann, vol. 1, VCH,
Weinheim, 1996.
2 E. G. Kuntz, CHEMTECH, 1987, 570; Y. Chauvin, L. Mussmann and
H. Olivier, Angew. Chem., Int. Ed. Eng., 1995, 34, 2698; I. T. Horváth,
G. Kiss, R. A. Cook, J. E. Bond, P. A. Stevens, J. Rabai and E. J.
Mozeleski, J. Am. Chem. Soc., 998, 120, 3133; E. Lindner, T. Schneller,
F. Auer and H. A. Mayer, Angew. Chem., Int. Ed. Eng., 1999, 38,
2155.
3 H. H. Szmant, Organic building blocks of the chemical industry, Wiley,
New York, 1989; Ullmann’s Encyclopedia of Ind. Chem., Vol. A11,
VCH, Weinheim, Germany, p. 141.
4 C. Botteghi, R. Ganzerla, M. Lenarda and G. Moretti, J. Mol. Catal.,
1987, 40, 129; P. Eilbracht, L. Bärfacker, C. Buss, C. Hollmann, B. E.
Kitsos-Rzychon, C. L. Kranemann, T. Rische, R. Roggenbuck and A.
Schmidt, Chem. Rev., 1999, 99, 3329.
5 H. M. Hugel and D. J. Kennaway, Org. Prep. Proced. Int., 1995, 27,
1.
6 W. Marais and C. W. Holzapfel, Synth. Commun., 1998, 28, 3681.
7 I. Ojima and Z. Zhang, J. Org Chem., 1988, 53, 4422; I. Ojima and Z.
Zhang, J. Organomet. Chem., 1991, 417, 253; I. Ojima, A. Korda and
W. R. Shay, J. Org. Chem., 1991, 56, 2024; I. Ojima, Z. Zhang, A.
Korda, P. Ingallina and N. Clos, Adv. Chem., 1991, 56, 278; see also: S.
Sato, M. Takesada and H. Wakamatsu, Nippon Kagaku Zasshi, 1969,
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45, 2145.
Fig. 1 Reaction profiles of Exp. 5 and Exp. 6.
To increase the regioselectivity towards the linear aldehyde,
generally, rigid diphosphine ligands with a large bite angle are
used.9 We tested the Rh–Xantphos combination10 (Xantphos =
4,5-bis(diphenylphosphino)-9,9-dimethylxanthene) in our in-
verted two-phase system and, indeed, the l/b ratio increased to
20. The reaction rate, however, decreased dramatically to 31
8 G. Fremy, E. Monflier, J. F. Carpentier, Y. Castanet and A. Mortreux,
Angew. Chem., Int. Ed. Engl., 1995, 34, 1474.
9 For the hydroformylation of functionalised olefins in THF: G. D. Cuny
and S. L. Buchwald, J. Am. Chem. Soc., 1993, 115, 2066.
10 M. Kranenburg, Y. E. M. van der Burgt, P. C. J. Kamer, P. W. N. M. van
Leeuwen, K. Goubitz and J. Fraanje, Organometallics, 1995, 14,
3081.
h
1 (Table 1, Exp. 7). At 90 °C, in the presence of 0.2% catalyst,
a nearly quantitative conversion was reached in 10 h reaction
time with a small compromise in the l/b ratio. The organic
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Chem. Commun., 2000, 1363–1364