Table 1 Products obtained from the reactions of ammonia with EDA
(1a, Scheme 1)a
Table 2 Products obtained from the reactions of ammonia with the
diazoester 1b (Scheme 1)a
Reaction
T/u C time/h
Reaction
T/u C time/min Selectivity
Entry Catalyst
Solvent ‘‘NH3’’
Gas
Selectivity
Entry Catalyst Solvent ‘‘NH3’’
1
2
Rh2(OAc)4 THF
6
25
25
24
5
No reaction
5a (97%)
4a (3%)
2a (73%)
4a (27%)
4a (100%)
2a (100%)
4a (100%)
1
2
7b
7b
7b
THF
THF
THF
Gas
NH4OAc 65
2b 65
65
3
2
2
2b (91%)
3b (9%)
2b (68%)
3b (32%)
3b (100%)
THF
Gas
3
7a
Ether
Gas
25
5
3
a
4
5
6
a
7b
7b
7b
Ether
THF
THF
Gas
Gas
25
25
3
Reaction conditions as in Table 1, except of the temperature.
1
10 min
Specific amounts of reagents and mol% relative to catalyst were as
follows. Entry 1: 20 mg 1b, 107 mol%, active NH3 purging. Entry 2:
20 mg 1b, 107 mol%, NH4OAc (1 gr, 12.9 mmol). Entry 3: 20 mg
1b, 107 mol%, 2b (18.3 mg, 0.156 mmol).
NH4OAc 25
The solutions (7 mL) containing all reagents and 1 mg catalyst
were mixed until complete disappearance of EDA was assured by
TLC. NMR spectroscopy, GC/MS, and GC were used for
identification of the reaction products and their relative yields.
Control reactions revealed that none of the products is obtained
without catalyst. Specific amounts of reagents and mol% relative to
catalyst were as follows. Entry 1: 118 mL EDA, 500 mol%. Entry 2:
50 mL EDA, 475 mol%. Entry 3: 100 mL EDA, 1000 mol%. Entry 4:
100 mL EDA, 651 mol%. Entry 5: 153 mL EDA 1000 mol% (0.2 M)
and either saturated NH3 solution (0.46 M) or under active NH3
purging. Entry 6: 153 mL EDA, 1000 mol%, NH4OAc (1 g,
12.9 mmol).
and diazoesters. Mechanistic investigations of this catalytic process
and advantageous extension of the unique features for synthetic
purposes are currently carried out in our laboratories and will soon
be reported.
The German–Israel Project Cooperation (DIP F 6.2) is grate-
fully acknowledged for financial support of this work.{
Notes and references
ether (entries 3–4). Consistent with this assumption, only the
product from single activation of ammonia (2a) was obtained
when the reaction was performed in either saturated NH3/THF
solution (0.46 M by titration vs. 0.20 M EDA) or under NH3 flow
(entry 5). The glycine ester 2a from these reactions was isolated as
the trifuoroacetic acid salt in 81 and 87% yield,11 respectively,
corresponding to 810–870 catalytic turnovers.
{ Procedure for quantitative reactions of ammonia with EDA, leading to
2a as exclusive product: THF (7 mL) was purged with ammonia gas for
15 minutes, leading a solution that is 0.46 M NH3 (titration). Neat EDA
(153 mL, 1.46 mmol, 0.2 M) was added to the solution, followed by solid
catalyst (1 mg, 1.46 mmol, 0.1 mol% relative to EDA). This induced a color
change from brown to red and nitrogen gas emission. The consumption of
EDA was followed by TLC examinations. The solvent (and residual
ammonia) was evaporated after 1 h, the oily residue was dissolved in
diethyl ether (1 mL), and TFA (0.11 mL) was added. The TFA salt of
glycine ethyl ester (mp = 138 uC)9 separated from the solution, yielding
257 mg (81% yield relative to EDA) as white salt. Alternatively, the
reaction was carried out under a slow stream of gaseous ammonia, yielding
275 mg (87% yield) after the same workup procedure.
The results presented so far clearly demonstrate that these
catalysts can utilize ammonia as the nitrogen atom source of
amino acid derivatives, that the reactivity of ammonia in this
system is only slightly smaller than of the produced amines (2a and
3a) and that the iron complex of the cheapest and most accessible
porphyrin (7b) is an excellent catalyst for the transformation. A
demonstration of these conclusions is provided in Fig. 1, which
compares the 7b-catalyzed reactions of EDA with ammonia (from
ammonium acetate) and aniline. Bubbles due to the release of N2
developed within seconds even in the reaction with ammonia,
although with aniline this occurred more vigorously. No reaction
took place under identical conditions within 24 h when Rh2(OAc)4
was used. Nitrogen evolution due to EDA decomposition started
only after all ammonia was evaporated and 5a and diethyl
fumarate were the sole products in that case.
1 (a) M. R. Fructos, T. R. Belderrain, M. C. Nicasio, S. P. Nolan,
H. Kaur, M. M. D´ıaz-Requejo and P. J. Pe´rez, J. Am. Chem. Soc., 2004,
126, 10846; (b) E. Galardon, P. L. Maux and G. Simonneaux, J. Chem.
Soc., Perkin Trans. 1, 1997, 2455; (c) Y. Wang, Y. Zhu, Z. Chen, A. Mi,
W. Hu and M. P. Doyle, Org. Lett., 2003, 5, 3923; (d) H. Haoxi,
Y. Wang, Z. Chen and W. Hu, Adv. Synth. Catal., 2005, 347, 531; (e)
K. E. Bashford, A. L. Cooper, P. D. Kane, C. J. Moody, S. Muthusamy
and E. Swann, J. Chem. Soc., Perkin Trans. 1, 2002, 1672; (f)
M. P. Doyle, M. A. McKervey and T. Ye, in Modern Catalytic Methods
for Organic Synthesis with Diazo Compounds, John Wiley & Sons, New
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A. C. B. Burtoloso and C. R. D. Correia, J. Organomet. Chem., 2005,
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The iron porphyrin 7b was further tested as a possible catalyst
for the preparation of alanine esters as well (Scheme 1, R = CH3).
The methyl-substituted diazoester (ethyl diazopropionate, 1b)12
was less reactive than EDA and did not react with ammonia at
room temperature, but reactions performed at 65 uC were
nevertheless complete within minutes (Table 2, entries 1–2). The
alanine ester 2b and the doubly substituted ammonia derivative
(diethyl 2, 29-iminodipropionate 3b) were the only products,9,13
obtained in 10 : 1 and 2 : 1 ratios from dissolved ammonia and
ammonium acetate, respectively. The fully substituted 4b was not
obtained in these reactions, even when 2b was used as the starting
material (entry 3, clean transformation into 3b).
2 (a) For iron corroles in other catalytic processes, see: Z. Gross,
L. Simkhovich and N. Galili, Chem. Commun., 1999, 599;
L. Simkhovich, A. Mahammed, I. Goldberg and Z. Gross, Chem.
Eur. J., 2001, 7, 1041; L. Simkhovich and Z. Gross, Tetrahedron Lett.,
2001, 42, 8089; J. Grodkowski, P. Neta, E. Fujita, A. Mahammed,
L. Simkhovich and Z. Gross, J. Phys. Chem. A, 2002, 106, 4772;
A. Mahammed and Z. Gross, J. Am. Chem. Soc., 2005, 127, 2883;
A. Mahammed and Z. Gross, Angew. Chem., Int. Ed., 2006, DOI:
10.1002/anie.200601399; (b) For catalysis by other metallocorroles, see:
Z. Gross, G. Golubkov and L. Simkhovich, Angew. Chem., Int. Ed.,
2000, 39, 4045; A. Mahammed, H. B. Gray, A. E. Meier-Callahan and
Z. Gross, J. Am. Chem. Soc., 2003, 125, 1162; H.-Y. Liu, T.-S. Lai,
L.-L. Yeung and C. K. Chang, Org. Lett., 2003, 5, 617; J. P. Collman,
L. Zeng and R. A. Decre´au, Chem. Commun., 2003, 2974; Z. Gross and
H. B. Gray, Adv. Synth. Catal., 2004, 346, 165; S. H. Wang,
B. S. Mandimutsira, R. Todd, B. Ramdhanie, J. P. Fox and
D. P. Goldberg, J. Am. Chem. Soc., 2004, 126, 18; I. Luobeznova,
M. Raizman, I. Goldberg and Z. Gross, Inorg. Chem., 2006, 45, 386;
The iron complexes of porphyrins (and to a lesser extent
corroles as well) are the first reported metal complexes to catalyze
the formation of N-free glycine and alanine esters from ammonia
4478 | Chem. Commun., 2006, 4477–4479
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