to Cu(I) in iPrOH,12 we carried out the AAC reaction
between 2-picolylazide (1) and phenylacetylene (2) in
tBuOH, iPrOH, EtOH, and MeOH (Table 1, entries 1-4)
with 5 mol % CuCl2 loading. The reactions in iPrOH and
EtOH proceeded, albeit sluggishly. The isolated yield reached
79% in MeOH after 18 h. In tBuOH, the reaction failed to
afford an identifiable amount of 3 by thin-layer chromatog-
raphy (TLC). The fact that only readily oxidizable alcohols
(MeOH, EtOH, and iPrOH) allowed the formation of a
detectable amount of the product supported the hypothesis
that a catalytic Cu(I) species was generated via the reduction
of CuCl2 (Scheme 1A).
the catalytic Cu(I) species that allows the AAC reaction to
proceed (Scheme 1B) in tBuOH. The Glaser induction period
to generate Cu(I) species was observed by Mizuno et al. in
their catalytic AAC processes using silicotungstate- and
alumina-supported Cu(II).16
Scheme 1
.
Two Processes by Which Catalytic Cu(I) Species
Might Have Been Generated
Table 1. Effects of Copper Source and Solvent on Reaction
Yield After 18 h at rta
It should be noted that the “catalytic” effect of Cu(OAc)2
on AAC reactions was reported by Kantam et al. in 2006.17
In their procedure, satisfactory yields were achieved with
20 mol % catalyst loading in aqueous solutions for 20 h.
Kantam et al. postulated a direct participation of Cu(II) in
the catalysis. We, on the other hand, hypothesize that under
the reported conditions at least two processes, alcohol
oxidation and homocoupling of terminal alkyne by Cu(OAc)2
(Scheme 1), may generate the needed Cu(I) to complete the
catalytic cycle of the AAC reaction proposed and substanti-
ated by Sharpless, Meldal, and others.10,18 It is conceivable
that the efficiencies of these “autoreduction”19 processes are
highly condition-dependent. For instance, in the presence of
ligands that favor the +1 oxidation state of copper, the
reduction of Cu(II) is known to proceed in a deceptively
effortless manner.20
entry
copper source
copper loading
solvent
yield
1
2
3
4
5
6
7
8
9
CuCl2
CuCl2
CuCl2
CuCl2
CuSO4
CuSO4
Cu(OAc)2
Cu(OAc)2
CuCl2 + NaOAc
5 mol %
5 mol %
5 mol %
5 mol %
5 mol %
5 mol %
5 mol %
5 mol %
5 mol %
tBuOH
iPrOH
EtOH
MeOH
MeOH
tBuOH
MeOH
tBuOH
tBuOH
NDb
4%
17%
79%
81%
6%
90%
>95%
88%
a 0.2-0.25 mmol of 1 and 0.3 mmol of 2 in 0.5 mL of solvent. b ND:
Not detected by thin-layer chromatography (TLC).
On the basis of the postulate that either processes A or B
or both may afford the catalytic Cu(I) species, two reaction
conditions that favor either process were selected to evaluate
various azide and alkyne substrates. Condition A entails 5
mol % CuSO4 in MeOH where Cu(II) reduction by MeOH
is presumably the major process to generate the Cu(I) species.
The effect of counterion was studied using three Cu(II)
salts, CuCl2 (entry 4), CuSO4 (entry 5), and Cu(OAc)2 (entry
7), in MeOH. All three counterions gave satisfactory yields
after 18 h. However, unlike CuSO4 and CuCl2, Cu(OAc)2
enabled a highly efficient reaction in tBuOH (>95%, entry
8). To eliminate the possibility that Cu(OAc)2 may have been
contaminated by a miniscule amount of Cu(I) species, the
reaction was run using 5 mol % of CuCl2 (99.999% pure),
which is inactive in tBuOH (Table 1, entry 1), and NaOAc
each in tBuOH (entry 9). An 88% yield was achieved. This
observation forced us to formulate an alternative hypothesis
accounting for the reaction in tBuOH, which is not prone to
oxidation (CuSO4 enabled a 6% yield in tBuOH, entry 6).13
It is known that terminal alkynes may undergo Cu(II)-
catalyzed oxidative homocouping reactions to afford diynes
(the Glaser reaction).14 In the classical Eglinton protocol,15
Cu(OAc)2 is the most active Cu(II) agent. We hypothesize
that a Glaser-type reaction may be taking place to produce
(16) (a) Kamata, K.; Nakagawa, Y.; Yamaguchi, K.; Mizuno, N. J. Am.
Chem. Soc. 2008, 130, 15304–15310. (b) Katayama, T.; Kamata, K.;
Yamaguchi, K.; Mizuno, N. ChemSusChem 2009, 2, 59–62.
(17) Reddy, K. R.; Rajgopal, K.; Kantam, M. L. Synlett 2006, 957–
959. For other examples appearing later where Cu(II) was postulated as
the catalytic species in AAC reactions, see:(a) Fukuzawa, S.-I.; Shimizu,
E.; Kikuchi, S. Synlett 2007, 2436–2438. (b) Reddy, K. R.; Rajgopal, K.;
Kantam, M. L. Catal. Lett. 2007, 114, 36–40. (c) Song, Y.-J.; Yoo, C.;
Hong, J.-T.; Kim, S.-J.; Son, S. U.; Jang, H.-Y. Bull. Korean Chem. Soc.
2008, 29, 1561–1564. (d) Namitharan, K.; Kumaaraja, M.; Pitchumani, K.
Chem.sEur. J. 2009, 15, 2755–2758.
(18) (a) Himo, F.; Lovell, T.; Hilgraf, R.; Rostovtsev, V. V.; Noodleman,
L.; Sharpless, K. B.; Fokin, V. V. J. Am. Chem. Soc. 2005, 127, 210–216.
(b) Rodionov, V. O.; Fokin, V. V.; Finn, M. G. Angew. Chem., Int. Ed.
2005, 44, 2210–2215. (c) Straub, B. F. Chem. Commun. 2007, 3868–3870.
(d) Nolte, C.; Mayer, P.; Straub, B. F. Angew. Chem., Int. Ed. 2007, 46,
2101–2103. (e) Ahlquist, M.; Fokin, V. V. Organometallics 2007, 26, 4380–
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(19) Kitagawa, S.; Munakata, M.; Higashie, A. Inorg. Chim. Acta 1984,
84, 79–84.
.
(12) Kirai, N.; Yamamoto, Y. Eur. J. Org. Chem. 2009, 1864–1867.
(13) The same reaction was observed to proceed to a small extent in
CH3CN. A comprehensive solvent scope study is planned in the future.
(14) Siemsen, P.; Livingston, R. C.; Diederich, F. Angew. Chem., Int.
Ed. 2000, 39, 2632–2657.
(20) (a) Musker, W. K.; Olmstead, M. M.; Kessler, R. M. Inorg. Chem.
1984, 23, 1764–1768. (b) Benzekri, A.; Cartier, C.; Latour, J.-M.; Limosin,
D.; Rey, P.; Verdaguer, M. Inorg. Chim. Acta 1996, 252, 413–420. (c)
Malachowski, M. R.; Adams, M.; Elia, N.; Rheingold, A. L.; Kelly, R. S.
J. Chem. Soc., Dalton Trans. 1999, 2177–2182. (d) Sarkar, S.; Patra, A.;
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