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Table 1: Influence of the ruthenium catalyst on the hydrogenation of
aldehyde A1.[a]
obtained with complete conversion and chemoselectivity and
isolated in high yield (ꢀ 98%).
Entry Ruthenium complex[b]
T
t
Conv. Yield
The catalytic results reported in Table 3 support the
general efficiency of the biscarboxylate complexes of type 3 in
the selective base-free hydrogenation of aldehydes; nearly no
heavy by-products were formed under these conditions. The
catalyst [(en)(dppe)Ru(OCOtBu)2] (3 f) proved to be highly
selective (ꢀ 98%) in the presence of tetra- and trisubstituted,
E, and gem-disubstituted alkenes as well as epoxides, which
remained intact, and aldehydes A1–7 were reduced with high
efficiency to the desired alcohols at 1008C under hydrogen
(10–50 bar) with TONs of 40000–100000. Even the sterically
hindered aldehyde A4 could be hydrogenated at a ruthenium
loading of just 0.002 mol% to afford the desired alcohol with
nearly no alkene hydrogenation or isomerization nor epime-
rization at the a position (99.5% selectivity). In the case of
substrates containing terminal or Z-disubstituted alkenes,
such as A8 and A9, we applied slightly different conditions to
maintain high chemoselectivity (90 and 95%, respectively).
Because of the absence of an acidic cocatalyst (to minimize
alkene isomerization) and the lower reaction temperature,
a higher catalyst loading was required (0.01 mol%). The
reactions also needed to be stopped right upon completion to
avoid a noticeable decrease in selectivity. The complex
[(en)(dppe)Ru(OCO(1-adamantyl))2] (3g), which displayed
[8C] [h][c] [%][d] [%][e]
1
2
trans-[Ru(H)(BH4)(S-binap)(S,S-dpen)] 30 24
(1a)
trans-[Ru(H)(BH4)(S-binap)(S,S-dpen)] 100 24
(1a)
12
15
12
14
3
4
5
6
7
8
9
trans-[Ru(H)(BH4)(dppe)(en)] (1b)[f]
[(en)(dppe)Ru(OCOMe)2] (3a)
[(en)(dppe)Ru(OCOCF3)2](3b)
cis-[(en)(dppe)Ru(OCOtBu)2] (3c)
trans-[(en)(dppe)Ru(OCOtBu)2] (3d)
[(en)(dppe)Ru(OCOPh)2] (3e)
[(en)(dppe)Ru(OCOPh)2] (3e)
100 24
100 24
100 24
14
10
8
13
10
7
100 8.5 100 >99
100
100
8
6
100 >99
100 >99
0
30 24
[a] Reaction conditions: aldehyde A1 (0.05 mol), catalyst (0.01 mol%),
iPrOH (13 mL), H2 (50 bar: maintained throughout the reaction).
[b] binap=2,2’-bis(diphenylphosphanyl)-1,1’-binaphthyl, dpen=1,2-
diphenyl-1,2-diaminoethane, en=ethylenediamine, dppe=1,2-bis(di-
phenylphosphanyl)ethane. [c] The time required for the reaction to reach
completion was determined by H2 consumption. [d] Conversion was
measured by GC. [e] After solvent removal and bulb-to-bulb distillation,
the reaction yield was determined on the basis of product purity by GC.
[f] Complex 1b was synthesized according to the procedure described by
Noyori and co-workers.[7]
and 1b, the pivalate and benzoate derivatives 3c–
e (isomers 3c and 3d were separated by crystalliza-
tion) displayed much higher catalytic activity, with
complete conversion in 6–8.5 h. The desired unsatu-
rated primary alcohol was then isolated in nearly
quantitative yield: we did not detect the formation of
heavy by-products or the hydrogenation of either of
the two alkene groups in the substrate. Although
previously reported ruthenium base-free systems
had been reported to be active at room temper-
ature,[7,8] a higher reaction temperature was gener-
ally required when the biscarboxylate complexes
were used as catalysts.
In attempts to further improve these results, we
found that the reaction is usually most efficient in
apolar aprotic solvents, such as heptane. We then
discovered that the catalytic efficiency could be
further increased significantly by carrying out the
hydrogenation in the presence of catalytic amounts
of carboxylic acids. Turnover numbers (TONs) up to
Table 2: Influence of the carboxylic acid additive on the hydrogenation of aldehyde
A1.[a]
Entry
Carboxylic acid
t
Conv.
[%][c]
Yield
[%][d]
Remarks[e]
[h][b]
1
2
3
4
5
6
7
8
9
none
48
48
24
24
20
20
12
8
2
n.d.
98
3-methylbutanoic acid
2,4,6-trimethylbenzoic acid
isobutyric acid
3,3-dimethylbutanoic acid
1-adamantanecarboxylic acid
pivalic acid
100
100
100
100
100
100
100
100
25% at 6.5 h
65% at 6.5 h
70% at 6.5 h
75% at 6.5 h
75% at 6.5 h
87% at 6.5 h
95% at 6.5 h
>99
>99
>99
>99
>99
>99
>99
benzoic acid
2-naphthoic acid
6.5
[a] Reaction conditions: aldehyde A1 (0.1 mol), catalyst 3a (0.0025 mol%),
carboxylic acid (2.5 mol%), heptane (30 mL), 1008C, H2 (50 bar: maintained
throughout the reaction). [b] The time required for the reaction to reach completion
was determined by H2 consumption. [c] Conversion was measured by GC. [d] After
solvent removal and bulb-to-bulb distillation, the reaction yield was determined on
the basis of product purity by GC; n.d.=not determined. [e] Partial conversion was
40000 and turnover frequencies (TOFs) up to determined on the basis of H2 consumption.
6153 hÀ1 were then observed at complete conversion
in the hydrogenation of the same aldehyde A1 even
with the poorly active bisacetate complex 3a (Table 2).
Whereas the catalytic activity generally increased with the
steric hindrance of the aliphatic carboxylic acid cocatalyst, in
analogy with the trend observed for the carboxylate ligand,
we observed the reverse tendency between 1-adamantane-
carboxylic acid and pivalic acid (Table 2, entries 6 and 7). In
the case of aromatic cocatalysts, highly bulky 2,4,6-trimethyl-
benzoic acid also proved to be inferior to both benzoic acid
and 2-naphthoic acid, which were the most effective cocata-
lysts tested at a 2.5 mol% loading (< Table 2). Under these
mildly acidic conditions, the unsaturated primary alcohol was
higher catalytic activity under such conditions, was used in
these two cases. With a,b-unsaturated aldehyde substrates,
such as A10–12, the catalyst [(en)(Xantphos)Ru(OCOtBu)2]
(3h) was generally used to promote high chemoselectivity (ꢀ
96%) and thus avoid further reduction of the allylic alcohol
formed. Although substrates of this type are often less
sensitive to basic conditions, the desired products were
obtained with complete conversion at catalyst loadings of
0.0025–0.005 mol% and isolated in higher yields than those
observed for reactions carried out under classical basic
conditions.[6,18]
2
ꢀ 2013 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2013, 52, 1 – 5
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