COMMUNICATION
Table 1. Influence of iron on catalytic b-boration of ethylcrotonate.[a]
AHCTUNRTGEG(NNNU cod)2 (cod= cycloocta-l,5-
diene),[11] under the standard
conditions of the iron-mediated
reactions. In these reactions,
NaOtBu was used as a base in
the stock solutions because of
its high solubility in tetrahydro-
furan (THF; Table 3, entries 1–
3, 9, and 10). In subsequent ex-
periments, we gradually de-
creased the concentration of
the “in situ” formed, base-acti-
vated copper and nickel com-
Entry
Iron system
Fe(acac)2
FeCl2
Fe(OMe)2
(acac)3
(acac)2
(acac)2
(acac)2
(acac)2
(acac)2
(acac)2
Cs2CO3 [mol%]
PPh3 [mol%]
T [8C]
t [h]
Conv. [%][b]
1
2
3
4
5
6
7
8
U
3
3
3
3
3
–
–
–
–
4
4
4
4
4
4
4
–
70
70
70
70
70
70
70
70
45
25
70
70
6/24
6
6
6
6/24
6
6
6
6
6
42/80
60
15
56
26/99
73
87
99
54
21
G
Fe
Fe
Fe
Fe
Fe
Fe
Fe
E
N
R
6
N
12
15
15
15
15
15
T
9
R
10
11
12
C
–
–
6
6
54
45
[a] Standard conditions: ethylcrotonate/bis(pinacolato)diboron/Fe complex=0.5:0.55:0.01. Fe/PPh3 =1:2.
Cs2CO3: mol% with respect to the substrate, MeOH: (2.5 mol%). Solvent: THF (2 mL). [b] Determined by
G.C.
plexes from 5ꢄ10À3
m
to 5ꢄ
and
10À6 m.
Both CuCl
CuOTf·4CH3CN form consider-
ably more active catalysts than
served in the Fe
G
(acac)2 when applied in the same concentration, 5ꢄ10À3
FeACHTUNRGTNEGNU m
sired b-borated product in quantitative yield (Table 2, en-
tries 2–4). Importantly, the PPh3/Cs2CO3 organocatalytic
system was not able to promote the b-boration of the imine
substrate (Table 2, entry 5).
(Table 2, entries 1–3). The higher activity is even more obvi-
ous when the catalyst concentration is decreased by one
magnitude, to 5ꢄ10À4 m (S/Cu=500), and the substrate is
still quantitatively converted into the product (Table 2,
entry 4). Further decreasing the concentration of the copper
Recent evidence about the role of metal impurities in
“iron-mediated” reactions[9] prompted us to carefully exam-
complex, the conversion quickly diminishes: at 5ꢄ10À5
m
copper concentration only 5%
of the product can be observed,
and at 5ꢄ10À6 m concentration,
the substrate remains intact.
Under the optimized conditions
for the iron-mediated b-bora-
tion reactions, nickel complexes
are much less active than the
copper catalysts (Table 2, en-
tries 9 and 10). Both NiCl2 and
Table 2. Influence of iron on catalytic b-boration of (E)-1-phenyl-N-(4-phenylbutan-2-ylidene)methanamine.[a]
Entry
Iron system
Cs2CO3 [mol%]
PPh3 [mol%]
T [8C]
t [h]
Conversion [%][b]
1
2
3
4
5
Fe
Fe
Fe
Fe
N
15
3
9
15
15
–
4
4
4
4
70
70
70
70
70
6
6
6
6
6
28
32
74
99
–
–
[a] Standard conditions: (E)-1-phenyl-N-(4-phenylbutan-2-ylidene)methanamine/bis(pinacolato)diboron/Fe
complex=0.5:0.55:0:01. Fe/PPh3 =1:2. Cs2CO3: mol% with respect to the substrate, MeOH: (2.5 mol%). Sol-
1
vent: THF (2.5 mL). [b] Determined by H NMR spectroscopy.
Ni
ACHTUNGRTEN(NUNG cod)2 provided incomplete
conversions when applied in the
ine the possible effect of traces of transition metals in our
iron precursors. As a matter of fact, the Fe(acac)2 catalyst
concentration of the iron precursor, and decreasing the con-
centration by one magnitude resulted in complete inactivity.
AHCTUNGTRENNUNG
precursor received from Sigma–Aldrich (99.95%) reported-
ly contains copper and nickel impurities in 6.1 and 43.0 ppm
concentrations, respectively. Phosphine complexes of copper
and nickel are well-known catalysts for b-boration of acti-
vated olefins.[5,6] No other metals, known to be active in b-
boration of a,b-unsaturated carbonyl compounds, such as
platinum, rhodium, and palladium were listed in the quality
certificate of the product. Under standard reaction condi-
tions, the concentration of the iron system is approximately
5ꢄ10À3 m (Table 1, foot note). Considering the heavy metal
impurities reported by the provider, the catalytic system
might contain “in situ” formed copper/phosphine, nickel/
phosphine complexes in 1.2ꢄ10À7 m and 9.2ꢄ10À7 m concen-
trations, respectively. To estimate the contribution of the im-
purities to the overall catalytic activity, we monitored the
conversion as the function of the phosphine-complex con-
centration for both copper and nickel. As a comparison, we
performed reactions using CuCl and CuOTf·4CH3CN[10] as
transition-metal precursors, as well as with NiCl2 and Ni-
Considering the high purity of the FeACTHNGUTRENU(NG acac)2 precursor
(99.95%), and the activity versus concentration profiles of
Table 3. Conversions in b-boration of ethylcrotonate with bis(pinacola-
to)diboron as the function of the concentration of copper and nickel, typ-
ical heavy metal impurities of the FeACTHNUTRGNEUNG
(acac)2 precursor.[a]
Entry
Precursor
Concentration [moldmÀ3
]
Conversion [%][b]
1
2
3
4
5
6
7
8
Fe(acac)2
CuCl
N
5ꢄ10À3
5ꢄ10À3
45
99
99
99
28
17
5
CuOTf·4CH3CN
CuOTf·4CH3CN
CuOTf·4CH3CN
CuOTf·4CH3CN
CuOTf·4CH3CN
CuOTf·4CH3CN
NiCl2
5ꢄ10À3
5ꢄ10À4
2.5ꢄ10À4
1.25ꢄ10À4
5ꢄ10À5
5ꢄ10À6
0
9
10
11
5ꢄ10À3
53
51
0
Ni
Ni
U
5ꢄ10À3
5ꢄ(10À4–10À6
)
[a] Standard conditions: ethylcrotonate=0.5 mmol, bis(pinacolato)dibor-
on=0.55 mmol, metal/PPh3/NaOtBu=1:2:5, T=708C, t=6 h. MeOH
(2.5 mol%). Solvent: THF (2 mL). [b] Determined by G.C.
1012
ꢃ 2011 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Chem. Asian J. 2011, 6, 1011 – 1014