Chemistry Reference
In-Depth Information
Tab l e 7 . 3 A summary of rhodium catalysts and their activities.
Inter-
Intra-
p (CO)
Entry
PKR
PKR
Catalyst system
[atm]
TON a
Ref.
X
1
[Rh(dppp) 2 Cl] b
0
(11-20)
16
X
2
[Rh(dppp) 2 Cl] c
0
(7-10)
15
X
3
[Rh(COD)Cl] 2 +
( S )-P-Phos c
0
(8-15)
24
X
4
[Rh(COD)Cl] 2 +
( S )-BisbenzodioxanPhos c
0
(10-16)
25
X
5
[Rh(COD)Cl] 2 +
( S )-xyl-BINAP d
0
(1-7)
32
X
6
[Rh(COD)Cl] 2 +
dppp e
0
(3-15)
37
X
7
[Rh(COD)Cl] 2 +
dppp f
0
(3-7)
36
X
8
[Rh(COD)Biphemp]X g X
=
BF 4 ,PF 6 ,OTf
0
(16-25)
8
X
9
[Rh(COD)Cl] 2 +
dppp
+
TPPTS
+
SDS h
0
(6-9)
20
10
X
[Rh(COD)Cl] 2 i
5
(7-9)
6
√√ [Rh(CO) 2 Cl] 2
11
1
(4-6) (7-28)
5
12
X
[Rh(CO) 2 Cl] 2 +
( R )-SIPHOS
1
(5-12)
13
[Rh(CO)(dppp)Cl] 2 j
13
X
1
(7-15)
38
14
X
[Rh(CO) 2 Cl] 2 +
( S )-BINAP
1
(6-16)
4
[Rh(CO) 2 Cl] 2 k
15
X
1
(3-10)
9
a TONs calculated with respect to the number of moles of Rh 1 , TONs in parentheses are turnover numbers of intramolecular
PKR
b Using pentafluorobenzaldehyde as CO source
c Using cinnamaldehyde as CO source under conventional heating
d Using benzylformate as CO source under conventional heating
e Using cinnamaldehyde as CO source under microwave irradiation
f Using p-chlorobenzylformate as CO source under microwave irradiation
g Using 4 A M.S. entrapped with CO
h Using formaldehyde as CO source in aqueous medium
i Rh catalyst entrapped by silica-sol gel
j Under an (Ar:CO) atmosphere, demonstrating the effects of CO pressure on product yields
k Under 1 atm (Ar:CO
=
10:1) atmosphere
Intramolecular Ir-catalyzed PKR
R'
Ph
10 mol% [Ir(cod)Cl] 2
R'
20 mol% ( S )-tol-BINAP
Z
R
Z
O
O
O
Toluene, reflux
CO (1 atm)
*
*
R
Me
R=HorMe
R' = aryl, alkyl
Z = O, NTs, C(COOEt) 2
CO (1 atm): 88% ee (30% yield)
CO (0.2 atm): 93% ee (86% yield)
82-98% ee
51-85% yield
Intermolecular Ir-catalyzed PKR
O
O
10 mol% [Ir(cod)Cl] 2
20 mol% ( S )-tol-BINAP
Ph
Me
+
+
Ph
Me
Toluene, reflux
CO (1 atm)
Me
Ph
A 93% ee
B
Excess
32% yield ( A:B =>10:1)
Scheme 7.25 Asymmetric Ir-catalyzed intra- and intermolecular PKR.
 
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