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H. T. Bonge, T. Hansen / Tetrahedron Letters 49 (2008) 57–61
Table 1. Initial screening
results seemed to be more reproducible at 30 °C than
at room temperature. A reaction time of 3 h, as chosen
to begin with, proved to be sufficient. Increasing the
reaction time to 7, 15 or 24 h had no effect on yields.
A reaction time of 1 h gave a 66% yield of 1, compared
to 75% after 3 h. Rigorously dry conditions did not
increase yields, whereas 0.3 equiv of added water pre-
vented completely the reaction. We originally believed
that 2 equiv of base was necessary. It did, however,
become apparent that the reaction was in fact catalytic
with regards to base, and as little as 0.6 equiv of potas-
sium fluoride was sufficient to obtain high a yield of 1
(Table 3, entry 2). Since both nitromethane and THF
are inexpensive and readily available, both were initially
used in a rather large excess. Experiments showed that
the amounts of THF and nitromethane could be
decreased to 5 equiv and 10 equiv, respectively, without
significant effect on the yields (Table 3, entries 6–8). The
amounts of all three reagents could not be reduced
simultaneously without lowering the yield (Table 3,
entry 12). To reduce the equivalents of THF and nitro-
methane, the amount of potassium fluoride had to be at
least 1.0 equiv.
Entry Catalyst
Catalyst Base
loading
(mol %)
Equiv
Yield
of base of 1a (%)
1
2
3
Rh2(esp)2
Rh2(esp)2
Rh2(esp)2
2.5
2.5
2.5
KF
1.0
1.0
1.0
2.2
75
69
32
55
43
26
0
42
34
33
12
10
KOAc
NaOAc
KF
4
5
6
7
Rh2(OOct)4 2.5
Rh2(OOct)4 2.5
Rh2(OOct)4 2.5
Rh2(OOct)4 2.5
Na2CO3 2.2
K2CO3
MgO
2.2
2.2
2.2
2.2
2.2
2.2
2.2
8
9
10
11
12
Rh2(OAc)2
Rh2(OAc)2
Rh2(OAc)2
Rh2(OAc)2
Rh2(OAc)2
10
10
10
10
10
KF
K3PO4
K2CO3
CsF
CsCO3
a Measured by internal standard (1,3,5-trimethoxy benzene) in 1H
NMR analysis of crude reaction mixture.
It was clear from the initial screening that the ligands on
the dirhodium core of the catalyst had a substantial
effect on the outcome of the reaction. Hence, the effect
of different catalysts and catalyst loadings was systemati-
cally examined (Table 2). Potassium fluoride was chosen
as the base for these and the following optimisation
experiments. Whereas Pd(OAc)2 and Cu(acac)2 failed
to catalyse the formation of 1 (entries 12 and 13), all
the Rh(II) catalysts tested provided 1. Ether cleavage
did not occur in the absence of catalyst. The bridged
catalyst Rh2(esp)2 was the catalyst of choice in the
previously described cyclopropanation reaction with
nitromethane.18 Once again, this catalyst proved the
most efficient, allowing for a rather low catalyst loading
while still giving good yields (entries 1–4). Reducing the
catalyst loading to only 1 mol % still gave a yield of 64%
(entry 4).
Having established a satisfactory set of reaction condi-
tions, we then proceeded to investigate the effect of other
hypervalent iodine compounds. The experiments were
performed at 30 °C, using a catalyst loading of
2.5 mol % and reagent amounts as shown in Table 3,
entry 8. PhI(OPiv)2 gave a 57% yield of 4-(nitro-
methoxy)butyl pivalate, the analogous product to 1.
This result confirmed that the carboxylate group in the
product originated from the hypervalent iodonium
source. With PhI(TFA)2 as the hypervalent iodine
compound, no formation of the TFA-derivative of 1
was observed. Iodosylbenzene, having no carboxylate
substituent on iodine, gave a complex product mixture.
These factors having been established, we started
investigating the effects of other parameters on the reac-
tion. Initially, all experiments were performed at room
temperature. However, more satisfactory results were
obtained when the temperature was increased to 30 °C.
The reaction showed a slight temperature dependence;
To examine the scope of the three-component coupling
reaction, a number of cyclic ethers were exposed to the
same reaction conditions as described for the previous
experiments. Table 4 shows the results from this exami-
nation, in which no steps were taken to optimise the
reaction conditions for the substrates in entries 2–10.
Table 2. Effect of catalyst and catalyst loading
Table 3. Effect of varying the amounts of reagents
Entry Catalyst
Catalyst loading (mol %) Yield of 1a (%)
Entry
KF
(equiv)
THF
(equiv)
MeNO2
(equiv)
Yield of
1a (%)
1
2
3
Rh2(esp)2
Rh2(esp)2
Rh2(esp)2
Rh2(esp)2
10
5
2.5
1
71
74
75
64
63
55
55
31
57
42
11
0
1
2
3
4
5
6
7
8
9
0.5
0.6
0.8
1.0
1.5
1.0
1.0
1.0
1.0
1.0
1.0
0.6
10
10
10
10
10
5
10
5
3
18.6
18.6
18.6
18.6
18.6
18.6
10
10
10
10
5
67
76
76
75
78
71
73
71
58
33
67
59
4
5
6
7
Rh2(OOct)4 10
Rh2(OOct)4
Rh2(OOct)4 2.5
5
8
9
Rh2(OOct)4
Rh2TMA4
1
10
10
11
12
13
Rh2(OAc)2 10
Rh2TFA4
Pd(OAc)2
Cu(acac)2
10
10
10
10
11
12
1
5
5
0
10
a Measured by internal standard (1,3,5-trimethoxy benzene) in 1H
NMR analysis of crude reaction mixture.
a Measured by internal standard (1,3,5-trimethoxy benzene) in 1H
NMR analysis of crude reaction mixture.