Table 1 Stereoselective hydrogenation of 1 with 4 and 5a,b as catalysts in various two-phase systemsa
Selectivity (S)
cis-hex-3-enoic trans-hex-3-enoic
TOF/h2
1
Entry
Solvent system
Catalyst
2
p(H )/bar Conv. 1 (%)
acid 2 (%)
acid (%)
n
1
2
MeNO
MeNO
2
–Bu
–Bu
2
O
O
4
60
60
60
10
60
16
45
95
94
78
68
85
93
66
86
96
71
96
6
34
7
1
29
3
3.1
92
300
97
580
1057
n
2
2
5a
5a
5a
5a
5b
b
3
4
Ethylene glycol–MTBE
Ethylene glycol–MTBE
Sulfolane–MTBE
MTBE
b
5
6
c
a
Reagents and conditions: 60 °C; 20 mmol sorbic acid; 0.06 mmol catalyst; catalyst phase: 30 ml solvent; nonpolar product phase: 44 ml solvent; Conv.
b
=
2
conversion; selectivity (S) = (n(product)/∑n (all products)) 3 100; TOF = turnover frequency = (∑n (all products))/(n(catalyst) h).; Some trans-hex-
-enoic acid is formed: (3) S = 7%, (4) 3%. c 40 mmol sorbic acid, 75 ml MTBE, 50 °C.
Table 2 Stereoselective hydrogenation of sorbic alcohol with 5a as catalyst in ethylene glycol–MTBEa
Conv. sorbic
alcohol (%)
Selectivity to leaf
alcohol 3 (%)
Entry
T/°C
2
p(H )/bar
n (5a)/mmol
t/h
TOF/h2
1
1
2
3
4
21
40
60
60
20
20
20
4
0.0424
0.0426
0.0219
0.0428
1.5
44
70
88
86
98.3
98.9
98.6
97.8
184
1055
2495
714
0.42
0.40
0.77
a
Reagents and conditions: 25–27 mmol sorbic alcohol; 25 ml ethylene glycol; 45 ml MTBE; in each experiment 1–2% trans-hex-3-en-1-ol is formed.
Conv. = conversion; selectivity = (n(product) / ∑n (all products)) 3 100; TOF = turnover frequency = (∑n (all products))/(n(catalyst) h).
The highest selectivities (S) (S(cis-hex-3-enoic acid) = 96%)
were obtained in ethylene glycol when the hydrogen pressure
Notes and references
‡
The complexes were synthesized in an argon atmosphere with dried
was reduced from 60 to 10 bar.
solvents. Before the hydrogenation experiments the solutions of the
complexes and the substrates were handled under argon.
The highest activities with 5a as catalyst (TOF = 580 h21)
were obtained in sulfolane, but the selectivity was not as high as
in ethylene glycol.
General procedure for the synthesis of 5a,b: 2.94 mmol [(Cp*Ru(m-
2 2 2
OMe)) ], which was prepared from 2.94 mmol [(Cp*RuCl ) ] according to
Since the BARF anion is much more lipophilic than the
triflate anion, complex 5b is more soluble in nonpolar solvents
than 5a. For this reason 5b was used as catalyst in an MTBE
solution instead of using it in a two-phase system. Experiments
the procedure described in the literature,6b were dissolved in 30 ml
dichloromethane and 10 ml diethyl ether. A solution of 3.44 mmol sorbic
acid and 3.15 mmol triflic acid (or HBARF) in 12 ml diethyl ether was
added to the stirred solution of the complex at 278 °C. The reaction mixture
changed immediately from deep red to brown. The reaction mixture was
stirred for 10 min at 278 °C and was slowly brought to room temperature.
After being stirred for a further 5 min at room temperature, the solvent was
evaporated under reduced pressure. The residue was treated with 10 ml ethyl
acetate to effect formation of an orange solid. For a better precipitation, 10
ml diethyl ether were added. The solid was filtered off washed twice with
10 ml diethyl ether and dried in high vacuum. 2.11 mmol 5a were obtained
5
and 6 in Table 1 can be compared because they both have been
carried out in one-phase systems at the same reaction tem-
perature. Evidently, 5b is a more active catalyst than 5a because
the BARF anion has much weaker coordinating properties than
7
the triflate anion. Thus, the BARF anion does not compete with
sorbic acid and hydrogen for free coordination sites at the
ruthenium center in the catalytic steps of the reaction.
(71.7% yield based on [(Cp*RuCl
§ Crystal data for C56
2.648(6), b = 14.323(3), c = 16.711(6) Å, a = 78.23(2), b = 80.09(3), g
2
)
2
]).
We also used hexa-2,4-diene-1-ol (sorbic alcohol) as sub-
strate, which can be directly hydrogenated to cis-hex-3-ene-1-ol
H51BF24
O
4
Ru 5b: M
r
1355.87, triclinic, a =
1
=
3
¯
84.53(3)°, V = 2914(2) Å , T = 203 K, Z = 2, space group P1 (no. 2),
3
(leaf alcohol). Preliminary results have shown that the
21
m(Mo-Ka) = 3.80 cm , 12258 independent reflections measured (Rint
0
=
catalytic hydrogenation is much faster with sorbic alcohol than
with sorbic acid. It was thus possible to reduce the hydrogen
pressure from 60 to 20 bar in the experiments shown in Table
2
.032). The final wR(F ) = 0.1497 (all data). The structure was solved
2
using direct methods and refined by full matrix least squares on F . Single
crystals of [Cp*Ru(m-O-(h:s-cis-2,3,4,5-Me(CH) CO(OH)))] [B(C
CF -3,5) ·4THF 5b were crystallized from THF–dibutyl ether and
4
2
6 3
H -
2.
(
)
3 2
4 2
]
The best results were obtained with 5a, which hydrogenates
washed with pentane.
CCDC 182/1513.
2
1
sorbic alcohol with a TOF of ca. 2500 h at 60 °C in the two-
phase system ethylene glycol–MTBE. Even at low hydrogen
pressures of 4 bar, which allows working in glassware reactors,
1
2
S. Arctander, Perfume and Flavour Chemicals II, Montclair, USA,
969.
(a) M. Cais, E. N. Frankel and A. Rejoan, Tetrahedron Lett., 1968, 1919;
b) E. N. Frankel, E. Selke and C. A. Glass, J. Am. Chem. Soc., 1968, 90,
1
2
1
the reaction rate stays fairly high (TOF = 714 h ). The very
high selectivity (98–99%) to leaf alcohol is virtually independ-
ent of the reaction temperature, while the hydrogenation activity
raises as expected with increasing temperature. Other than in
hydrogenations of sorbic acid the selecivity depends negligibly
on the conversion. While the selectivity to cis-hex-3-enoic acid
often decreases at conversion rates of > 90%, the selectivity to
cis-hex-3-enoic alcohol remains constant even at 100% con-
version.
(
2446; (c) A. Furuhata, K. Onishi, A. Fujita and K. Kogami, Agric. Biol.
Chem., 1982, 46, 1757; (d) A. A. Vasil’ev and E. P. Serebryakov,
Mendeleev Commun., 1994, 4.
3
J. Heinen and B. Drießen-Hölscher, J. Organomet. Chem., 1998, 570,
1
41.
4
5
J. Heinen, Ph.D. Thesis, 1997, RWTH-Aachen.
P. J. Fagan, W. S. Mahoney, J. C. Calabrese and I. D. Williams,
Organometallics, 1990, 9, 1843.
We have thus shown that the concept of using ‘naked’ Cp*Ru
complexes for stereoselective hydrogenations of functionalized
dienes to cis-olefins is successful. In further work we will try to
elucidate the mechanism and the kinetics of the reaction.
We thank the Bundesministerium für Bildung und Forschung
and the Ministerium für Wissenschaft und Forschung des
Landes NRW (Katalyseverbund NRW) for financial support.
6
(a) U. Kölle and J. Kossakowski, J. Chem. Soc., Chem. Commun., 1988,
5
49; (b) U. Kölle and J. Kossakowski, J. Organomet. Chem., 1989, 362,
383.
7 G. M. DiRenzo, P. S. White and M. Brookhart, J. Am. Chem. Soc., 1996,
118, 6225.
Communication a909355i
218
Chem. Commun., 2000, 217–218