Dalton Transactions
Paper
characteristics of the “(P–P)Ni” fragment (dicationic versus
neutral) and this fact has given us a better insight aiming to
improve the activity and selectivity of this nickel catalyzed
process. Current studies are, in fact, underway to enhance
such selectivity with other phosphite and phosphonite ligands
and aiming to adapt this method for use under a non-inert
atmosphere.
Table 6 Catalytic hydroamination of diphenylacetylene (1n)
Entry
Cat.
T (°C)
t (h)
2na (%)
3na (%)
1
2
3
4
5
6
[(PEt3)2NiCl2] 12
140
140
140
140
140
160
72
72
72
72
216
216
22
39
16
27
36
16
11
3
0
6
3
[(P(OEt)3)2NiCl2] 15
[(PPh3)2NiCl2] 16
[(P(OPh)3)2NiCl2] 14
[(P(OEt)3)2NiCl2] 15
[(P(OEt)3)2NiCl2] 15
Acknowledgements
25
Financial support from CONACYT (178265) and UNAM-DGAPA
(IN-210613) is gratefully acknowledged. A. R.-S. thanks
CONACYT (254535) for a scholarship for graduate studies. We
also thank Dr Alma Arévalo for her technical assistance.
a Chromatographic yield.
The alkynes employed in Table 5 are more activated than
1-phenyl-1-propyne and therefore better yields and selectivities
could be successfully obtained (Schemes S14–S21, ESI†). In
fact, the hydrogenation of the starting material was completely
inhibited. In previous experiments without the additional
argon pressure and by using 1, 3 or 6, the hydroamination of
1n and 1g was not observed at all (vide supra). In sharp con-
trast, with the conditions shown in Table 5, the desired enam-
ines for such alkynes were successfully obtained in moderate
yields (entries 1 and 2). In the same way, the yield for the
hydroamination of 1e (entry 4) was dramatically higher (91%)
than that with the use of dicationic nickel (1) at a lower
pressure (Table 2, entry 1, 64%).
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Dalton Trans., 2014, 43, 1762–1768 | 1767