2
Y. Zhao et al. / Tetrahedron Letters xxx (2013) xxx–xxx
Table 2
OH
Cl
O
O
O
O
cat.
Optimization of reaction conditions for ring opening of epichlorohydrin with acetic
acid under solvent free conditiona
O
Cl
OH
Cl
O
heat
OH
Entry FeCl3/
pyridine
T (°C)
Time
(h)
Conversionb
(%)
Regioisomeric
1a
2a
3a
4a
ratio (3a:4a)b
(mol %)
Scheme 1. Ring opening of epichlorohydrin with acetic acid.
1
0.5/0.5
0.5/0.5
0.5/0.5
0.5/0.5
0.05/0.05
0.125/0.125
0.5/0.5
0.5/0.5
1.0/0.25
1.0/0.5
1.0/0.5
1.0/1.0
2.0/0
1.25/1.25
1.25/1.25
2.5/2.5
40
17
89
14.2
6.0
6.1
2c
3
40 + 80 17 + 12 100
60 17 100
60 + 80 17 + 12 100
4c
5
6
7
8
6.0
40
40
40
40
40
40
40
40
40
40
40
40
40
50
50
50
50
50
50
24
24
12
46
12
12
20
12
12
12
24
12
36
24
24
12
12
12
12
19
38
55
96
89
92
96
83
86
91
98
94
99
77
94
94
94
99
99
20.0
18.0
15.0
8
11.6
10.9
7.8
Table 1
Screening of catalysts for ring opening of epichloro-hydrinwith acetic acid under
solvent free conditions
Entry Catalyst
Substrate ratio Conversionc
Regioisomeric
9
(1a:2a)
(%)
ratio (3a:4a)c
10
11
12
13
14
15
16
17
18
19
20
21
22
23
1a
2a
3a
4a
5a
6a
7a
8a
9a
10b
LiClO4
MgBr2
LiCl
CeCl3
Ca(OTf)2
Pyridine
FeCl3
Fe(TFA)3
Fe(O2CC5H12
FeCl3/
1:1
1:1
1:1
1:1
1:1
1:1
1:1
1:1
1:1
1.05:1
18
7.5
6.6
7.0
8.0
6.6
7.7
8.5
10.8
5.9
5.5
9.4
42
25
13
27
60
80
93
81
97
11.3
11.0
8.5
10.0
6.7
7.0
7.7
11.0
11.4
8.2
2.5/2.5
0.25/0.25
0.375/0.375
0.5/0.5
1.0/0.25
1.0/0.5
)
3
pyridine
FeCl3/
pyridine
FeCl3/
11b
12b
1:1
100
99
5.3
5.6
1.25/1.25
7.6
1:1.05
a
Reactions were carried out by employing 50.0 mmol epichlorohydrin and
pyridine
52.5 mmol acetic acid under solvent free condition.
b
a
Determined by GC.
Acetic acid (50.0 mmol) was treated with epichlorohydrin (50.0 mmol) in the
presence of catalysts (1.0 mol %) at 60 °C under solvent free condition for 12 h.
c
Continuation of the previous reaction, that is, next 12 h at 80 °C after 17 h at
b
40 °C.
Reactions were carried out by employing 50.0 mmol substrate as 1 equiv in the
presence of FeCl3/pyridine (0.5 mol %/0.5 mol %) at 60 °C in absence of solvent for
12 h.
c
Determined by GC and 1H NMR.
O
OH
Cl
O
O
O
cat.
O
Cl
O
OH
2a
heat
ClH
O
OH
Various common catalysts were screened (Table 1). While Lith-
ium, Magnesium, Cerium, and Calcium salts (Table 1, entries 1–5)
exhibit low catalytic capability, pyridine was found to have modest
efficiency (Table 1, entry 6). Various Ferric salts were identified to
possess higher catalytic efficiency (Table 1, entries 7–9). However,
Fe(TFA)3 was observed to generate more impurities judged by GC
3a
4a
1a
Cl
O
OH
and 1H NMR. FeCl3 and Fe(O2CC5H12 3
) were found to give almost
Scheme 2. Acetyl migration during opening of epoxide rings with acetic acid.
identical conversion and relatively clean product. FeCl3 was also
identified to provide better selectivity, and was selected for further
optimizations.
the regioselective nucleophilic attack of HOAc to the less hindered
side to generate 3a in good selectivity. At an elevated temperature,
more regioisomer 4a was generated not only from the increased
nucleophilic attack to the more hindered side, but also from the
acetyl migration from the initially formed 3a through a five-mem-
bered ring transition state and then reached a balance at a certain
ratio. The acetyl migration might be promoted by pyridine.15
For further optimizations, reactions with various catalysts ratio/
loading were carried out as well. As a general trend, with increased
catalytic loading, enhanced conversion with sacrifice of selectivity
was noticed. When the reactions were carried out at 40 °C under
low catalytic loading (<1 mol %), long reaction time was required
to reach good conversion (Table 2, entries 5–8). Higher catalyst
loading (Table 2, entries 9–17) led to improved conversion (Table 2,
entries 15 and 17). At 50 °C the reaction rate was significantly in-
creased (Table 2, entries 18–23). Complete conversion was accom-
plished within 12 h (Table 2, entries 22 and 23). The best
conversions identified were: 1.0 equiv of epoxide to react with
1.05 equiv of HOAc in the presence of FeCl3/pyridine (1 mol %/
0.5 mol %) at 50 °C for 12 h (Table 2, entry 22).
Under various conditions, FeCl3 alone could not drive to full
conversion even under prolonged reaction time and elevated tem-
perature with conversion at most to 80%.10h With the knowledge
that pyridine shows a modest catalytic activity, we expected that
the FeCl3/pyridine combination would be ideal partners to act as
acid–base dual-activation catalysts because either one is effective
and tolerable to each other. To our delight, FeCl3/pyridine effi-
ciently catalyzed the opening of epoxide and complete conversion
could be reached (Table 1, entries 10–12) in model reaction.
During the initial screening, it was observed that regioselectiv-
ity was affected by the ratio of the reactants (Table 1, entries 10–
12). Significant efforts for optimization were taken and the results
are summarized in Table 2. It was discovered that lower reaction
temperature, for example, 40 °C for 17 h provided improved selec-
tivity (14.2) with 89% conversion (Table 2, entry 1). Under elevated
temperature, full conversion could be reached, however the selec-
tivity dropped to 6 (Table 2, entries 2–4).
The diminished selectivity from 14.2 in 89% conversion at 40 °C
to 6.0 in full conversion with continuous heating at an elevated
temperature (80 °C) suggested that acetyl transfer process oc-
curred during the reaction (Scheme 2). Low temperature favors
With the optimized conditions in hand, the scope of this reac-
tion was further explored with a range of epoxides and carboxylic