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O
O
Catalyst
Conditions
CO 2 t -Bu
CO 2 t -Bu
PhCH 2 Br
+
*
Ph
24
25
Ph
OH
HO
Ph
26 (1 mol %)
K 2 CO 3
Toluene
0°C
44%, 50% ee ( R )
1d (5 mol %)
K 2 CO 3
Toluene
rt
97%, 46% ee ( S )
-
Br
OH
O
NH
HN
O
+
N
N
H
-
Br
26
1d
+
PPh 3
Ar
-
5f (1 mol %)
CsOH·H 2 O
Toluene
-40°C
94%, 97% ee ( S )
CF 3
Br
+
Ar =
N
CF 3
Ar
( S , S )- 5f
Scheme 2C.13.
Ar
O
O
O
4 (15 mol %)
CO 2 Et
27
CO 2 Et
+
ArF
Ar
+
CsOH
Toluene-CHCl 3 (9:1)
-20°C
CO 2 Et
28
29
O 2 N
NO 2
4c : 90%, 28 / 29 = 1.0:1
racemic for 28
: 89%, 28 / 29 = 16:1
80% ee for 28
Ar =
-
X
4d
+
H
N
OR
4c (R = Bn, X = Br)
4d (R = Bz, X = Cl)
N
Scheme 2C.14.
Jørgensen and others developed the catalytic, regio- and enantioselective nucleo-
philic aromatic substitution reaction between activated aromatic compounds and
1,3-dicarbonyl compounds under phase-transfer conditions. Interestingly, examination
on the addition of 2,4-dinitrofl uorobenzene to 2-carboethoxycyclopentanone 27 revealed
that the use of O - benzoylated cinchonidine - derived catalyst 4d was crucial for obtaining
C - arylated product 28 predominantly with high enantioselectivity (Scheme 2C.14 ) [35] .
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