COMMUNICATION
of our knowledge represents the first application of continu-
ly full substrate conversion and a 81% isolated yield of the
desired acetal 3a (Table 1, entry 10, see also Table S1). The
lack of product formation in control experiments without
oxidant clearly underlines the importance of both metal cat-
alyst and oxidant (Table 1, entries 11 and 12).
Encouraged by the results obtained in the optimization
experiments described above, a number of analogous CDC
transformations varying both reaction partners were studied
(Table 2). Cyclic ethers such as 1,4-dioxane (2a) and THF
(2b) reacted smoothly with different 2-carbonyl-substituted
phenol derivatives (1a–e) to provide the corresponding
acetal products (3a–j) in moderate to excellent yields.
Linear, unsymmetrical ethers such as 1,2-dimethoxyethane
(DME; 2c) furnished a mixture of products resulting from
[11]
À
ous-flow processing to C H activation chemistry.
Previous investigations from our laboratory on the
copper-catalyzed CDC reaction of b-dicarbonyl derivatives
or 2-carbonyl-substituted phenols with N,N’-disubstituted
formamides mediated by stoichiometric amounts of TBHP
have indicated that the carbonyl group adjacent to the hy-
droxy moiety acts as directing group, and therefore consti-
tutes an essential functionality for efficient coupling reac-
tions.[12] To explore the ability of these substrates in a puta-
tive CDC reaction with ethers, the coupling behavior of 2-
hydroxyacetophenone (1a) and 1,4-dioxane (2a) under dif-
ferent conditions was evaluated (Table 1). Gratifyingly, the
À
competitive C H activation of the internal methylene and
Table 1. Optimization of reaction conditions.[a]
the terminal methyl group, respectively (3k–3n). Methyl
tert-butyl ether (MTBE; bp. 568C) as well as simple Et2O
(bp. 358C) remained completely unreactive under these re-
action conditions operating at the reflux temperature of the
solvent (3p–3q). Subsequently, without further reoptimiza-
tion, the substrate scope was further extended to b-keto-
Entry Catalyst [mol%]
Oxidant [equiv]
T [8C] 3a [%][b]
AHCTUNGTRENNUNG
1
2
3
4
5
6
7
8
9
Cu
(OAc)2 (10)
TBHP in water (1.5)
80
80
80
80
80
80
80
80
100
29
24
–
24
–
–
–
31
69
81
–
CuN
volving a peroxide/ether mixture to a safe and scalable con-
tinuous-flow regime,[13] we first attempted to reduce the ini-
tially optimized reaction time of 3 h under reflux conditions
(Table 1) to something more suitable for a continuous pro-
CuCl2 (10)
CuCl (10)
TBHP in water (1.5)
TBHP in water (1.5)
H2O2 (1.5)
Cu
Cu(OAc)2 (10)
Cu(OAc)2 (10)
Cu(OAc)2 (10)
Cu(OAc)2 (5)
Cu(OAc)2 (5)
A
R
NaOCl (1.5)
DTBP[c] (1.5)
AHCTUNGTREGcNNUN essing approach (<30 min). Therefore the CDC of 2-hy-
ACHTUNGTRENNUNG
N
TBHP in decane (1.5)
TBHP in water (2.2)
TBHP in decane (2.2) 100
TBHP in decane (2.2) 100
R
10
11
12
R
Table 2. Substrate scope in the Cu
ACHTUNGRTEN(NUNG OAc)2-catalyzed coupling of 2-car-
bonyl-substituted phenols with ethers.[a]
–
CuN
–
100
–
[a] Reaction conditions: 1a (1 mmol), 2a (2 mL), 3 h, unless noted other-
wise. [b] Yields isolated after chromatograhpy. [c] Di-tert-butyl hydro-
ACHTUNGTRENNUNGperoxide.
Entry
1
2
Product
3a
Yield
[%][b]
use of 10 mol% of CuACHTNUGTRNEUNG(OAc)2 as catalyst in combination
with aqueous (70%) TBHP at 808C for 3 h did indeed
afford the desired acetal (3a) in moderate yield (Table 1,
entry 1). Surprisingly, all other tested CuII species, with the
1
2
3
4
5
79
80
55
85
28
exception of CuACHTUNGTRENNUNG(OAc)2 hydrate, were completely inactive
3b
(Table 1, entries 2 and 3, see also Table S1 in the Supporting
Information), whereas several CuI catalysts showed moder-
ate catalytic activity (Table 1, entry 4 and Table S1). The
nature of the oxidant was also found to be a crucial factor in
this transformation; no desired product was observed by re-
placing TBHP with a variety of other common oxidants
(Table 1, entries 5–7, see also Table S1). Moving from aque-
ous TBHP to a commercially available solution of TBHP in
decane (5–6m), the product yield could be slightly increased
(Table 1, entry 8) and further experiments at elevated tem-
perature clearly demonstrated a reaction enhancement using
the water-free variant (Table 1, entries 9 and 10). A system-
atic reaction optimization using both increased temperatures
and higher amounts of oxidant in combination with a signifi-
cantly reduced catalyst loading ultimately resulted in virtual-
3c
3d
3e
6
7
8
9
1a
1b
1c
1d
1e
3 f
3g
3h
3i
74
66
39
82
45
10
3j
Chem. Eur. J. 2012, 18, 6124 – 6128
ꢀ 2012 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
6125