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X. Shen et al. / Tetrahedron Letters 54 (2013) 3937–3939
Table 1
up to 68% (Table 3, entries 1–9), whereas electron poor amines
2k–m were inactive under the reaction condition (Table 3, entries
10–12). Secondary amine 2n reacted smoothly with 1 to give 3n
without formation of any undesired products (Table 3, entry 13).
To better understand the behaviors of the catalyst, some exper-
iments were consciously designed and conducted. Firstly, in order
to examine whether Bronsted acids are effective on the reaction,
hydrochloric acid (10% aq), trifluoromethanesulfonic acid, aniline
hydrochloride, and N,N-dimethylaniline hydrochloride were,
respectively, used with a catalytic loading (2 mol %) to catalyze
the reaction of 1 with 2a in toluene at 20–60 °C. The former two
reactions stopped soon after the initial hour and just generated
inseparable mixtures containing very low contents of 3a. However,
isolatable 3a was obtained in yields of 31% and 35% in aniline
hydrochloride and N,N-dimethylaniline hydrochloride-catalyzed
The catalyst screening for the hydroamination of 2,5-dihydrofuran (1) with aniline
(2a)
H
NH
2 catalyst
N
O
OH
2a
1
3a
Entry
Catalyst
Conditions
Conversiona (%)
Yieldb (%)
1
FeCl3
AlCl3
HfCl4
Zn(CF3SO3)2
ZnCl2
CuCl
CuI
Pd(PPh3)4
Pd(OAc)2
RhCl3
10 h, 25 °C
10 h, 25 °C
10 h, 25 °C
10 h, 25 °C
24 h, 25 °C
24 h, 60 °C
24 h, 60 °C
10 h, 60 °C
10 h, 60 °C
10 h, 25 °C
42
28
75
70
45
17
10
0
27
20
45
49
22
0e
0e
0
2c
3d
4
5
6
7
8d
9d
10
reactions, respectively. Second,
1 was directly treated with
23
15
0e
0e
Zn(CF3SO3)2 at 60 °C for 6 h in an anhydrous argon atmosphere
to examine whether it was effective to catalyze the ring-cleavage
of 1 or the isomerization of 1 to 2,3-dihydrofuran. After that treat-
ment, the mixture was carefully distilled and only one fraction was
collected, which was proved to be the material itself having purity
more than 99% based on GC analysis. So we deduce that the forma-
tion of 3a should not be only ascribed to Zn(II) itself and a proton-
induced and Zn(CF3SO3)2-assisted mechanism is proposed as
shown in Scheme 1. The interaction between aniline and
Zn(CF3SO3)2 generates an ammonium salt. The protonation of the
complex of 1 by the ammonium salt gives a carbon cation interme-
diate (4). Compound 4 is attacked by aniline and a domino type
ring cleavage is induced with the help of Zn(CF3SO3)2 to afford 6.
The elimination of LH from 6 produces the target product 3a as
well as Zn(II) catalyst to complete a catalytic cycle. As a good leav-
ing group, the anion takes an important role in the reaction to im-
prove the efficiency. Zn(II)-catalyst may also be helpful to the
a
b
c
Conversion of 2a determined by HPLC.
Isolated yield of 3a.
CH2Cl2 as the solvent.
Experiment was conducted under strict anhydrous and oxygen-free condition.
3a was observable in TLC but inseparable due to its low content.
d
e
Returning to the catalyst screening question, among the seven
Lewis acids, only HfCl4 and Zn(CF3SO3)2 gave comparably inspiring
results (Table 1, entries 3 and 4). When FeCl3, AlCl3, and ZnCl2 were
used, lowered yields of 3a were obtained (Table 1, entries 1, 2, and
5). While Cu(I) catalysts were employed in the reaction under a
more drastic condition, no 3a was isolated for its low contents
(Table 1, entries 6 and 7). Pd(PPh3)4 and Pd(OAc)2 showed no
activation on the reaction though the temperature was raised to
60 °C (Table 1, entries 8 and 9). While RhCl3 was used (Table 1,
entry 10), an inseparable mixture was obtained but no 3a was
found. Based on the results, Zn(CF3SO3)2 is clearly the most
suitable since it is less expensive and gives a reasonable yield of
3a requiring no strict anhydrous and oxygen-free condition.
The solvent and temperature factor were then examined with
Zn(CF3SO3)2 as the catalyst (shown in Table 2). Toluene was found
to be the best solvent in which 49% yield of 3a was achieved
(Table 2, entry 1). Other solvents such as methanol, N,N-dimethyl-
formamide (DMF), acetonitrile, tetrahydrofuran (THF), and
dichloromethane were not suitable for this conversion (Table 2,
entries 4–9). The reaction temperature was also examined when
toluene was used. Raising temperature is not useful but harmful
to the yield. When the reaction was conducted under 150 °C in a
sealed tube, just an inseparable mixture was produced containing
only a trace of 3a according to the TLC analysis (Table 2, entry 3).
A series of aromatic amines were then examined for the amina-
tion-ring cleavage feasibility (Table 3). The catalytic system
worked well with primary amines 2b–j to afford 3b–j with yields
reaction for the weakening of p–p conjugation between oxygen
and carbon cation in 5 and thus inhibiting or partially inhibiting
the isomerization of 4 to 5. The reaction could not be induced by
Pd(PPh3)4 and Pd(OAc)2 because no active proton was generated
there, while RhCl3 could interact with 2a to produce active proton,
the reaction did take place though the selectivity of 3a is almost
zero.
Table 3
Zn(CF3SO3)2–catalyzed hydroamination-ring cleavage of 2,5-dihydrofuran with aro-
matic amines
R1
H
N
N
R1 Zn(CF3SO3)2
+
OH
toluene
O
1
R
R
2
3
Entry
2
3
Conditions
Yielda (%)
1
2
3
4
5
6
7
8
2b, R = 2-Me, R1 = H
2c, R = 3-Me, R1 = H
2d, R = 4-Me, R1 = H
2e, R = 4-OMe, R1 = H
2f, R = 2,6-Me2, R1 = H
2g, R = 3,5-Me2, R1 = H
2h, R = 2-Et-6-Me, R1 = H
2i, R = 4-OCF3, R1 = H
2j, R = 4-Cl, R1 = H
3b
3c
3d
3e
3f
3g
3h
3i
8 h, 25 °C
8 h, 25 °C
8 h, 25 °C
8 h, 25 °C
6 h, 25 °C
6 h, 25 °C
6 h, 25 °C
6 h, 25 °C
10 h, 25 °C
24 h, 60 °C
24 h, 60 °C
24 h, 60 °C
6 h, 25 °C
61
58
55
59
64
66
68
63
45
0
Table 2
The condition optimization of the reaction of 1 and 2a in the presence of Zn(CF3SO3)2
Entry Solvent
Temperature (°C) Time (h) Conversiona (%) Yield (%)
1
2
3
4
5
6
7
8
9
Toulene
Toulene
25
60
10
10
1
70
77
73
17
14
51
45
40
27
49
40
Toulene 150
––b
––b
––b
38
9
3j
MeOH
DMF
CH3CN
THF
Dioxane
CH2Cl2
25
25
25
25
25
25
10
24
10
10
10
10
10
11
12
13
2k, R = 4-NO2, R1 = H
2l, R = 3-NO2, R1 = H
2m, R = 2-COOMe, R1 = H
2n, R = H, R1 = Me
––b
––b
––b
3n
0
0
33
65c
32
––b
a
b
c
Isolated yield of 3.
No reaction.
Without side product.
a
Conversion of 2a determined by HPLC.
Inseparable due to the low content of 3a.
b